EAEU HS code

8419 89 989 0 — Machinery, plant or laboratory equipment, whether or not electrically heated (excluding furnaces, ovens and other equipment of heading 8514), for the treatment of materials by a process involving a change of temperature such as heating, cooking, roasting, distilling, rectifying, sterilising, pasteurising, steaming, drying, evaporating, condensing or cooling, other than machinery or plant of a kind used for domestic purposes; instantaneous or storage water heaters, non-electric: other machinery, plant and equipment: other: other: other

Machinery, plant or laboratory equipment, whether or not electrically heated (excluding furnaces, ovens and other equipment of heading 8514), for the treatment of materials by a process involving a change of temperature such as heating, cooking, roasting, distilling, rectifying, sterilising, pasteurising, steaming, drying, evaporating, condensing or cooling, other than machinery or plant of a kind used for domestic purposes; instantaneous or storage water heaters, non-electric: other machinery, plant and equipment: other: other: other

Names come in English where the EU Combined Nomenclature publishes them — chapters, headings and subheadings, whose first six digits are the same Harmonized System; deeper EAEU detail is a machine translation, marked as such. Official texts — tariff notes, measures, lists and classification rulings — are the original: customs and your broker go by that wording. Where we show a machine translation of them, it is marked; where our quality check rejected one, the Russian stays.

Machine translation. The original is the Russian text of the EAEU tariff, and customs goes by it; this translation is for understanding only and has no legal force.

Duty rate

This is the base rate. A tariff quota, a preference for the country of origin and a tariff exemption lower it; anti-dumping and special duties are paid on top of it

EEC Council Decision No. 80 of 14.09.2021

Supplementary unit

шт

Item

Requirements and measures

Russian bans and restrictions2
Veterinary and sanitary control1
Conformity assessment7
Dual use6
EAEU non-tariff regulation2

None: trade defence measures — duty on top of the tariff, tariff quota.

Whether a measure applies to your goods depends on their characteristics and the shipping documents

VAT

VAT-exempt or 22%

Exempt if it is a medical device on the exemption list. Otherwise 22%.

Where it sits in the nomenclature

Section XVI. Machinery and mechanical appliances; electrical equipment; parts thereof; sound recorders and reproducers, television image and sound recorders and reproducers, and parts and accessories of such articles

84Nuclear reactors, boilers, machinery and mechanical appliances; parts thereof
8419Machinery, plant or laboratory equipment whether or not electrically heated (excl. furnaces, ovens and other equipment of heading 8514), for the treatment of materials by a process involving a change of temperature such as heating, cooking, roasting, distilling, rectifying, sterilising, pasteurising, steaming, drying, evaporating, vaporising, condensing or cooling (excl. those used for domestic purposes); instantaneous or storage water heaters, non-electric; parts thereof
8419 89Machinery, plant or laboratory equipment, whether or not electrically heated, for the treatment of materials by a process involving a change of temperature such as heating, cooking, roasting, sterilising, pasteurising, steaming, evaporating, vaporising, condensing or cooling, n.e.s. (excl. machinery used for domestic purposes and furnaces, ovens and other equipment of heading 8514)
8419 89 98Machinery, plant or laboratory equipment, whether or not electrically heated, for the treatment of materials by a process involving a change of temperature, n.e.s.
8419 89 989 0you are here

Compare the description of your goods with the neighbouring codes on the subheading line above.

Explanatory notes to heading 8419 11 paragraphs

Machine translation from Russian. The original is the EEC explanatory note, and that is what a classification dispute is argued from; the translation is for understanding and has no legal force.

8419 Machinery, plant or laboratory equipment, whether or not electrically heated (excluding furnaces, ovens and other equipment of heading 8514), for the treatment of materials by a process involving a change of temperature such as heating, cooking, roasting, distilling, rectifying, sterilising, pasteurising, steaming, drying, evaporating, condensing or cooling, other than machinery or plant of a kind used for domestic purposes; instantaneous or storage water heaters, non-electric: – Instantaneous or storage water heaters, non-electric: 8419 11 – – Instantaneous gas water heaters 8419 19 – – Other 8419 20 – Medical, surgical or laboratory sterilisers – Dryers: 8419 31 – – For agricultural products 8419 32 – – For wood, paper pulp, paper or paperboard 8419 39 – – Other 8419 40 – Distilling or rectifying plant 8419 50 – Heat exchange units 8419 60 – Machinery for liquefying air or other gases – Other machinery, plant and equipment: 8419 81 – – For making hot drinks or for cooking or heating food 8419 89 – – Other 8419 90 – Parts

This heading excludes: (a) domestic stoves, fireplaces, cookers, etc., of heading 7321; (b) air heaters and hot air distributors, non-electric, of heading 7322; (c) domestic appliances for cooking or heating food of heading 7418; (d) fractional distillation plant (e.g., in the production of heavy water) and rectifying plant, specially designed for the separation of isotopes, as well as isotopic exchange apparatus using the "dual temperature" method (heading 8401);

(e) steam or superheated water boilers (heading 8402) and their auxiliary plant (heading 8404); (f) central heating boilers of heading 8403; (g) industrial or laboratory furnaces and ovens, including furnaces for the separation of irradiated nuclear fuel by pyrometallurgical processes, and microwave ovens (heading 8417 or 8514, as the case may be); (h) refrigerating equipment and heat pumps of heading 8418; (ij) seed-germinating plant, incubators or brooders (heading 8436); (k) grain dampening machines (heading 8437); (l) diffusion apparatus for the extraction of sugar juices (heading 8438); (m) plant for the heat-treatment of textile yarns, fabrics or made up textile articles (e.g., yarn conditioners and singeing machines) (heading 8451); (n) apparatus for chemical vapour deposition in the manufacture of semiconductor devices (heading 8486); (o) industrial or laboratory equipment for the heat treatment of materials by induction or dielectric loss, including microwave equipment (heading 8514); (p) microwave ovens for industrial or commercial use, of the kind used in restaurants or similar establishments (heading 8514); (q) immersion heaters not permanently built in, for heating liquids, viscous (other than solid) substances or gases, as well as immersion heaters permanently built into a vat, tank, etc., and intended solely for heating water (heading 8516); (r) electric soil heating apparatus, electric space heating apparatus and domestic electro-thermic appliances of heading 8516. Apart from the machinery listed above, this heading covers equipment designed to heat or cool materials (solid, liquid or gaseous), either simply to change their temperature or to effect a transformation of the materials resulting principally from the change of temperature (e.g., for heating, cooking, roasting, distilling, rectifying, sterilising, pasteurising, steaming, drying, evaporation, vaporising, condensing or cooling). However, this heading excludes machinery and plant in which the heating or cooling, even if essential, is merely a secondary process designed to facilitate the main mechanical function of the equipment, e.g., machines for coating biscuits, etc., with chocolate and conches (heading 8438), washing machines (heading 8450 or 8451), machines for spreading and compacting bituminous road-surfacing materials (heading 8479). The machines and plant covered by this heading may or may not be fitted with mechanical equipment. This equipment may operate with any heating system (coal, oil, gas, steam, electricity, etc.), except for instantaneous and storage water heaters, which, when electrically heated, fall in heading 8516. This heading covers only equipment not used for domestic purposes, with the exception of instantaneous and storage water heaters, which are dealt with below in this Explanatory Note. This heading covers a wide range of machinery and equipment, described below.

(I) HEATING OR COOLING PLANT AND MACHINERY This category covers general-purpose equipment used in many industries for the simple treatment of materials by heating, boiling, cooking, concentrating, evaporating, vaporising, cooling, etc. This equipment includes: (A) Vessels, vats, etc., of various types for heating or cooling: (1) Vessels, vats, etc., for indirect heating or cooling, having double walls or bottoms and fitted with devices for the circulation of steam, chilled brine or other heating or cooling medium. However, vessels with double walls or double bottoms fall in Section XIV or Section XV (e.g., heading 7309) if they are not fitted with such devices for the circulation of a heating or cooling medium (e.g., heat-insulated containers), or in heading 8418 if they are fitted with the evaporator of a refrigerating unit (direct cooling). (2) Single-walled vessels, vats, etc., incorporating devices for direct heating (including heating by perforated steam coils), other than such vessels of the kind normally used for domestic purposes (generally heading 7321). In general, the industrial types are distinguished by their large dimensions and sturdy construction or by the presence of filters, condensate collectors or mechanical devices such as stirrers or tipping devices. Such vessels, whether single- or double-walled, are often designed for the needs of the chemical and allied industries for operation under high pressure (e.g., autoclaves) or at reduced pressure for special purposes, particularly in the chemical and related industries. Vessels fitted with mechanical devices but not having direct or indirect heating systems fall in heading 8479, unless by their construction they are clearly identifiable as equipment specified in another heading. This category of heating vessels includes pasteurisers, sometimes operating at reduced pressure, which are used for the treatment of foodstuffs or beverages (milk, butter, wines, beer, etc.) at temperatures ensuring the destruction of harmful micro-organisms. (B) Heat exchange units in which a hot medium (hot gas, steam or hot liquid) and a cold medium flow in parallel, usually in opposite directions, separated from each other by thin metal walls so that one medium is cooled and the other heated. These units are generally of three types: (i) concentric tube systems: one flow runs in the annular space, the other in the central tube; (ii) a tubular system for one fluid, enclosed in a chamber through which the other fluid flows; or (iii) two parallel systems of interconnected narrow chambers formed by separating plates. As noted in exclusion (e) of this Explanatory Note, the heading excludes auxiliary plant for steam boilers (heading 8404), many types of which (e.g., steam condensers, air preheaters, economisers) are of the general type of the heat exchange units described above. The following are examples of equipment which, subject to the provisions stated above, is included in Part (I) of this Explanatory Note:

(1) Freezers of the type of salt-freezers (other than those of heading 8210). (2) Condensers for nitrogen or other gases. (3) Units for pasteurization, concentration, cooling, etc. of milk (including vats with cooling systems). (4) Chants for processing and ripening of cheeses. (5) Equipment for concentration, cooling, etc. fruit juices, wines, etc. (6) Equipment used in agriculture (e.g. autoclaves for cooking potatoes, etc. as fodder; hot water baths for heating honeycombs, including tubs equipped with pressure screws). (7) Cooling columns (for example, used for grinding grains). (8) Autoclaves and steam-processing, boiling, cooking, frying, etc. equipment for cooking or canning food (for example, cooking chambers for ham; braziers for fish; plates, blanching autoclaves, etc. for fruits, vegetables, etc.; autoclaves and coolers for the canning industry; boilers for jam; boilers for confectionery products). (9) Soaking vessels and stirring vats equipped with heating appliances; hop-boiling vessels; pasteurizers and beer coolers, etc. (10) Juice defectors, concentration equipment, vacuum evaporators, vats for carbonization, sulfation or refining, etc., used in the sugar industry. Diffusion units (spray chambers and “calorizers” supplied together) for the extraction of sugar beet juice are not included in this heading (see paragraph (V)(B)(3) of the HS Explanatory Note to heading 8438); however, “calorizers” presented separately are classified in this heading. (11) Autoclaves for melting beef fat or saponifying fats; margarine hardening tanks equipped with a cooling rotating cylinder on which margarine hardens. (12) Vats, vessels, autoclaves, etc. for the chemical preparation of wood pulp or for the hydrolysis of wood. (13) Chans and other dyes preparation containers. (14) Autoclaves for vulcanization of rubber. (15) Vats for etching or degreasing metals. (16) Submersible spirals consisting of plastic tubes arranged in parallel or in the form of braids and sealants orally connected at each end in the form of a honeycomb structure with a connecting element. When immersed in a bath, such devices maintain a predetermined temperature or heat or cool the medium with a liquid or steam circulating in the tubes. (17) Special appliances for heating or cooking, usually not used in everyday life (for example, coffee strainers, tea or milk electric heaters, steam kettles and other items used in restaurants and canteens; steam-heated stoves, p-heating stoves, buffets with a heating system, drying cabinets, etc.; fryers).

(18) Machines for issuing hot or cold drinks without a payment collection device. The above equipment is mainly used in industry, but this heading also includes non-electric water heaters flowing and storage (capacitive), including water heaters based on the use of solar energy, both domestic and non-domestic. Such appliances shall not be included if the heating is by electricity (heading 8516). It should be noted that this heading does not include household steamers, pressure plates, and certain strainers of base metal (Section XV).

(ii) Equipment for DISTILLATION OR RECTIFICATION Except for distillation apparatus made of ceramics (heading 6909) or glass (heading 7017 or 7020), this category includes all installations for distillation of substances (liquid or solid). (A) Simple distillation machines. These devices usually consist of a fixed container in which the distilled liquid evaporates, a cooling device for condensing vapors leaving the container, and a vessel(s) in which distillate (distillates) is collected. These apparatuses may be of periodic action (e.g., simple portion distillers heated directly or by an internal steam coil) or continuous action. In the latter case, the distiller is constantly supplied with liquid and is usually heated by steam pipes or spirals. Continuous distillers can be connected in series; the first of them is heated directly or by steam, and the rest are supplied with a distillate and heated by pairs coming from the previous distiller. (B) Fractionation or rectification devices. This includes more complex machines of continuous operation, including vertical rectification columns, which ensure the separation of complex mixtures in one operation. The most common type of column consists of connecting sections that are separated by plates equipped with bubble caps and drain pipes. The steam rising from one section is in contact with the condensate coming from the above section, and due to a decrease in temperature when the steam rises in the column, the steam streams are separated at different levels according to their boiling points. Apparatuses for the distillation of solid products (charcoal, rot, wood, etc.) operate on the same principle, but the products are heated in furnaces of heading 8417. This heading covers only condensing or rectifying installations used for the separation of volatile products produced in a furnace. The main parts of distillation and the like devices are usually made of metal (for example, corrosion-resistant steel, copper or nickel), but they can be lined with glass or any refractory material. Devices designed for distillation under reduced or increased pressure may be equipped with vacuum pumps or compressors. Portion distillers are used mainly for the preparation of essential oils, liqueurs, etc. Continuous distillation devices (simple or fractional) are used in many industries (for example, in the production of industrial

alcohols, fatty acids, liquid air, synthetic motor fuels, various chemical products; in the refining of crude petroleum; for the distillation of wood, coal, shale, lignite, coal tar). This category also covers separators for irradiated fuel or process effluents. These separators operate on the principle of fractional distillation.

(III) evaporative or drying equipment This equipment is designed for various purposes (sometimes for operation in vacuum) according to the types of different materials, taking into account their heat sensitivity. This equipment can be heated directly or indirectly. This heading covers only evaporative or drying units employing comparatively low temperatures which are to be distinguished from industrial furnaces of heading 8417 in which the generated temperature is much higher. The most common types of industrial units within this heading are: (A) Vaporizers. These installations are usually in the form of vessels with a large working surface, heated directly or indirectly by steam coils. They are usually equipped with a system for removing generated vapors. These installations can be single or multi-purpose. In the latter case, their principle of operation and design are similar to multi-purpose distillers, but do not provide recoupling of condensed steam. (B) Laboratory freeze drying units and freezer dryers. These aggregates are used for stabilization and preservation by dehydration of biological substances such as antitoxins, bacteria, viruses, plasma and serums. The substances are frozen and then gradually reheated at very low pressure as the ice sublimates, leaving the dehydrated product. (C) Tunnel drying units . They consist of large chambers, usually equipped with conveyor equipment, with the help of which materials move at the required speed in the direction opposite to the flow of hot air. These installations are used, inter alia, in pottery, in the manufacture of glass, in the food industry (including equipment for smoking fish, meat, etc.); in drying wood, hay, etc. (D) Rotating dryers. These units consist of rotating cylinders or drums that are heated by internal or external sources. They are used in azlic industries (paper industry, potato flakes, etc.). (E) Plate dryers . . . These include metal chambers having a series of horizontally cut plates or shelves, sometimes internally heated. The central rotating shaft, which has lattices, distributes the material over the surface of the hot plates and directs it down through the slots to each subsequent plate. Equipment of this type is used for processing malted barley. (F) Spray dryers . These mouths work as evaporators and are metal chambers equipped with an internal horizontal disk that rotates with high frequency. These include a heater and fan to create a stream of hot air through which the injected disc centrifugally sprays liquid matter in the form of dispersion. So the liquid is instantaneous.

dried and converted to a powdered state. In devices of another type, the liquid is injected into the chamber with a thin stream directed against the flow of hot air. Devices of this type are used, in particular, for the preparation of powdered milk. This category of goods also includes units and equipment intended for evaporating solutions of fissile or radioactive substances and whether for drying fissile or radioactive products. This heading does not cover: (a) centrifuges for drying radioactive fallout (heading 8421); (b) equipment for drying bottles or other containers (heading 8422); (c) equipment for drying textile yarn, fabrics or finished textile articles (heading 8451). The equipment of this type often consists of rotating cylindrical or spherical containers in which the products to be processed (e.g. coffee beans, cocoa beans, cereals or nuts) are subjected to controlled heating by contact with the heated walls of the container or by a direct flow of air supplied through a heating medium (e.g., gas or fuel oil burners or coke flames). These devices are usually equipped with devices that ensure the constant rotation of the material for uniform processing, as well as to prevent charring. Other types are performed in the form of perforated, inclined or rotating shelves installed in the chamber into which heated gases are supplied. The equipment of this heading is not to be confused with industrial or laboratory furnaces of heading 8417. These devices may be closed vessels (their general type is described in this explanatory note above) in which various materials may be wet-heated (e.g., by steam supplied under pressure or by vapours emitted by the products themselves). Such equipment is used in various industrial operations (for example, in the preparation of plant or animal extracts; in the food industry as a whole; in operations involving the use of steam for degreasing or cleaning). Devices of another type are larger chambers in which the substance is exposed to more or less prolonged exposure to vapor. Such equipment is used, for example, for conditioning textile fibers in bulk, for steam processing of wood, etc. This heading does not include machinery for the conditioning of textile yarn or fabrics or for other steam treatment of such textile materials (heading 8451). As a rule, these apparatuses are containers or chambers, usually heated by steam or boiling water (or sometimes hot air), in which the articles or materials to be sterilized are kept at high temperature for a time necessary to kill bacteria, etc., without changes in the composition or physical condition of the articles or materials themselves. Many sterilizers for liquids are similar to the apparatus described above in point (I) (for example, pasteurizers). Some large arithic sterilizers can

be fitted with conveyors by which the articles are carried through the heating medium and then, if necessary, passed through a cooling unit which may also form part of the equipment. This category covers not only industrial sterilisers (e.g., for milk, wine, fruit juices, cotton wool) but also sterilisers used in operating theatres, etc. (VII) MACHINERY FOR LIQUEFYING AIR; SPECIAL LABORATORY APPARATUS AND EQUIPMENT The heading covers machines of the Linde or Claude type, used for liquefying air. The heading also covers specially designed laboratory apparatus and equipment, usually of small size (autoclaves, distilling, sterilising or steaming apparatus, dryers, etc.), but it excludes demonstration apparatus falling in heading 9023, as well as measuring, checking and similar apparatus more specifically described in Chapter 90. PARTS Subject to the general provisions regarding the classification of parts (see the General Explanatory Note to Section XVI), the heading covers parts of the apparatus described above. These parts include certain components of stills or rectifying columns, such as retorts, bubble caps and rings, plates and certain pipe elements; rotating plates and drums, etc., for roasters or dryers. Unassembled metal pipes and tubes which have been bent or curved but not otherwise worked are not identifiable as parts of articles of this heading and therefore fall in Section XV.

Official text adopted by a Recommendation of the EEC Board

Notes to chapter 84 — Nuclear reactors, boilers, machinery and mechanical appliances; parts thereof 24 items

Notes

Machine translation. The original is the Russian text of the EAEU tariff, and customs goes by it; this translation is for understanding only and has no legal force.

1. This group does not include:

(a) millstones, grinding stones or other articles of Chapter 68;

(b) equipment or devices (e.g. pumps) of ceramic materials and ceramic parts of machinery or devices of any material (Chapter 69);

(c) laboratory glassware (heading 7017); equipment, devices or other articles for technical purposes or parts thereof of glass (heading 7019 or 7020);

(d) articles of heading 7321 or 7322 or similar articles of other base metals (Chapters 74 to 76 or 78 to 81);

(e) vacuum cleaners of heading 8508;

(f) electromechanical household appliances of heading 8509; digital cameras of heading 8525;

(g) radiators for articles of Section XVII; or

(h) manual mechanical brushes for floor cleaning, without engine (heading 9603).

2. Subject to the provisions of Note 3 to Section XVI and Note 11 to this Chapter, a machine or device which meets the description in one or more of headings 8401 to 8424 or heading 8486 and at the same time the description in one or more headings 8425 to 8480 is included in the relevant heading of the first series of headings or in heading 8486 as the case may be, and not in the second series.

(A) However, heading 8419 does not cover:

(i) seed germination equipment, incubators or brooders (heading 8436);

(ii) machinery for wetting grains (heading 8437);

(iii) diffusion apparatus for the extraction of sugary juice (heading 8438);

(iv) equipment for the heat treatment of textile yarn, textile materials or finished textile articles (heading 8451); or

machining equipment, assemblies or laboratory equipment in which temperature change, even if necessary, is an auxiliary process.

(B) Heading 8422 does not cover:

(i) sewing machines for sewing bags or similar packagings (heading 8452); or

(ii) office equipment of heading 8472.

(i) paint-blasting printing presses (heading 8443); or

(ii) water jet cutting machines (heading 8456).

3. A machine for processing any material which corresponds to the description of heading 8456 and simultaneously to the description of heading 8457 to 8461, 8464 or 8465 is classified in heading 8456.

4. Heading 8457 covers only metalworking machines other than lathes (including multipurpose lathes) which may perform different types of machining operations by:

(a) the automatic replacement of tools from a tool store or similar device in accordance with the processing program(s);

(b) the automatic application simultaneously or sequentially of different processing heads operating at a fixed workpiece (assembly single-position machines); or

5. For the purposes of heading 8462, the term “longitudinal cutting line” for flat products means a process line consisting of a winder, a correct device, a longitudinal cutting device and a winder. The term “cross-cutting line” for flat products means a process line consisting of a unwinder, a correct device and a cutting device.

6. (A) For the purposes of heading 8471, the term “computers” means machines capable of:

(i) store the processing program or programs and at least the information currently necessary to execute the program;

(ii) be freely reprogrammable according to user requirements;

(iii) perform user-defined arithmetic calculations; and

(iv) perform, without human intervention, a processing program requiring the computer to modify its actions by making logical decisions during processing.

(B) Computing machines can be made in the form of systems consisting of a different number of individual blocks.

(C) Subject to the provisions of Notes (D) and (E) below, a block shall be treated as part of a computing system if it satisfies all of the following conditions:

(i) exclusively or principally used in a computing system;

(ii) is capable of being connected to the central processing unit either directly or through one or more other units; and

(iii) is capable of receiving or presenting information in such form (codes or signals) as may be used by the system.

Separately presented computer units are classified in heading 8471.

However, keyboards, X-Y-coordinate input devices and disk storage units which satisfy the conditions laid down in Notes (B) (ii) and (B) (iii) above are in all cases to be regarded as blocks of heading 8471.

(D) Heading 8471 does not cover the following devices, presented separately, even if they meet all the conditions of Note 6(C) above:

(i) printers, copiers, facsimile machines, combined or not;

(ii) apparatus for receiving or transmitting voice, images or other data, including apparatus for providing communications over a wired or wireless communication network (for example, on a local or wide area network);

(iii) loudspeakers and microphones;

(iv) television cameras, digital cameras and video recording cameras;

(v) monitors and projectors not combined with television reception equipment.

(E) Machines containing or working in conjunction with a computer and performing specific functions other than information processing are classified in the headings according to their specific functions or, if this is not possible, in the residual headings.

7. Heading 8482, inter alia, covers polished steel balls whose maximum and minimum diameter does not differ from the nominal diameter by more than 1% or by more than 0.05 mm, whichever is smaller. Other steel balls are classified in heading 7326.

8. A machine which is used for more than one purpose shall be classified as if its primary purpose were the only one.

Subject to the provisions of Note 2 to this Chapter and Note 3 to Section XVI, a machine whose primary purpose is not described in any heading or a machine in which none of its functions is primary is classified in heading 8479, unless the context otherwise provides. Heading 8479 also includes machinery for the manufacture of ropes or ropes (e.g. knitting machines) from metal wire, textile yarn or other materials or from a combination of such materials.

9. For the purposes of heading 8470, the term “pocket” applies only to devices not exceeding 170 x 100 x 45 mm.

10. For the purposes of heading 8485, the term additive manufacturing (also referred to as 3D printing) means the formation of physical objects based on a digital model by successively adding and layering, sealing and curing a material (e.g., metal, plastics or ceramics).

Subject to the provisions of Note 1 to Section XVI and Note 1 to Chapter 84, machines as described in heading 8485 are classified in that heading and no other heading of the Nomenclature.

11. (A) Notes 12(a) and 12(b) to Chapter 85 also apply to the terms “semiconductor devices” and “electronic integrated circuits”, respectively, as used in this note and in heading 8486. However, in this note and in heading 8486, the term "semiconductor devices" also applies to photosensitive semiconductor devices and LEDs.

(B) In this note and in heading 8486, the term “plane display panel production” covers the fabrication of a flat panel of substrates. It does not cover the production of glass or the installation of printed circuit boards or other electronic components on flat panels. The term "flat display panel" does not apply to cathode ray tube technology.

(i) producing or eliminating defects in masks and patterns;

assemblies of semiconductor devices or electronic integrated circuits;

(iii) lifting, manipulating, loading or unloading boules, plates, semiconductor devices, electronic integrated circuits and flat display panels.

(D) Subject to the provisions of Note 1 to Section XVI and Note 1 to Chapter 84, machinery meeting the description in heading 8486 is classified in this heading and in no other heading of the Nomenclature.

Subheading notes

English text as published in Annex I to Regulation (EU) 2021/1832 (Combined Nomenclature). The EAEU tariff and the EU nomenclature copy these notes from the same convention. For a Russian declaration the binding version is the Russian one: Annex to Decision No 80 of the EEC Council of 14 September 2021.

1. For the purposes of subheading 8465 20, the term ‘machining centres’ applies only to machine-tools for working wood, cork, bone, hard rubber, hard plastics or similar hard materials, which can carry out different types of machining operations by automatic tool change from a magazine or the like in conformity with a machining programme.

2. For the purposes of subheading 8471 49, the term ‘systems’ means automatic data-processing machines whose units satisfy the conditions laid down in note 6(C) to Chapter 84 and which comprise at least a central processing unit, one input unit (for example, a keyboard or a scanner), and one output unit (for example, a visual display unit or a printer).

3. For the purposes of subheading 8481 20, the expression ‘valves for oleohydraulic or pneumatic transmissions’ means valves which are used specifically in the transmission of ‘fluid power’ in a hydraulic or pneumatic system, where the energy source is supplied in the form of pressurized fluids (liquid or gas). These valves may be of any type (for example, pressure-reducing type, check type). Subheading 8481 20 takes precedence over all other subheadings of heading 8481.

4. Subheading 8482 40 applies only to bearings with cylindrical rollers of a uniform diameter not exceeding 5 mm and having a length which is at least three times the diameter. The ends of the rollers may be rounded.

Additional notes

Machine translation. The original is the Russian text of the EAEU tariff, and customs goes by it; this translation is for understanding only and has no legal force.

1. For the purposes of subheadings 8407 10 and 8409 10, the term “aviation engines” shall apply only to engines intended for assembly with an air or rotor.

2. В подсубпозицию 8471 70 300 0 также включаются устройства считывания компакт-дисков, являющиеся запоминающими устройствами вычислительных машин, которые предназначены для считывания сигналов с CD-ROM, аудиокомпакт-дисков и фотокомпакт-дисков и снабжены разъемом для наушников, регулятором громкости или кнопкой пуск/стоп.

Additional notes of the Eurasian Economic Union

Machine translation. The original is the Russian text of the EAEU tariff, and customs goes by it; this translation is for understanding only and has no legal force.

1. For the purposes of subheading 8482 10 900 1, the term “gross mass” means the total mass of the goods with all kinds of packaging materials and packagings ensuring their safety during storage and transport. The total weight of the goods does not include the mass of packaging materials or containers that are clearly suitable for reuse.

2. For the purposes of subheading 8415 81 001 0, the term “special production facilities” means premises in which the maintenance of precise values of temperature and humidity is due to the operational requirements of the equipment installed therein, such as machines, computers, switching equipment, surgical equipment, etc., or to the operations performed therein.

3. In subheadings 8427 20 190 1, 8427 90 000 1 and 8436 80 100 1, the date of manufacture shall be determined on the basis of the technical documentation of the manufacturer (technical passport, instruction manual) and the manufacturer's plate, which shall be fixed in a conspicuous, easily accessible place of the machinery and shall not be replaced during operation. If the manufacturer's technical documentation and the manufacturer's plate contain conflicting information about the date of manufacture or there is no information about the manufacturer of the equipment on the date of manufacture, then this technique is considered a technique, since the release of which more than 3 years have passed.

If the manufacturer's information indicates only the year of manufacture, then the date of manufacture of the equipment is considered 1 July of the year of manufacture; if the month and year of manufacture are indicated, the date of manufacture is the 15th day of the month specified in the manufacturer's information.

4. For the purpose of classification of goods in subheading 8482 10 900 1 in the states, whose territories constitute the customs territory of the Eurasian Economic Union, when applying the term "French border of the country of importation", the country of import is understood as the customs territory of the Eurasian Economic Union.

5. For the purpose of subheading 8407 10 000 3, the term “take-off power” means the maximum power developed by an aircraft piston engine.

“Take-off power” is specified in the technical documentation and (or) accompanying documents, measured in kilowatts or horsepower (1 kW corresponds to 1.35962 hp).

6. В подсубпозиции 8421 99 000 5 термин «элементы мембранные рулонного типа для фильтрования или очистки жидкостей» означает устройства цилиндрической формы, состоящие из:

- internal plastic perforated tube on which spirally wound membrane bags;

- drainage material located between membrane bags and glued to them on three sides.

The membrane package consists of a twice folded band of membrane containing an extruded grid inside.

At the ends of the membrane roll-type element, fixing discs and sealing cuffs can be installed.

7. For the purposes of subheading 8415 20 000 2, the term “in a single enclosure” refers to air conditioning units (air conditioners) in which all the elements are combined in a single enclosure, frame or platform.

The term "in a single housing" also applies to air conditioning units (air conditioners) in which the refrigeration compressor, which is part of a given air conditioning unit (air conditioner), is located separately, that is, not combined with the rest of the elements in one housing, on one frame or on one platform.

EEC classification decisions (1)

Binding in all EAEU member states: if the goods match the description, the decision fixes the code

8419 89Decision No. 93 of Jul 11, 2023decision text → No. 93, opens in a new tab
Воздушный охладитель жидкости (драйкулер)

Classification rulings for this code (60)

Machine translation from Russian. The original is the Russian wording of the ruling, and customs goes by it; this translation is for understanding only and has no legal force.

Трубчатая выпарная установка с падающей пленкой, тип с колонной аромы предназначена для производства концентрированного яблочного и вишневого соков.

Full description

Производительность оборудования: с подачей сырого яблочного сока 20 800 кг/ч (10,5 Брикс), с подачей вишневого сока 12745 кг/ч (14 Брикс).

Состав оборудования: балансные ёмкости для сока - 2 шт., блок концентрации сока (состоящий из 5-ти выпарных агрегатов, 5-ти сепараторов, 3-х теплообменников предварительного нагрева, колон ректификации и охлаждения), каркас-платформы с лестницей, блок охлаждения воды, блок охлаждения концентрата, CIP-мойка, электрошкаф управления с панелью, комплекты трубопроводов. Принцип работы: сырой (мутный) сок закачивается в балансную ёмкость, откуда последовательно перемещается через теплообменник, ректификационную колону, 2-ю и 1-ю ступень блока концентрации для его постепенного нагрева; во 2-й и 1-й ступени блока концентрации происходит основное разделение ароматических веществ от сока; конденсированные ароматические пары направляются через сепараторы в ректификационную колонну для отделения жидкости и последующего направления ароматического концентрата во внешнюю ёмкость; мутный сок из 1-ой ступени концентрации поступает на дальнейшую фильтрацию (в объем поставки не входит); после очищенный продукт (чистый сок) поступает во 2-ю балансную ёмкость, после которого продукт проходит предварительный нагрев в теплообменнике и поступает для концентрации в 3-ю, 4-ю и 5-ю ступень до конечной концентрации продукта (яблочный концентрат 70 Брикс, вишневый концентрат - 65 Брикс); далее концентрат сока охлаждается поэтапно в 5-й ступени блока концентрации, теплообменнике и блоке охлаждения концентрата.

GRI 1 and 6

The installation is designed to heat the coolant by heat exchange with hot flue gas.

Full description

Delivered unassembled.

The package includes: gas burner, heat exchanger, gas pipe, chimney, control system complete with electrical binding.

Principle of operation: the mixture of natural gas and air burned with a burner turns into a stream of hot furnace gas, heating the internal space of the plant, crossed by turns of pipes through which the coolant circulates.

The main technical characteristics of the coolant: the working temperature of the thermo-oil up to 280 ° C.

GRI 1, 2(a) and 6

The installation is designed to heat the coolant by heat exchange with hot flue gas.

Full description

Delivered unassembled.

The main components: gas burner, heat exchanger, gas pipe, chimney, control systems.

The package includes: electrical binding, hydraulic binding, hydraulic separator, pump groups, shut-off and control valves, expansion and emergency systems, filling and drain kit, as well as thermal oil, pipes, fittings, fastening devices and fasteners in the amount necessary for the assembly and first start of the installation.

The main technical characteristics of the coolant: the working temperature of the thermo-oil up to 280 ° C.

GRI 1 and 6

The equipment of the solid furnace melting line (hereinafter referred to as the Equipment) is a single complex of machines designed for melting solid furnace.

Full description

The main stages of the solid peck melting process are: unloading, unpacking, transportation, crushing, melting. The smelting of the peck is carried out in the smelter at an operating temperature of 200o S. Maintaining the operating temperature is achieved by circulating the coolant (thermal oil with a temperature of 200-300o). (C) on the coils(s) for heating the bakers. The equipment consists of the following main components: equipment for moving peck in solid and liquid state; semi-automatic unpacking station 2 compl.;

Peck crushers 3 pcs. ; vibrating crash, solid-peak melter 3 compl. ; filter cleaning liquid furnace 8 pcs. ; circulating bakery pump 3 pcs. ; pumping pump liquid furnace 2 pcs; liquid-peak equalization bunker; thermal oxidizer air heater; MCC cabinet; PLC cabinet. The equipment is supplied in disassembled form.

GRI 1, 2(a) and 6

The block-modular unit for the production of starting hydrogen 7000 Nm3 / h by steam reforming methane (hereinafter - the Installation), is designed to produce hydrogen with a purity of 99.9% by steam catalytic conversion of hydrocarbons with a block for cleaning converted gas from impurities by short-cycle adsorption (hereinafter - CCA) on solid absorbers.

Full description

The main processes for obtaining hydrogen are: hydrodesulphurization of raw materials, absorption (chemosorption) of hydrogen sulfide, steam reforming, high-temperature conversion of carbon monoxide, purification of hydrogen by the CCA method on solid adsorbents. The steam reforming process is the main catalytic process of hydrogen production from hydrocarbon raw materials. Endothermic reactions of steam reforming take place on a nickel catalyst at high temperatures. The installation consists of the following main components: reforming furnace, preliminary air heater (2 pcs), burners (9 pcs), water system unit, pressure control unit of the starting gas, CCA unit, sulfur removal unit, airblock, candle compressor unit of the initial gas (2 pcs), exhaust fan (2 pcs), valves, insulation and electrical heating, pipelines and technical materials, including the Venturi tube, metal structures, analyzer cabinets with analyzers, technical materials for electricians and electricians, TIP cable, local control panels for dynamic equipment (8 units), switchboards 0.4 kV (8 pcs), lighting system, electric cable, CIPIA, automatic control system of protection and alarm (RSU, PAZ, HMI, LAN), sensors of gas content (18 pcs), adsorbents and catalysts for the first load, fireproof materials.

The installation comes in disassembled form in the kit necessary for its assembly.

GRI 1, 2(a) and 6

The fire heater (hereinafter referred to as the heater) is designed to heat a liquid high-temperature organic coolant to a temperature of 245 ° C by heat exchange with hot furnace gas for its further use in the technological process of a gas fractionation plant.

Full description

Principle of operation: the liquid coolant with the help of circulating pumps is continuously pumped along a closed heat circuit passing through coils (radiant and convection) heating furnaces of hot oil, in which it is heated to a temperature of 245 ° C, and heat exchangers of the gas fractionation unit, from which it is returned cooled to a temperature of 150 ° C to the heater for re-heating. Heating the internal space of the furnace and the coils in it is carried out using a burner that uses natural gas as fuel.

The composition of the Heater includes the following main blocks that make up a single heat circuit: a hot oil heating furnace, a blower unit (for supplying air to the furnace), a circulating pump unit (for circulating the coolant through the closed heater system), a fuel gas preparation unit (for preparing and supplying natural (fuel) gas to the burner). The heater is supplied in a block-complete version in a partially disassembled form in the kit necessary for its assembly. Power 19.24 MW, heating temperature of the coolant 245 oC.

GRI 1, 2(a) and 6

The fire heater, (hereinafter referred to as the heater), is designed to heat a liquid high-temperature organic coolant to a temperature of 245 ° C by heat exchange with hot furnace gas for its further use in the technological process of a gas fractionation plant.

Full description

GRI 1, 2(a) and 6

The raw material module (hereinafter referred to as the Module) is designed for heating and feeding raw materials (mazut, vacuum gas oils, hydrocracking residues, etc.) to test catalysts for catalytic cracking.

Full description

The operating principle of the module. In order to reduce viscosity and increase fluidity, liquid raw materials are preheated in containers of light raw materials using heating mats to a temperature of 80 ° C. Heated raw materials with the help of a pump are fed into a drop-down electric tubular furnace, in which the raw materials are heated to a temperature of 350 ° C. Next, the heated raw materials enter the elevator reactor (not included in the supply volume) for mixing with the regenerated catalyst. The module includes: capacity of light raw materials (1 pc), capacity of light raw materials (1 pc), scales (1 pc), scales (1 pc), pump (1 pc), opening tubular furnace (1 pc), pipeline complete with fittings, fittings, filters, pressure gauges, regulators, thermocouples, pressure converter in the amount necessary for assembly, installation, primary start of the module.

The module is delivered in disassembled form.

Technical characteristics of the module: the weight of one batch of raw materials is 10-50 kg, the feed rate is 0.25-2.5 kg / h, the required heating temperature of the raw materials is 350 ° C, the maximum possible operating temperature of the furnace is 500 ° C.

GRI 1, 2(a) and 6

Dryer / granulator - drying plant for drying - granulation, mixing various types of finely ground powdered substances and liquid in the hot air stream.

Full description

The installation consists of an air intake system; a fine spray system; a drying/granulation chamber; an air outlet system. Also, the drying unit includes: ducts; electrical equipment, control and measuring devices, electric cabinet, control cabinet, control panel (plc). The dryer / granulator is designed to obtain granular materials (reagents) with a maximum moisture content of up to 0.5%, such as: reagents for increasing oil recovery of reservoirs, temperature stabilizers, corrosion inhibitors, etc. Obtaining granular materials is carried out in ways: from the liquid phase (liquid or liquid emulsion), from the solid phase (powder, granules).

It is possible to obtain granules with specified surface properties (color coating, moisture-resistant coating, coating with specified physical and chemical properties).

GRI 1 and 6

Ёмкость для фосфорной кислоты с мешалкой представляет собой вертикальный цилиндрический аппарат из нержавеющей стали и состоит из следующих основных компонентов: корпус с усилителем жесткости днища, крышка верхняя, внешний змеевик, опорная плита, мешалка, фланцы, контрфланцы, крепежные элементы в количестве, необходимом для сборки и монтажа оборудования.

Full description

Принцип действия: в ёмкость нагнетаются по трубопроводам фосфорная кислота и серная кислота, смешиваются со скрубберной водой и нейтрализуются аммиаком с образованием суспензии DAP-MAP (диаммоний фосфат, моноаммоний фосфат) и/или сульфата аммония. Для поддержания температуры технологического процесса 80 – 150°С осуществляется нагрев ёмкости за счет водяного пара, подаваемого в змеевик.

Основные технические характеристики ёмкости: вместимость 65,3 м³, максимальная масса рабочей среды 56 500 кг, рабочая температура -35/ 200°С, расчётная температура 200°С, температура теплоносителя 80–150°С, масса пустой ёмкости 15 200 кг.

GRI 1 and 6

Full description

Принцип действия: в ёмкость нагнетаются по трубопроводам фосфорная кислота и серная кислота, смешиваются со скрубберной водой и нейтрализуются аммиаком с образованием суспензии DAP-MAP (диаммоний фосфат, моноаммоний фосфат) и/или сульфата аммония. Для поддержания температуры технологического процесса 80–150°С осуществляется нагрев ёмкости за счет водяного пара, подаваемого в змеевик.

GRI 1 and 6

A complete concentrate evaporation plant.

Full description

(hereinafter referred to as the Installation) is a three-stage direct-flow evaporation system using thermal vapor recompression (TVR) for the processing of desalination concentrate of salt sulphide-alkaline wastewater. Wastewater treatment is carried out using the following technological processes: thermal compression, deaeration, multi-stage evaporation, cooling of brine. The three stages of evaporation are arranged sequentially, while the factory steam is sent to an ejector type thermocompressor, from which the heating steam is further supplied to the first stage.

Each subsequent stage of evaporation works at lower pressure and steam temperature, since it uses steam produced in the evaporator of the previous, hotter stage, which allows for high efficiency of steam use. The system operates under vacuum, which is supported by a liquid ring vacuum pump. In order to avoid excessive foaming, anti-foaming systems are used in the Installation.

GRI 1 and 6

The set of equipment is designed to expand the existing tubular evaporation plant with a falling film from a column of aroma in order to increase the production of concentrated apple juice with the supply of raw apple juice from 9999 kg / h 10 Vx (Brix) to 25 500 kg / h 10 Vx.

Full description

The composition of the equipment: the juice concentration unit (consists of an evaporative unit, a separator and a tubular heat exchanger) - 3 pcs., plates for a plate heat exchanger - 2 packs, a heat exchanger for cooling, a pump - 8 pcs., temperature sensors - 6 pcs., flowmeter, valves - 22 pcs., viewing glasses - 17 pcs., a set of a frame platform with stairs and pipelines with fittings in the amount necessary for assembly and commissioning of equipment. Working principle: Raw (turbid) apple juice is pumped into the balance container (existing), from which it moves through heat exchangers (existing and supplied), rectification column (existing), 2nd (supplied) and 1st (existing) stage of the concentration block for its gradual heating; in the 2nd and 1st stages of the concentration block, the main separation of aromatic substances from juice occurs; condensed aromatic vapors are sent through separators (existing and supplied) and a cooling column into a distillation column to separate the liquid and then direct the aromatic concentrate into an external container; cloudy juice from the 1st stage of concentration (existing) enters further filtration (existing);

After that, the purified product (pure juice) enters the 2nd balance container (existing); then the product is preheated in the heat exchanger (supplied) and is supplied for concentration in the 3rd (existing), 4th (delivered), 5th (existing) and 6th stage (delivered) to the final product concentration (apple concentrate 70 Brix); Then the juice concentrate is cooled in stages in the 6th stage of the concentration unit, heat exchangers (existing and supplied) and the cooling unit of the concentrate.

GRI 1, 2(a) and 6

Voskotopka steam centrifugal, model: "..." (hereinafter - Voskotopka) is designed to melt wax from raw materials.

Full description

The composition of Voskotopka includes the following main components: cover, grip handle, steam entry pipe, tank, stand, control panel, mesh rotor, drain neck, electric motor. Principle of action. After loading the raw materials, steam is supplied from the steam generator (Voskotopka is not included in the set). Under the influence of high temperature, the wax melts and drains into the Voskotopka cavity. Residues of wax from raw materials come out under the action of centrifugal force after the inclusion of the mesh rotor.

Main characteristics: tank diameter 780 mm, height with stand 1150 mm, height of stand 435 mm, weight 78 kg, body and parts in contact with wax, made of stainless steel.

GRI 1 and 6

Channels of feeders (2 pcs) with built-in cooling and heating system are designed to deliver glass without loss of thermal homogeneity along refractory gutters from a glass-cooked furnace to a glass-forming machine.

Full description

Principle of operation: glass mass automatically moves along the channel of the feeder, where, depending on the volume of the glass mass moved, it is cooled (at high removables) or heated (at a decrease in volume). Cooling is carried out by air injected by fans from the external environment, by the method of convection cooling of the glass surface and by the method of indirect convection cooling of the channel inside the overlapping beam. Heating is carried out by gas burners when burning natural gas.

The main components of the feeder channel: metal structures (lower and upper structure), inside which there is a refractory masonry (components of the lower structure: frame, support structure, ladder, platform, staircase, housing (pill of the feeder) - the supply kit is not included in connection with the repeated use of equipment from the customer); combustion system (gas-air burners, gas-air mixture control module); a set of cooling equipment; exhaust gas flue equipment (brackets with flaps); control and measuring system; two supply control units are installed in the supply control unit (the control set of the supply chain);

Management is carried out automatically.

GRI 1, 2(a) and 6

Technological equipment of the stage of obtaining a melt of polyethylene terephthalate (PET) is a component of the line for the production of polyester staple fiber by extrusion and is designed to obtain a spinning solution for subsequent supply to the extrusion site.

Full description

The equipment includes the following nodes: ethylene glycol (EG) distribution site, terephthalic acid paste (TFA) preparation site, two-stage esterification site, pre-polycondensation site, polycondensation site, titanium dioxide solution (TiO2) preparation site, catalyst solution preparation site, diethylene glycol (DEG) and trimethyl phosphate (TMF), modification additives preparation site, secondary raw material dosing and combustion control system, waste gas generator, 4 process control system. The process of obtaining a PET melt occurs in two stages: esterification and polycondensation.

Before the start of esterification in a pasto mixer with heating up to 40-50 oC, a suspension of monomers is prepared by mixing TFC and EG with the addition of a catalyst, modifying additives and a solution of DEG. Further, the suspension of TFC in EG is pumped into the esterifier of the first stage, where it is mixed with ethylene glycol. In the process of mixing with heating to 260 ° C and an excess pressure of 1.3 bar, the formation of diglycol terephthalate (DHT) occurs and the process of condensation of DHT begins.

At this site, through the dosing unit of secondary raw materials, it is possible to add polymer flakes obtained by processing frozen raw materials. The DHT semi-product is transferred to the stage II esterifier, where at a temperature of 265 ° C and an excess pressure of 1.1 bar, a further reaction occurs with the introduction of TiO2, DEG and TMF. Further, due to the pressure difference, the product is pumped to the pre-polycondensation site, where the polycondensation reaction occurs when heated to 272 ° C under a vacuum of 0.015 bar.

The resulting oligomer is transferred to the reactor of the pupil of the polycondensation site, where at a temperature of 283 ° C under a vacuum of 0.001 bar with constant stirring, a polycondensation reaction occurs with the formation of PET, which is then sent to the polymer melt supply site (not included in the equipment). Gaseous products formed during the PET production process are fed into the exhaust gas collection and combustion control system. To heat and maintain heat in the jacket of the pre-polycondensation reactor, a steam-phase coolant terminol ..., heated in biphenyl generators, is used.

Remote control and control of the equipment is carried out through a distributed control system from the operator room (with automated workstations for the engineer and operators), located in a separate room of the production building and managing the entire production line for the production of polyester staple fiber by extrusion. The section of the line is supplied with a set of shut-off-regulating fittings, pipes and fasteners in the amount necessary for assembly and commissioning of equipment.

GRI 1, 2(a) and 6

Autoclave model is an industrial equipment designed to cure aerated concrete block under the influence of high temperature and pressure.

Full description

The autoclave is a special steam chamber that provides the required humidity, pressure (working pressure - 1.3 MPa) and temperature (working temperature - up to 195 ° C), necessary to gain strength with concrete material. The full technological cycle of autoclaving consists of uniform heating, pressure exposure, uniform pressure relief and unloading of aerated concrete from the autoclave. The autoclave consists of a housing with external vacuum reinforcing rings, with an internal steam distribution pipeline, with internal guides for trolleys, with rollers for movable supports, with steam supply and discharge flanges, with condensate output flanges and under the installation of control devices, with a complete bayonet closing system (counterweight, pneumatic system, reduction mechanism, end switches).

The case is divided into 2 parts with a set of materials for assembly and first start.

GRI 1, 2(a) and 6

Cast iron refrigeration plate, is the main element of the blast furnace cooling system and is designed to provide a heat-dissipating protective shield between the inner lining of the blast furnace and the outer body of the furnace.

Full description

It is installed in the middle and lower parts of the blast furnace, between the furnace casing and refractory lining and is located in the tenth row of the working zone of the shoulders of the lower working part of the blast furnace. Mounting of the plate is carried out at three points: two bolt connections at the top of the plate and one bolt connection at the bottom. Fixing elements are an integral part of the refrigeration plate unit, and serve to install and fix cast-iron refrigeration plates on the housing of the blast furnace.

Cast iron refrigeration plate is a rectangular plate made by casting from high-strength cast iron with spherical graphite brand, standard GB (body) with steel cooling pipes poured inside for the circulation of cooling technical water. The plates are supplied pre-foutered, with the installation of silicon carbide inserts on the building mortar (mertel) in the appropriate slots of the plates in order to protect the hot side of the plate. To cast iron refrigeration plates, technical water is supplied from the pumps of the water cooling system.

All cast iron refrigeration plates are connected to a single water cooling system of the closed circuit of the blast furnace. Cooling water under pressure through the supply enters the coil system of the cast-iron refrigeration plate. The coil acts as a cooling element that absorbs excess heat from the blast furnace workspace through contact with the circulating coolant. Cooling continues while heat exchange occurs between the bodies, preventing overheating of the surrounding equipment (refractory lining and casing).

The goods are supplied on a wooden pallet, fixed with metal screeds, have markings made by casting method on the cold (not working) part of the plate in the form of the number 21. The overall dimensions of the plate are (DhShV) 933x476x1178 mm.

GRI 1 and 6

Оборудование в блочно-модульном исполнении, предназначенное для пастеризации и охлаждения теплоносителем (водой) пива и других напитков в алюминиевых банках, выполненное в виде стального туннеля, состоит из 10 секций (секции I – IV, в которых осуществляется постепенный нагрев напитков теплоносителем до температуры пастеризации; секция V, в которой напитки под воздействием теплоносителя выдерживаются при температуре пастеризации определенный промежуток времени; секции VI –X, в которых происходит охлаждение напитков теплоносителем до заданной температуры на выходе из туннеля).

Full description

Основные компоненты, которыми оснащено оборудование: 10 центробежных насосов, посредством которых осуществляется циркуляция теплоносителя; 4 пластинчатых теплообменника; многорядный пластинчатый цепной транспортер; термостатическая система нагрева/охлаждения, регулирующая температуру теплоносителя; спринклерная система мойки; соединительные кабели и трубопроводы, а также трубная обвязка секций пастеризатора; трубопроводная арматура; электрокоммутационные приборы; контрольно-измерительные приборы; силиконовые шторы и панели с изоляцией из каменной ваты, установка которых позволяет разделить внутреннего пространство туннеля на секции и предотвратить перепады температур; шкаф управления на основе программируемого логического контроллера, оснащенный системой кондиционирования.

Производительность: 38 000 банок (450 мл)/час, 39000 (330 мл)/час. Габариты (высота х ширина х длина) корпуса туннеля, мм: 2 800 х 5 850 х 19 180. Изделие поставляется в разобранном виде.

GRI 1, 2(a) and 6

The plant with a capacity of 9 tons is designed for thermal cracking (pyrolysis) of plastic waste, waste tires and other rubber products.

Full description

The main components of the pyrolysis plant are: pyrolysis reactor, water scrubber, mechanical impurity settling device, water oil separator (not included in the supply), large tubular capacitor, oil storage tanks, cooling tower (evaporative cooler), gas output capacity, electric cabinet, pipes for the passage of pyrolysis gas/vapor and flue gas, flue pipes, pipes for connecting plant units.

Principle of operation: combustion of combustible gas in atmospheric air with heat release leads to thermal decomposition in the reactor in an oxygen-free environment of high molecular weight compounds of processed tires with a decrease in their molecular weight. From the hot combined cycle mixture released from the pyrolysis reactor, after mechanical cleaning with a water oil separator, the water fraction is separated. Cooled below the flash point, gas from the tubular heat exchanger is sent to consumers and partially selected to maintain combustion in the heating system.

Cooled below the temperature of vaporization, the pyrolysis gas after the tubular heat exchanger passes from the vapor state to the liquid-pyrolysis oil, which is collected in the tank.

GRI 1, 2(a) and 6

The equipment is a single complete equipment designed for the production of bromine (with a capacity of 3000 t / g) and sodium bromide (with a capacity of 3750 t / g).

Full description

Composition of equipment: bromine storage tanks, acid sodium bromide, water - 12 pcs, capacity of hydrobromic acid, reboiler - 2 pcs, steam desorption column - 4 pcs, rectification column - 2 pcs, Absorber of Abkhazians, device for preheating brine - 4 pcs, heat exchangers for heating brine - 4 pcs, bromine vapor condenser - 7 pcs, rectification glass condenser - 2 pcs, bromine water separator - 10 pcs, cooling column (cooling tower), buffer capacity of chlorine gas - 2 pcs, capacity of absorbent liquid - 2 pcs, emergency storage container for bromine, pumps - 19 pcs, tub of uterine solution, measuring tanks - 5 pcs, capacity for condensate collection - 4 pcs, reactor type "K" - 3 pcs, type "K" evaporator - 4 pcs, evaporator (crystallizer) type "K" - 2 pcs, evaporative capacitors - 4 pcs, vacuum installation - 2 pcs, bag filters - 2 pcs, centrifuges - 2 pcs, drying system, vibrator, exhaust gas absorber, crane beam, Acoustic computer for PLC, control cabinets and distribution of electric current, instrumentation, electrical devices, cables, cable trays, set of pipelines, hoses, fittings, set of sealing elements, refractory and thermal insulation materials, lubricants and installation materials in quantity, necessary for assembly and commissioning, Technical documentation - 27 pieces.

The production process includes: acidification of an aqueous solution of bischofite (the brine of production raw materials is acidified with a small amount of hydrochloric acid); oxidation (acidified brine is passed through chlorine gas to oxidize bromine ions in the brine to free bromine); distillation and condensation (oxidized to free bromine brine is heated by steam in the distillation column for evaporation of bromine, Then the paars of bromine are condensed into liquid bromine, Raw bromine and bromine water are then separated in a bromine water flask separator; rectification (at this stage, bromine is separated from other impurities); reaction (a liquid alkali is added to the reaction boiler, water, urea and bromine for bromination reaction to form sodium bromide solution; evaporation (solution of sodium bromide is indirectly heated by steam, Evaporated and concentrated under vacuum to prolapse solid sodium bromide; crystallization (in the crystallizer, the solution is cooled to 70-80 ° C, At this time, most of the solid sodium bromide falls out of the solution; filtration and separation (sodium bromide enters centrifuges, where the separation into solid wet sodium bromide and uterine solution occurs; drying (through steam indirect heating, excess water is removed); crushing (in the presence of a large fraction, sodium bromide enters the grinder).

The equipment is delivered in disassembled form for ease of transportation.

GRI 1, 2(a) and 6

The plant with a capacity of 9 tons is designed for thermal cracking (pyrolysis) of plastic waste, waste tires and other rubber products.

Full description

The pyrolysis plant consists of the following main components: pyrolysis reactor, water scrubber, mechanical impurity separator, oil separator, large tubular capacitor, oil storage tanks, cooling tower (evaporative cooler), gas output capacity, electric cabinet, pipes for the passage of pyrolysis gas/vapor and flue gas, flue pipes, pipes for connecting the plant units, stairs.

Cooled below the temperature of vaporization, the pyrolysis gas after the tubular heat exchanger passes from the vapor state to the liquid-pyrolysis oil, which is collected in the tank.

GRI 1, 2(a) and 6

Fire heater, designed for heating a liquid high-temperature organic coolant to a temperature of 163 ° C by heat exchange with hot flue gas for its further use in the technological process of the complex gas treatment plant (hereinafter - GCP).

Full description

Principle of operation: the liquid coolant with the help of a block of circulating pumps (not included in the delivery) is continuously pumped along a closed heat circuit passing through coils (radiant and convection) heating furnaces of hot oil, in which it is heated to a temperature of 163 ° C, and heat exchangers of UGP, from which it is returned cooled to a temperature of 107 ° C to the heater for reheating. Heating the internal space of the furnace and the coils in it is carried out using a burner that uses natural gas as fuel.

The composition of the Heater includes the following main blocks that make up a single thermal circuit: a hot oil heating furnace, a blower unit (for supplying air to the furnace and maintaining the necessary combustion mode), a fuel gas preparation unit (for preparing and supplying natural (fuel) gas to the burner). The heater is supplied in a block version, partially disassembled and unfinished (without a block of circulating pumps). Power 10.3 MW, heating temperature of the coolant 163 oC.

GRI 1, 2(a) and 6

The fire heater (hereinafter referred to as the Heater) is designed to heat a liquid high-temperature organic coolant to a temperature of 163 ° C by heat exchange with hot flue gas for its further use in the technological process of an integrated gas treatment plant (hereinafter referred to as the GCP).

Full description

GRI 1, 2(a) and 6

Установка, представляющая собой воздушный охладитель жидкости, предназначенный для промежуточного охлаждения горячего амина температурой 75 0С до температуры 57 0С с целью его дальнейшего использования на установке по производству серы.

Full description

Основные компоненты установки: 1 трубный теплообменный пучок из оребренных алюминием стальных трубок и коллекторов, оборудованных патрубками с фланцами, к которым подключаются подающий и отводящий трубопроводы, и которые распределяют охлаждаемую среду равномерно по трубкам теплообменного пучка, под которыми расположены 2 лопастных вентилятора (приводятся в действие посредством ременных передач от электродвигателей); 3 вида жалюзи, предназначенные для регулировки потока воздуха при естественной конвекции и предотвращения переохлаждения оборудования в зимнее время года (входные располагаются по бокам установки; рециркуляционные – между вентиляторами и трубным пучком; выходные – над трубными пучками), которые приводятся в действие 3 пневматическими приводами (пневматическими актуаторами); кабельные трассы с конструкционными компонентами (кабельные лотки и крышки к ним, крепежные изделия и т.п.); устройства контроля (вибрационные датчики, температурные датчики).

Основные компоненты установки подлежат последующему монтажу в местах их расположения в несущей металлоконструкции, которая включает в себя металлический каркас, площадки обслуживания, лестницы подъема персонала, перила, рифленые листовые элементы противоскольжения, профилированные листы обшивки и др. Принцип работы установки: амин подается насосами установки по производству серы по трубопроводам (не входят в комплект поставки) на входные фланцы трубного пучка, проходя через который, амин охлаждается за счет температуры окружающего воздуха.

Эффективность теплообмена с окружающей средой повышается за счет работы вентиляторов, задействуемых попеременно, при пиковых нагрузках функционируют оба вентилятора. Установка поставляется в несобранном виде совместно с монтажными элементамми.

GRI 1 and 6

Installation, which is a liquid air cooler, designed to cool circulating acidic water with a temperature of 99.6 0C to a temperature of 54 0C for further use in a sulfur production plant.

Full description

The main components of the installation: 1 pipe heat exchange beam of aluminum-finned steel tubes and collectors, equipped with pipes with flanges, to which the supply and discharge pipelines are connected, and which distribute the cooled medium evenly through the tubes of the heat exchanger beam, under which there are 2 bladed fans (powered by belt transmissions from electric motors); 3 kinds of blinds, designed to regulate the flow of air during natural convection and prevent hypothermia of equipment in the winter season (inputs are located on the sides of the installation; recycling - between fans and a pipe beam; weekend - over the tube bundles, which are driven by 3 pneumatic actuators (pneumatic actuators); cable tracks with structural components (cable trays and covers to them, fasteners, etc.; monitoring devices (vibration sensors, temperature sensors).

The main components of the installation are subject to subsequent installation in places of their location in the supporting metal structure, which includes a metal frame, service areas, ladders for lifting personnel, railings, fluted sheet anti-slip elements, profiled sheets of skin, etc.

The principle of operation of the installation: water is supplied by the pumps of the sulfur production plant through pipelines (not included in the delivery) to the inlet flanges of the pipe beam, passing through which the water is cooled due to the ambient air temperature. The efficiency of heat exchange with the environment is increased due to the work of fans used alternately, both fans function at peak loads. The installation is supplied unassembled together with the installation elements.

GRI 1 and 6

Установка, представляющая собой воздушный охладитель жидкости, предназначенный для охлаждения горячего амина температурой 77,5 0С до температуры 50 0С с целью его дальнейшего использования на установке по производству серы.

Full description

Основные компоненты установки: 4 трубных теплообменных пучка из оребренных алюминием стальных трубок и коллекторов, оборудованных патрубками с фланцами, к которым подключаются подающий и отводящий трубопроводы, и которые распределяют охлаждаемую среду равномерно по трубкам теплообменных пучков, под которыми расположены 4 лопастных вентилятора (приводятся в действие посредством ременных передач от электродвигателей); 3 вида жалюзи, предназначенные для регулировки потока воздуха при естественной конвекции и предотвращения переохлаждения оборудования в зимнее время года (входные располагаются по бокам установки; рециркуляционные – между вентиляторами и трубными пучками; выходные – над трубными пучками), которые приводятся в действие 6 пневматическими приводами (пневматическими актуаторами); кабельные трассы с конструкционными компонентами (кабельные лотки и крышки к ним, крепежные изделия и т.п.); устройства контроля (вибрационные датчики, температурные датчики).

Основные компоненты установки подлежат последующему монтажу в местах их расположения в несущей металлоконструкции, которая состоит из двух блоков и включает в себя металлический каркас, площадки обслуживания, лестницы подъема персонала, перила, рифленые листовые элементы противоскольжения, листы обшивки и др. Принцип работы установки: амин, подвергнутый ранее регенерированию, подается насосами установки по производству серы по трубопроводам (не входят в комплект поставки) на входные фланцы трубных пучков, проходя через которые, амин охлаждается за счет температуры окружающего воздуха.

Эффективность теплообмена с окружающей средой повышается за счет работы вентиляторов, задействуемых попеременно парами, при пиковых нагрузках функционируют все вентиляторы. Установка поставляется в несообранном виде совместно с монтажными элементами.

GRI 1 and 6

Full description

Основные компоненты установки: 4 трубных теплообменных пучка из оребренных алюминием стальных трубок и коллекторов, оборудованных патрубками с фланцами, к которым подключаются подающий и отводящий трубопроводы, и которые распределяют охлаждаемую среду равномерно по трубкам теплообменных пучков), под которыми расположены 4 лопастных вентилятора (приводятся в действие посредством ременных передач от электродвигателей); 3 вида жалюзи, предназначенные для регулировки потока воздуха при естественной конвекции и предотвращения переохлаждения оборудования в зимнее время года (входные располагаются по бокам установки; рециркуляционные – между вентиляторами и трубными пучками; выходные – над трубными пучками), которые приводятся в действие 6 пневматическими приводами (пневматическими актуаторами); кабельные трассы с конструкционными компонентами (кабельные лотки и крышки к ним, крепежные изделия и т.п.); устройства контроля (вибрационные датчики, температурные датчики).

Эффективность теплообмена с окружающей средой повышается за счет работы вентиляторов, задействуемых попеременно парами, при пиковых нагрузках функционируют все вентиляторы. Установка поставляется в нессобранном виде совместно с монтажными элементами.

GRI 1 and 6

The product designed for completing the middle part of the blast furnace mine provides protection of the steel body of the blast furnace from thermal destruction (burnout) by removing heat from the refractory masonry of the inner surface of the mine due to the constant circulation of technical water.

Full description

Horizontal refrigeration plate is an assembly unit of a complex configuration, which is made by welding the connection of two main elements: a refrigeration plate (made of high-strength cast iron with spherical graphite of the brand by casting, in the process of which two steel p-shaped tubes with a diameter of 32 mm (internal and external coils) designed for the circulation of heat-dissipating technical water) and a steel welded bracket (ambrazure), through which the horizontal refrigeration plate is vertically attached to the main fireplaced elements;

The overall dimensions of the product are 730*752*970 mm, the weight of the product is 327 kg (in accordance with drawing No. L24751-34SB-01).

GRI 1 and 6

Installation, which is an air cooler of a liquid, designed for intermediate lowering of the temperature of cooling (quenching) water with a temperature of 67 0 C to a temperature of 57 0 C for the purpose of its further use at a sulfur production plant.

Full description

The principle of operation of the installation: tempering water is supplied by pumps of the sulphur production plant through pipelines (not included in the delivery) to the inlet flanges of the pipe beam, passing through which the water is cooled due to the ambient air temperature. The efficiency of heat exchange with the environment is increased due to the work of fans used alternately, both fans function at peak loads. The installation is supplied unassembled together with the installation elements.

GRI 1 and 6

Full description

The principle of operation of the installation: tempering water is supplied by pumps of the sulphur production plant through pipelines (not included in the delivery) to the inlet flanges of the pipe beam, passing through which the water is cooled due to the ambient air temperature. The efficiency of heat exchange with the environment is increased due to the work of fans used alternately, both fans function at peak loads. The installation comes in unassembled form together with the mounting elements.

GRI 1 and 6

Full description

Основные компоненты установки: 1 трубный теплообменный пучок из оребренных алюминием стальных трубок и коллекторов, оборудованных патрубками с фланцами, к которым подключаются подающий и отводящий трубопроводы, и которые распределяют охлаждаемую среду равномерно по трубкам теплообменного пучка), под которыми расположены 2 лопастных вентилятора (приводятся в действие посредством ременных передач от электродвигателей); 3 вида жалюзи, предназначенные для регулировки потока воздуха при естественной конвекции и предотвращения переохлаждения оборудования в зимнее время года (входные располагаются по бокам установки; рециркуляционные – между вентиляторами и трубным пучком; выходные – над трубными пучками), которые приводятся в действие 3 пневматическими приводами (пневматическими актуаторами); кабельные трассы с конструкционными компонентами (кабельные лотки и крышки к ним, крепежные изделия и т.п.); устройства контроля (вибрационные датчики, температурные датчики).

Основные компоненты установки подлежат последующему монтажу в местах их расположения в несущей металлоконструкции, которая включает в себя металлический каркас, площадки обслуживания, лестницы подъема персонала, перила, рифленые листовые элементы противоскольжения, профилированные листы обшивки и др. Принцип работы установки: тощий амин, подается насосами установки по производству серы по трубопроводам (не входят в комплект поставки) на входные фланцы трубного пучка, проходя через который, амин охлаждается за счет температуры окружающего воздуха.

GRI 1 and 6

The line is designed for the production of granular five-water sodium metasilicate.

Full description

The principle of operation: when spraying a liquid solution of sodium silicate with a temperature of 80-90 ° C, its cooling occurs in the crystallizer, and at a temperature below 72.2 ° C, the process of its crystallization begins (the transition of sodium silicate from a liquid state to a crystalline one). The initiators of crystallization are the starting powder of five-water metasilicate, which at the time of the first start of the line comes from the sieving machine, forming a dust cloud inside the crystallizer.

In the granulator, the raw materials are rolled into granules, which are subjected to classification, crushing and grinding. The small fraction returns to the crystallizer in the form of a starting powder.

The main components of the line: filtration system of incoming raw materials (includes: filter 2. 1 of them is not available for importation; filter pump - 2 pcs) with pipe tying; raw material supply system (consisting of: jet pump-2 pcs, pipe valve) with pipe binding; granulation and crystallization system with pipe binding; cooling system (consisting of: cooler; pump for cooling hot water - 2 pcs. ; air conditioning pump - 2 pcs. ; cooling exchanger; air treatment device) with pipe binding; system of supply of bulk materials (consisting of: Bucket elevator - 2 pcs. ; feeder -2 pcs. ; main valve for distribution of raw materials) with tubing; classification and grinding system (consisting of: diffuser; double-headed mill; crusher) with pipe binding; dust removal system with pipe binding (includes: cyclone separator; dust collector fan; water pump for dust capture - 2 pcs. ; intermediate fan; automatic process control system (ACUCP system)

(consisting of: computer equipment control cabinet, remote control, pressure transducers, flowmeters, thermometers, etc.).

GRI 1, 2(a) and 6

Voskotopka steam 12 frame, (hereinafter - Voskotopka) is designed to melt wax from honeycomb frames or raw materials.

Full description

Steam is formed by heating water, which is poured into the lower part of the body. Heating of the lower part of the body can be carried out by a gas burner or an electric stove (Voskotopki is not included in the kit). The pump consists of the following main parts: lid, body, water level, drain pipe wax, pallet, cavity for water and steam, mesh basket, screws for securing the lid. Principle of action. Before starting work in Voskotopka, water is poured to a certain level. After that, Voskotopka is installed on a gas burner or electric stove, open the lid and load raw materials into the mesh basket, close the lid and fix it with screws located in the upper part.

Next, include a gas burner, let the raw material melt and drain into the pallet of Voskotopka and through the tube into the wax collection container. Main characteristics: height 500 mm, width 522 mm, length 570 mm, capacity (water) 15 l, weight 15 kg, number of frames 12 pcs., material stainless steel.

GRI 1 and 6

The installation is designed to prepare gas mixtures from industrial gases (oxygen, argon, nitrogen, carbon dioxide) in the established ratios and fill cylinders and monoblocks (bundles of cylinders) with these mixtures and industrial gases, as well as liquefied carbon dioxide.

Full description

The principle of operation of the installation is as follows. Gaseous oxygen, argon and nitrogen from external tanks (not included in the package) are fed to receiving ramps. From receiving ramps, industrial gases are fed either to ramps for subsequent filling of cylinders and monoblocks with these gases, or to a gas mixing ramp, which is used for the preparation of gas mixtures. Carbon dioxide gas is also used to prepare gas mixtures. From the gas mixing ramp, the obtained gas mixtures are fed to the ramps for subsequent filling (filling) of cylinders and monoblocks with these gas mixtures.

Gaseous carbon dioxide is obtained as follows. Liquefied carbon dioxide from an external tank (not included in the package) is supplied through a compressor to an electric evaporator. Liquefied carbon dioxide, passing through the coil, contacts with circulating hot water with a temperature of 80 ° C, is heated and intensively evaporates with the formation of steam, passing into a gaseous phase. From an electric compressor, the resulting carbon dioxide gas is fed to a gas mixing ramp, where it is used to prepare gas mixtures.

Liquefied carbon dioxide through the compressor can also be fed to the ramp for subsequent filling of cylinders and monoblocks with liquefied carbon dioxide.

The package includes: the site of reception of gaseous oxygen, nitrogen and argon; the site of filling cylinders and monoblocks with industrial gases and their mixtures; the site of preparation of carbon dioxide gas and filling of cylinders and monoblocks with liquefied carbon dioxide; an automated system of control and control of the installation; safety, regulating and closing pipe fitting; control and measuring instruments and automation devices; a connecting pipeline; a load-bearing metal structure of the steel plant; a set of fasteners in the amount necessary for initial assembly and commissioning.

The equipment is supplied in a partially disassembled form.

GRI 3(c) and 6

The reactor is designed to simulate the operation of the stage of liquid-phase hydrocracking.

Full description

The raw material is a mixture of heavy hydrocarbons with a density above 900-950 kg / m3 (at 20 ° C), as well as mixtures of heavy fractions of oil refining and petrochemicals with spent oils, waste plastic waste (polyethylene, polypropylene, polystyrene). The working principle is as follows. Raw materials are poured into the reactor vessel, the reactor lid is closed, nitrogen is supplied to the reactor to displace air, electric heating of the reactor vessel is included (maximum heating temperature of 500 ° C). When the specified temperature is reached, a sample is taken from the lower connections of the reactor.

The set temperature is maintained for 6 hours, samples continue to be taken every 2 hours. After 6 hours, the heating is turned off, the reactor begins to cool with recycled water from an external source. When the temperature in the reactor reaches 100-120 ° C, the valve is opened on the drain from the reactor to the receiver. The reactor is controlled by a reactor controller with a primary temperature regulator. The reactor is supplied in the composition: a stand with a reactor vessel assembled, a controller with a primary temperature regulator.

GRI 1 and 6

The installation is a circulating mixing vessel with a volume of 39.6 liters, equipped with electric heating elements, a pneumatic stirrer, as well as a shut-off and control valve and instrumentation.

Full description

The equipment is designed for heating (up to 135 ° C) and mixing of slurry raw materials (activated lignite, heavy petroleum product, plastic) for subsequent use in the slurry hydrocracking plant. The installation comes in assembled form.

GRI 1 and 6

Full description

GRI 1 and 6

The first stage suspension hydrocracking unit is designed for processing the suspension mixture of lignite and oil residue through catalytic hydrogenation in the presence of a catalyst to obtain purified light hydrocarbons.

Full description

Installation composition: node supply gas phase of raw materials, node supply liquid phase of raw materials, reactor unit, separation node, liquid waste treatment unit, control system.

Principle of operation: a suspension mixture with hydrogen is supplied to the reactor, where the raw material is heated to 450 ° C, as a result of which heavy hydrocarbons in the presence of a catalyst (not included in the package) are divided into medium and light distillates in the gas and liquid phase, cubic residue, water, etc.; then the obtained substances are sent to the separator to separate gas and liquid; separated light hydrocarbons are cooled and accumulated in the receivers. The installation comes in the form of assembled modules with equipment, metal structures (ladders, service areas), pipelines, cables, control and measuring devices and shut-off and control valves.

GRI 1, 2(a) and 6

The catalytic plant of high-pressure hydrocracking of the second stage is designed for deep processing of the cube product by means of catalytic hydrogenation in the presence of a catalyst to obtain purified light hydrocarbons.

Full description

Supplied in the collection in modular execution. The equipment includes the following main components: raw materials (2 pcs.), dosage pump, hydrocracking reactors (2 pcs.), electric reactor furnaces (2 pcs.), separators (2 pcs.), distillation steam column, heat exchanger, food tank, cabinet distribution control system, blowing tank, sampler, tank catcher.

Principle of operation: hydrogen and liquid-phase raw materials are fed into the reactor with a fixed layer and subjected to catalytic hydrogenation reactions in the presence of a catalyst (not included in the delivery) to obtain purified light hydrocarbons; then the reacted materials enter the separator for separation of liquid and gas, cooled and collected for storage in a food container. The temperature in the reactors is maintained in the range of 400-450 ° C, the pressure is 190-240 kgf / cm2.

GRI 1 and 6

Autoclave plant is technological equipment for curing composite products under the influence of temperature and pressure.

Full description

Technical specifications: working area 3.5x6 m, max. working pressure - 1.2 MPa, max. working temperature - 250 ° C. Equipment composition: autoclave, door opening motor - 2 pcs., electric heater - 54 pcs., cooler, electric motor drive fan, cooling fan, muffler, vacuum pump - 2 pcs., trolley, tow cart, rail bridge, nitrogen removal system, compressor, dehumidifier, air filter - 3 pcs., nitrogen system, pressure creation system, receiver, steel water tank - 2 pcs., cooling system - 2 pcs., cooling system - industrial water control system, 2 pc.

Principle of operation: a form with a material (glass or carbon fabric impregnated with a polymer resin) is immersed on a transport trolley in a vacuum bag and moves along the rail bridge into an autoclave; an inert gas (nitrogen) is pumped into the autoclave to the working pressure; then the working temperature necessary for polymerization of the resin in the product is created in the chamber; excess air is removed from the vacuum system; after polymerization, a smooth decrease in temperature is provided by the cooling system, and the atmospheric pressure is also reduced from the vehicle.

The equipment is supplied in disassembled form complete with materials necessary for assembly and commissioning.

GRI 1, 2(a) and 6

The evaporation plant for the production of calcium chloride is designed to obtain a scaled salt of mixed crystalline hydrates of calcium chloride CaCl2*nH2O (hereinafter - the Installation).

Full description

Evaporation of calcium chloride from brine is carried out in shell tube heat exchangers. As a heat source, steam with a temperature of 165 ° C generated outside the boundaries of the Installation is used to heat the brine. Main components of the Installation: feeding tank vaporizer separator vaporizer separator cooler, cooler, preliminary heater - 2 pcs, vacuum installation, air compressor, receiver, dehumidifier - 2 pcs, mixer concentrator - 2 units, centrifuge cooled cutter - 2 pcs, fan, loading bunker - 2 pcs, packing machine - 2 pcs, cooler of sealing liquid, container (only 10 pcs), pumps (a total of 31 units);

ATSUP (integrated management and security system); (i.e., induction and distribution devices); AZRA (stop-regulating fittings); KIPiA (control and measuring instruments); pipeline, connecting / installation materials and tools in the kit necessary for the assembly of the Installation. The installation is supplied in a partially disassembled and incomplete form (does not include: pumping pump - 2 units, tower-cooling tower - 2 units, injector pump - 4 units, metal structures, cables, cable trays).

Principle of operation: The plant uses the process of “two-step countercurrent evaporation”. The pre-heated initial solution enters the evaporative circuit of the 2nd stage (separator - evaporator - circulation pump to remove excess moisture). In the process of evaporation, solid particles of sodium-potassium-magnesium salts are deposited in the lower part of the separator, from which it is necessary to clean the solution. To do this, a salt-containing suspension is fed through concentrators to a centrifuge to separate the solid and liquid fractions.

Solid particles of sodium-potassium-magnesium salts are dissolved in the container and removed beyond the limits of the installation. The liquid fraction (uterine solution) is returned to the evaporative circuit. The next stage of evaporation is carried out in the evaporation circuit of the 1st stage (separator - evaporator - circulation pump) of the amount of moisture remaining in the solution with its subsequent cooling and "cutting" on the cooled cutters. As a result, the finished product is formed - solid calcium chloride hydrates.

GRI 1, 2(a) and 6

The plant is designed for the production of nitrous oxide (hereinafter - gas) from ammonium nitrate (ammonium nitrate), a capacity of 74 m3 / h.

Full description

The equipment consists of the following main components: system of melting and decomposition of ammonium nitrate (electric furnaces-reactors - 6 pcs., primary scrubbers - 6 pcs, refrigerator - 6 pieces, gas condenser - 6 pcs, water scrubber - 6 pcs; gas purification system (hydrotraps - 2 pcs., block of permanganate gas purification (permanganate scrubber and reservoir of potassium permanganate solution 500 l), alkaline gas purification unit (alkaline scrubber and sodium hydroxide solution reservoir with a volume of 500 liters), acid gas purification unit (acid scrubber and reservoir of sulfuric acid solution with a volume of 500 liters), capacitor; receiver; gasholder; gas compressor; gas drying system (purging capacity of 0.04 m3 - 3 pcs), dehumidifier of 0.04 m3-3 pcs;

Control panel; safety and shut-off pipe fittings (safety valves - 3 pcs., flange valves - 9 pcs, ball valves - 16 pcs; KIPiA (glass gauge - 6 pcs., temperature regulator i-them A-5931 - 3 pcs., temperature sensors Pt-100 - 12 pcs.); a set of fasteners in the amount necessary for initial assembly and commissioning.

It is supplied in a partially disassembled form. Working principle: raw materials (ammonium nitrate in liquid or dry form) are supplied to electric reactor furnaces, where it decomposes with the release of heat to gas (nitrogen oxide) and water vapor; control of the chemical reaction is carried out by regulating the temperature and pressure in the electrical furnace reactor system; nitrous oxide, formed in a decomposition boiler at a temperature of 255-260oC with a pressure of 0.5 bar, He enters the primary scrubbers. passing through plastic nozzles which are partially cooled to 160oC, a part of the undecomposed liquid ammonium nitrate is reduced and fed back to the reactor part of the furnace; further gas enters refrigerators (heat exchangers) and is cooled (the resulting water vapor is used in boilers to decompose nitrate as a phlegm for irrigation);

Then nitrous oxide and water vapor enter the gas capacitors (heat exchangers), which are partially cooled to 100°C, steam condenses and collects at the bottom of the container, from where it merges into the drainage system; further, passing water scrubbers, from above through liquid nozzles, the gas is irrigated with cold water under the pressure of the oncoming flow of hot gas for partial removal of water-soluble impurities (chlorides, sulphates) and cooling nitrous oxide to the temperature in the production room (19-22oC);

Then the gas passes the hydrotraps to collect and remove excess moisture, system of sequentially connected blocks of gas purification from impurities (sulphate chlorides, higher nitrogen oxides, organic impurities, in which the gas is irrigated with aqueous chemical solutions; further purified nitrous oxide enters the condenser to remove excess moisture; then passing the receiver, gas pressure is reduced from 0.5 bar to 0 bar and the gas is supplied to the gas holder for temporary storage before compression; further, getting into a compressor with a water cooling system, the pressure of nitrous oxide by compression is increased from 0 bar to 60 bar, the temperature decreases to -27 ° C and the gas enters the gas drying system to remove moisture and water vapor, formed in the process of compression; the final product is drained compressed gas/nitrogen oxide with a pressure of 60 bar and a temperature of 27°C; control and control of the technological process is carried out through the control panel.

Depending on the need, the gas can go to liquefaction or storage tanks.

GRI 1, 2(a) and 6

The equipment used in the brewing industry is designed to heat and sterilize the wort with its subsequent cooling and addition of yeast for the initial growth and reproduction of yeast cells by maintaining an optimal temperature regime.

Full description

The equipment includes the following main components: two cylindrical containers with a conical bottom (propagators) with a volume of 1400 and 9000 liters, made of stainless steel with thermal insulation and protective shells, equipped with steel jackets of heating, through which the coolant (vapor) circulates, steel cooling shirts, through which the refrigerant propylene glycol flows (not included in the package), vertical stirringers assembled, dispensing engines, 2 vertical tubing plates, control tubes with armostating tubes, control plates for mineration, 125 tubes, aration plates, aration system with aramping tubes.

The principle of operation of the equipment: the must enters the first propagator with a volume of 1400 liters. is heated and sterilized by steam created in the shirt of the conical bottom of the container. The sterilized wort is cooled to 20 – 25 ° C with the help of a refrigerant flowing through the cooling shirt of the cylindrical part of the container. Breeded in a laboratory container (the supply does not include) yeast is added to the wort and aerated sterile air supplied under pressure, and stirring the resulting mixture (to exclude precipitation of yeast and maintain temperature), the initial growth and reproduction of yeast cells is carried out.

The yeast reproduced in the first propagator is mixed with an increased volume of wort and transfused into a second propagator of 9000 liters to implement a technological cycle (similar to the first propagator), as a result of which the volume and growth rate of yeast cells increases. After the completion of the breeding cycle, lasting 16-24 hours, yeast from the second propagator enters the fermentation department of the brewing industry (the supply is not included). The goods are delivered in a partially disassembled form.

GRI 1, 2(a) and 6

The evaporation plant for the production of sodium chloride is intended for the production of sodium chloride, as well as a lithium-containing sorbent (hereinafter - the Installation).

Full description

Evaporation of sodium chloride from brine is carried out in casing tube heat exchangers. As a heat source, steam generated within the installation is used to heat the brine. The solution in the heat exchanger is heated to a temperature of 100-110 ° C, as a result of which the solution goes into the vapor-liquid phase, which is subject to further separation.

The main components of the Installation: supply tank; injection pumps; filters; impurity collection capacity; evaporator; preheater; separator; condensate capacity; circulating pump; condensate pump; compressor; steam generator; cyclone; centrifuge; uterine solution pump; pump pumping pump; alkaline tank; foaming capacity; automatic pumping pumps; liquid pumping; fluid control system (water mounting device; water suction system; water suction control; water mounting device; co-containing device; 17; water sing equipment for suction control;

The installation comes in partially disassembled form for ease of transportation. The main stages of production: 1) cleaning of the incoming solution (brine) from foreign impurities and regulation of pH values; 2) formation of a salt suspension in the evaporative circuit (“separator – evaporator – circulating pump” (main equipment of the Installation)); 3) separation of solid and liquid fractions resulting in the formation of a salt of sodium chloride and a concentrate of lithium-containing solution.

GRI 1, 2(a) and 6

The station for use in its own brewing industry, serves for the reproduction of yeast during yeast expansion, further cultivation of yeast and their sterilization between fermentation cycles.

Full description

The main components of the station: - Three yeast tanks (No. 1.2 3) of stainless steel of 170 hl, 45 hl and 7 hl, accordingly Everyone with a lid, equipped with a cooling shirt and a heating shirt, thermal insulation, tank No. 2 - with a vertical stirrer with a geared engine, with spraying heads, viewing glass, tube supports, service areas, vertical staircases; - valve tubing modules, stations and matrices (cooling tanks DRT No. 1-3), discharge of steam and compressed air valve; cooling valves with a pump module; technological CIP-valves for the DRT module; - internal sprinkler system of SIP-wash with a chemical reagent dosing system with two dosage pumps, heat exchanger, conductometer, flowmeter, temperature sensor; - dosage pump;

CIP-tanks (3 units. total volume of 60 l) for hot alkali, acid and hot water with fenced service areas); - CIP modules (heating and return pipeline; recharge); - control cabinets (4 pcs); - control and measuring equipment; - electrical switching equipment. Application of the station for its intended purpose (preparation of a yeast suspension with established technological parameters) includes the following stages: CIP cleaning of the corresponding yeast tank and wort pipeline, steam sterilization of the must and oxygen pipeline; supply of high-temperature wort to yeast tanks from the cooking shop; reducing the temperature of the wort to a set value; introduction of yeast culture into yeast tank No. 1; supplying oxygen from the oxygen pipeline and starting the stirrer to maintain a uniform temperature of the yeast suspension, which, due to the pressure difference between tanks, is consistently pumped from tank No. 1 to tanks No. 2 and 3, in each of which, being under the influence of controlled temperature and oxygen content (which accelerates the growth and reproduction of yeast) achieves the specified technological parameters, after which from tank No. 3, the finished yeast suspension, finally prepared for further production, is pumped through the yeast pipeline to the fermenter using a yeast supply pump, After that, the CIP station completely cleans tanks No. 1-3 and pipelines before preparing for the production of the next batch.

The goods are delivered in a partially disassembled form.

Установка представляет собой единое комплектное оборудование, предназначенное для производства линейной алкилбензолсульфоновой кислоты (LABS) и сульфата натрия лаурилэфира (SLES) производительностью 1,6 тонны в час посредством обработки сырья в процессах с изменением температуры.

Full description

Установка состоит из следующих основных элементов: блок (плавление серы, сжигание серы, конверсия диоксида серы в триоксид серы): резервуар-плавитель для серы А, резервуар для серы В, серный фильтр А – 2 шт., серный фильтр В – 2 шт., шестеренчатый насос А/В – 2 шт., предпусковой подогреватель, зажигалка для серы, бак для дизельного топлива, дизельный насос, горелка, печь для сжигания серы, охладитель диоксида серы, первый охладитель конвертера диоксида серы - триоксид серы, конвертер диоксида серы - триоксид серы, первый охладитель триоксида серы, второй охладитель триоксида серы, резервуар для олеума, вентилятор охлаждающего воздуха, воздуходувка, нагнетающая воздух для горения); блок 02 (для осушения воздуха): охлаждающая группа, воздуходувка технологического воздуха, входной фильтр, предохранительный клапан, обратный клапан, регенеративный теплообменник, рефрижератор с резервуаром для гликоля, воздушный гликолевый охладитель, воздушный водяной охладитель, насос для рециркуляции гликолевого раствора, осушитель воздуха А, осушитель воздуха В, вентилятор регенерационного воздуха); блок (плёночное сульфирование/сульфатирование триоксида серы, старение и стабилизация алкилбензолсульфоновой кислоты, очистка выхлопных газов): фильтр для воздушно-капельной смеси триоксида серы, насос рециркуляции охлаждающей воды, резервуар аварийной подачи, плёночный мультитрубный реактор сульфирования, сепаратор газ/жидкость, циклонный сепаратор, насос для перекачки сульфоновой кислоты со специальным инвертором, насос подачи некондиционного продукта, резервуар для некондиционного продукта, резервуар для промывочной горячей воды, стабилизационный насос, ёмкость для старения, стабилизационный дозирующий насос, ббалансировочный резервуар, насос для перекачки сульфоновой кислоты, теплообменник сульфоновой кислоты, электростатический осадитель, подогреватель воздуха, воздуходувка защиты электродов, скруббер для диоксида серы, циркуляционный насос промывки, балансировочный резервуар для жидкой каустической соды); блок утилизации отработанного тепла (теплообменник/парогенератор, предварительный нагреватель, насос для умягчённой воды, резервуар для умягчённой воды, насос рециркуляции горячей воды, резервуар для горячей воды); однотрубная экспериментальная установка по сульфированию 1, 6 т/час (реактор сульфирования, газожидкостный разделитель, резервуар для органического сырья, фильтр воздушно-капельной взвеси оксида серы, фильтр воздушно-капельной взвеси, перекачивающий насос А для сульфоновой кислоты, дозирующий насос для органического сырья, циркуляционный насос); блок (нейтрализации и очистки): резервуар для чистой воды, резервуар для гидроксида натрия, резервуар для буферного раствора, резервуар для перекиси водорода, дозирующий насос для чистой воды, дозирующий насос для жидкой каустической соды, буферный дозирующий насос, дозирующий насос для перекиси водорода, насос нейтрализации, стриппинг-башня, насос рециркуляции SLES, насос для перекачки SLES, сепаратор, конденсатор, водокольцевой вакуумный насос); система управления, шкафы управления и распределения электрического тока, контрольно-измерительные приборы, электрические устройства, кабели, кабельные лотки, комплект трубопроводов, шлангов, фитингов, арматуры, комплект уплотнительных элементов, огнеупоров и теплоизоляционных материалов, смазочные и монтажные материалы, катализаторы в количестве, необходимом для сборки и пуско-наладки производственного процесса.

Производственный процесс: в блоке 02 осуществляется подготовка, осушение и охлаждение атмосферного воздуха. Подготовленный воздух направляется в блок 01, в котором происходит производство триоксида серы следующим образом: гранулированная сера загружается в резервуар-плавитель, где при помощи пара расплавляется до жидкого текучего состояния, накапливается в резервуаре для серы и непрерывно подаётся в печь сжигания серы. В результате сжигания серы образуется двуокись серы в виде газа, которая преобразуется в каталитическом конвертере с охлаждением в газообразный триоксид серы.

Далее триоксид серы поступает в блок 03 в многотрубчатый плёночный реактор сульфирования, который является основным элементом оборудования, где в процессе с охлаждением реагирует с линейным алкилбензолом (LAB), который в качестве органического сырья подаётся с сырьевого склада. В результате образуется сульфоновая кислота, которая после обработки процессами старения и стабилизации, и далее гидролиза, образует линейную алкилбензолсульфоновую кислоту (LABS), которая является готовым продуктом. Для получения сульфата натрия лаурилэфира (SLES), как готового продукта, технологический процесс аналогичен.

Изменяется только сырьё, подаваемое в многотрубчатый плёночный реактор сульфирования для реагирования с триоксидом серы, а именно: С12-С14 лауриловый спирт. И используется блок (нейтрализации и очистки) SLES от диоксана. Фильтры, насосы, трубопроводы установки снабжены паровыми рубашками для предотвращения охлаждения и кристаллизации серы. Оборудование поставляется в разобранном виде для удобства транспортировки.

GRI 1, 2(a) and 6

Complex equipment of the feed conditioning line is designed for steam processing and conditioning of the feed in accordance with the specified characteristics.

Full description

The process of conditioning provides deeper penetration and even distribution of moisture through the feed, as well as the destruction of pathogenic organisms.

The principle of operation of the feed conditioning line is as follows. The powdered feed mixture is loaded into the product supply hopper, equipped with a lower level sensor, from where it is loaded into the screw conveyor. Through the auger conveyor, the feed mixture through the adapter is fed into the steam mixer, in the steam mixer the bulk feed is moistened by steam to the necessary condition and mixed. The moistened bulk feed is moved from the steam mixer to the air conditioner with time control, in which the product is aged at a high temperature (up to 90 ° C) for a specified time.

After conditioning, the feed is unloaded from the air conditioner through the unloading sleeve. Steam is supplied to the steam mixer from the steam supply system of the plant, its supply is regulated by the steam control unit and the steam pressure reduction reducer. The temperature in the air conditioner is maintained by means of heating cables installed in it. The operation of the line is controlled by the air conditioning control system.

The package includes a product delivery hopper, lower-level sensor, screw conveyor 250, adapter from screw conveyor to steam mixer, steam mixer hot start 2700 single, steam control unit 450-1750 kg / h, steam pressure reduction reducer 250-1650 kg / h, air conditioner with time control with a feeding auger, the unloading hose of the product from the air conditioner with a length of 1227 mm, air conditioning control panel, electric cable with materials for connection (1170 m), cable trays (34 m), galvanized steel diames. 20 mm (13 m), galvanized steel diames. 25 mm (5 m), mounting materials.

The equipment is supplied in disassembled form. The specified number of components is necessary for the initial installation. The package does not include spare, replaceable parts.

GRI 1, 2(a) and 6

Technological plant for the production of photoresist is designed for technological processes with liquid and dry chemical media (raw materials for obtaining a photoresist (1,4-dioxane, methoxypropanol, methoxypropyl acetate, anisol, o-xylol, etc.) with the addition of sorbents, phenoloformaldehyde and ion exchange resins, light-sensitive product) when mixing them with simultaneous heating.

Full description

The installation is mounted on a single metal frame structure, having all the technological holes and fixing elements, and consists of the following main components: reactor 1 (vertical cylindrical steel vessel with a volume of 63 liters with a heat exchange shirt and a stirrer); reactor 2 (vertical cylindrical steel vessel with a volume of 63 liters with a frame stirrer); bunker (with a built-in vibrator for loading dry components into the reactor1); receivers (to collect liquid product); dryer filter (for filtration and drying of the intermediate product); electric heat exchanger (for heating and maintaining the temperature regime and for heating gas); filters (for multi-stage filtering solution); display scales (to weigh and control the amount of bulk components loaded into reactors 1 and 2); process control and control system complete with monitoring and monitoring sensors; a set of pipelines with flanges according to the technological scheme of installation.

Principle of operation: liquid and bulk chemical raw materials, with a temperature of at least 15 ° C, enter reactor 1 (liquid components are loaded with a pump, bulk through a loading bunker) and mixed with a stirrer. Mixing of raw materials occurs with heating of the reactor to 30 ° C until the dry and liquid components dissolve and a homogeneous mass is obtained. Maintaining the temperature to 30 ° C is necessary for stable dissolution of dry substances, resins, light-sensitive product in the solvent. The obtained photoresist-semi-finished product enters the filter dryer, where the photoresist is separated from the grains of the sorbent dehumidifier and resins, by filtration and drying.

Filtered to the specified parameters, the solution enters the reactor 2, where further mixing occurs, until the components added to obtain a homogeneous solution are completely dissolved. Further, the obtained photoresist sequentially passes through all stages of filtration, and at the output has a particle size of 0.1 microns, the mass fraction of water is not more than 0.5%, kinematic viscosity from 4.7 to 450 cSt. The finished product, after quality control, is merged into special containers (the supply is not included in the package) and fed to the packaging line (the delivery is not included in the package).

Management and control of the installation is carried out by a single control system.

Technical characteristics of the plant: capacity of 50 kg / day, reactor capacity of 63 l, operating pressure 0.4-0.6 MPa, operating temperature of the process of 30 ° C, particle size of the finished product 0.1 μr, compressed nitrogen temperature from + 5 ° C to + 40 ° C, compressed air temperature from + 5 ° C to + 40 ° C, water turnover temperature + 5 ° C to + 30 ° C. For ease of transportation, the equipment is supplied in a partially disassembled form.

GRI 1, 2(a) and 6

Automatic steam-air autoclave 1500x4200x6 mm is a site of sterilization (hereinafter - the Site) line designed for the production of wet animal feed in spiders (packages).

Full description

Sterilization is carried out in steam-air autoclaves (max. operating temperature 130 ° C, max. working pressure 0.3 mPa). The site consists of the following main components: automatic steam-air autoclave (1500x4200x6 mm) - 2 pcs; semi-automatic spider loader; semi-automatic spider unloader; conveyors for the transmission of trays - 6 pcs, conveyors for the transmission of spiders - 7 pcs, sterilization trays - 400 pcs, carts for trays - 16 pcs, delta robot, device for unloading trays, spider dryer, control cabinets - 2 pcs, set for installation.

Technological process of sterilization. Finished packages (spiders) with the help of a delta robot (a spider-like arm) are laid on trays. The trays filled with spiders are assembled in a stack of 25 pcs, loaded into a trolley and moved on floor rails to an autoclave for sterilization according to specified parameters. After sterilization, the spiders are unloaded and sent to the dryer. Then the spiders pass through the dryer and move to the packaging area in the box.

GRI 1 and 6

Full description

The installation is mounted on a single metal frame structure, having all the technological holes and fixing elements, and consists of the following main components: reactor (a vertical cylindrical steel vessel with a volume of 1000 liters with a heat exchange shirt and a stirrer); reactor (vertical cylindrical steel vessel with a volume of 1000 liters with a frame stirrer); 70 liter bunker (with a powder loading system for loading dry components into the reactor); receivers (to collect liquid product); filter dryer with stirrer (for filtration and drying of the intermediate product); filters (for multi-stage filtering solution); display scales (to weigh and control the amount of bulk components loaded into reactors); process control and control system complete with monitoring and monitoring sensors; a set of valves and pipelines with flanges according to the technological scheme of the installation.

Principle of operation: liquid and bulk chemical raw materials with a temperature of at least 15 ° C (at a lower temperature they are heated using a heating system) enter the reactor (liquid components are loaded using a pump (not included in the delivery), bulk through a bunker with a powder loading system) and mix with a stirrer. Mixing of raw materials occurs with heating of the reactor to 30 ° C until the dry and liquid components dissolve and a homogeneous mass is obtained. Maintaining the temperature to 30 ° C is necessary for stable dissolution of dry substances, phenoformaldehyde resins, light-sensitive product in the solvent, adsorption of molaga from the solution and demetallization of the solution under the influence of ion exchange resins.

The resulting semi-finished photoresist enters the filter dryer, where the photoresist is separated from the grains of the sorbent dehumidifier and ion exchange resins, by filtration and drying. The solution filtered to the specified parameters enters the reactor, where further mixing occurs, until the components added to obtain a homogeneous solution are completely dissolved. Further, the obtained photoresist sequentially passes through all stages of filtration, and at the output has a particle size of 0.1 microns, the mass fraction of water is not more than 0.5%, kinematic viscosity from 4.7 to 450 cSt.

The finished product, after quality control, is merged into special containers (the supply is not included in the package) and fed to the packaging line (the delivery is not included in the package). Management and control of the installation is carried out by a single control system.

Technical characteristics of the plant: capacity of 1000 kg / day, reactor capacity of 1000 liters, operating pressure of 4-6 MPa, operating temperature of the process of 30 ° C, particle size of the finished product 0.1 μr, compressed nitrogen temperature from + 5 ° C to + 40 ° C, compressed air temperature from + 5 ° C to + 40 ° C, water turnover temperature + 5 ° C to + 30 ° C. For ease of transportation, the equipment is supplied in a partially disassembled form.

GRI 1, 2(a) and 6

Full description

The installation is mounted on a single metal frame structure with all technological holes and fastener elements, and consists of the following main components: a reactor (vertical cylindrical steel vessel with a volume of 250 liters with a heat exchange shirt); a reactor (vertical cylindrical steel vessel with a volume of 250 liters with a frame stirrator); a bunker with a volume of 70 liters (with a built-in vibrator for loading dry components into the reactor); receivers (for collecting a dryer with an intermediate filter (for filtration and drying of the product); a system for controlling the process of loading and filtering);

Principle of operation: liquid and bulk chemical raw materials with a temperature of at least 15 ° C (at a lower temperature they are heated using a heating system) enter the reactor (liquid components are loaded using a pump (not included in the delivery), bulked through a loading bunker) and mixed with a stirrer. Mixing of raw materials occurs with heating of the reactor to 30 ° C until the dry and liquid components dissolve and a homogeneous mass is obtained. Maintaining the temperature to 30 ° C is necessary for stable dissolution of dry substances, phenoformaldehyde resins, light-sensitive product in the solvent, adsorption of moisture from the solution and demetallization of the solution under the influence of ion exchange resins.

Technical characteristics of the plant: capacity of 200 kg / day, reactor capacity of 250 liters, operating pressure of 4-6 MPa, operating temperature of the process of 30 ° C, particle size of the finished product 0.1 μr, compressed nitrogen temperature from + 5 ° C to + 40 ° C, compressed air temperature from + 5 ° C to + 40 ° C, water turnover temperature + 5 ° C to + 30 ° C. For ease of transportation, the equipment is supplied in a partially disassembled form.

GRI 1, 2(a) and 6

Autoclave plant is technological equipment for curing composite materials under the influence of high temperatures and pressure.

Full description

The installation consists of the following main components: autoclave system (autoclave body with bayonent door and sealing ring, with guides (rail system), with a circulation duct, with hydraulic drives to open and close the door, with internal thermal insulation, with a loading food trolley, with a safety locking device, with pneumatic valves of entry and exit of nitrogen; heating system (electric tubular heaters (33 units), thermocouples with plug connectors (6 units), Temperature sensors (6 units); cooling system (heat exchanger), connecting pipeline, pneumatic valves of primary and pre-cooling, open cooling tower with fan, with a tank of cooling water, water pumps (2 units), water-softening plant; circulation/forced convection system (centrifugal fan with impeller and water-cooled engine); vacuum and nitrogen system (vacuum pumps (2 units), pressure sensors (2 pcs), transmitters (6 units), air compressor, receiver, damper/muffler, nitrogen generator; control system (control boxes (3 units), PLC, industrial computer with control panel, frequency converter, software, low-voltage power distributor, low-voltage switch, automatic switch; pipe bandage.

Principle of operation: the form with the material (glass or carbon fabric impregnated with a polymer resin) in the vacuum package is immersed on the transport trolley and moved (tightened) along the rails into the autoclave; to increase the pressure, an inert gas (nitrogen) is supplied to the autoclave; then, using heating and circulation systems in the chamber, the operating temperature necessary for polymerization of the product is created; after reaching the specified values of temperature and pressure, they are maintained for a certain time; with the help of the vacuum system, excess air is removed from the vacuum package; after the polymerization process is activated, the autoclave is controlled by the autoclave.

Technical characteristics: the location of the autoclave is horizontal, the working zone is 1.5×3 m, the maximum working pressure is 1.2 MPa, the maximum operating temperature is 250 ° C. The equipment is supplied in disassembled form.

GRI 1, 2(a) and 6

The air cooling unit, the design pressure of 28.9 MPa, the design wall temperature of 180 ° C (hereinafter referred to as the Air Cooling Apparatus) is intended for cooling the gas-liquid mixture (hereinafter referred to as the working medium) for subsequent injection into the formation of the Bolshtyr oil field.

Full description

The main components of the air cooling unit: heat exchange sections (5 units); metal structure of the “closed” type; reference metal structure of the "open" type (3 sets); metal structure of the “open” type; horizontal blinds (5 sets); air humidification system (10 sets); upper air recirculation chamber (5 sets); vertical blinds (20 sets); side vertical blinds (4 sets); side vertical blinds (4 sets); stationary service platform and stairs; Fan blocks (15 sets); electrical equipment and KIPIA; cable products; mounting and connecting materials for equipment.

The operating principle of the air cooling unit is as follows. Heated to a temperature of 145 ° C, the working medium from the compressor of the gas pumping unit (not included in the supply) at a pressure of 25.2 MPa enters the heat exchange sections, in which the working medium cools to a temperature of 35.0 ° C due to the removal of heat by cold air injected by the fan blocks into the intertube space (tube beams) of the heat exchange sections. Cold air is injected perpendicularly to the tubular beams of heat exchange sections.

Heat exchange between the working medium and air is carried out through the walls of heat exchange pipes, there is no direct contact of cooling air and the working medium, the flows do not mix. The temperature of the working environment at the outlet of the heat exchange sections is regulated by changing the cooling air flow through the use of a frequency-controlled drive of fan units and air recirculation through a blind system. At the same time, the gas-liquid mixture is cooled with partial condensation of hydrocarbons.

The air cooling unit is supplied in a partially disassembled form.

GRI 1, 2(a) and 6

The air cooling apparatus, the design pressure of 10.8 MPa, the design wall temperature of 180 ° C (hereinafter referred to as the Air Cooling Apparatus) is intended for cooling the gas-liquid mixture (hereinafter referred to as the working medium) for subsequent injection into the Bolshtyr oil field formation.

Full description

The operating principle of the air cooling unit is as follows. Heated to a temperature of 150.2 ° C, the working medium from the compressor of the gas pumping unit (not included in the supply) under a pressure of 9.9 MPa enters the heat exchange sections, in which the working medium cools to a temperature of 35.0 ° C due to the removal of heat by cold air, injected by fans into the intertube space (tube beams) of the heat exchange sections. Cold air is injected perpendicularly to the tubular beams of heat exchange sections.

Heat exchange between the working medium and air is carried out through the walls of heat exchange pipes, there is no direct contact of cooling air and the working medium, the flows do not mix. The temperature of the working environment at the outlet of the heat exchange sections is regulated by changing the cooling air flow through the use of a frequency-controlled drive of fan units and air recirculation through a blind system. At the same time, the gas-liquid mixture with partial condensation of hydrocarbons is cooled.

The air cooling unit is supplied in a partially disassembled form.

GRI 1, 2(a) and 6

The air cooling apparatus, the design pressure of 4.0 MPa, the design wall temperature of 180 ° C (hereinafter referred to as the Air Cooling Apparatus) is intended for cooling the gas-liquid mixture (hereinafter referred to as the working medium) for subsequent injection into the Bolshtyr oil field formation.

Full description

The operating principle of the air cooling unit is as follows. Heated to a temperature of 150.2 ° C, the working medium from the compressor of the gas pumping unit (not included in the supply) under a pressure of 3.1 MPa enters the heat exchange sections, in which the working medium cools to a temperature of 35.0 ° C due to the removal of heat by cold air injected by the fan blocks into the intertube space (tube beams) of the heat exchange sections. Cold air is injected perpendicularly to the tubular beams of heat exchange sections.

The air cooling unit is supplied in a partially disassembled form.

GRI 1, 2(a) and 6

Установка представляет собой единое комплектное оборудование, предназначенное для производства 80 000 тонн в год 98%-ной серной кислоты и 20 00 тонн в год 105%-го олеума (в перерасчете на 100% H2SO4) посредством обработки сырья в процессах с изменением температуры.

Full description

Основные компоненты: блок подготовки сырья (ёмкости для жидкой серы - 5 шт., насосы циркуляционные - 6 шт., фильтр жидкой серы), блок деарации (сборник конденсата, устройство добавления фосфатов, деаэратор и ёмкость воды, насос подачи обессоленной воды - 2 шт.), блок сжигания и конверсии серы (печь сжигания серы, котел-утилизатор, нагреватели - 2 шт., 4-х секционный конвертер, теплообменник - 4 шт., экономайзеры - 2 шт., воздушные фильтры - 2 шт., воздуходувки - 2 шт., горелка на природном газе, вентиляторы - 2 шт.), блок абсорбции и сушки (колонна сушки воздуха, колонны абсорбции серной кислоты, олеума, газов - 5 шт., ёмкости для серной кислоты, олеума, раствора гидросульфита - 13 шт., теплообменники - 5 шт., насосы для подачи, циркуляции или отгрузки серной кислоты, олеума, щелочи - 13 шт., колонна нейтрализации, электростатический туманоуловитель, дымовая труба), блок водоподготовки (градирни - 2 шт., очистители накипи - 2 шт., дозирующие устройства - 2 шт., насосы циркуляционные - 2 шт., жалюзи с электроприводом - 4 шт.), блок бойлера (впрыскивающие пароохладители - 3 шт., охладитель отбора проб, расширительные баки - 2 шт., паросборник, глушители - 2 шт.), шкафы управления и распределения электрического тока, контрольно-измерительные приборы, кабели, кабельные лотки, комплект трубопроводов, арматуры и другие монтажные материалы в количестве, необходимом для сборки и пуско-наладки.

Производственный процесс: в блоке подготовки сырья осуществляется выгрузка, очистка и хранение жидкой серы; в блоке сушки осуществляется осушение воздуха для последующей подачи в блок сжигания и конверсии серы для проведения процесса сжигания серы и её конверсии до ангидрида (триокиси) серы; в печи сжигания жидкая сера подввергается необратимой экзотермической реакции с выделением очень большого количества тепла, в результате которого сера превращается в диоксид (двуокись) серы (SO2); далее смесь диоксида серы с остаточным воздухом через котел-утилизатор и систему теплообменников поступает в 4-х секционный конвертер, где в присутствии катализатора, диоксид серы конвертируется в ангидрид серы (SO3); далее полученный ангидрид серы через теплообменники поступает на колоны абсорбции, где смешивается с серной кислотой с водой для получения серной кислоты с концентрацией 98% и олеума с концентрацией 105 % (в перерасчете на 100% серную кислоту); далее полученная серная кислота и олеум поступает в ёмкости для хранения; блоки деарации, подготовки воды и бойлера предназначены для подготовки бессолевой воды для использования в котле-утилизаторе, теплообменниках и блоке абсорбции для производства конечного продукта.

Оборудование поставляется в разобранном виде для удобства транспортировки.

GRI 1, 2(a) and 6

A line of heat treatment of aluminum scrap (used aluminum cans from under drinks) by heating metal, during which organic compounds such as paint, food lacquer, water, beverage residues are evaporated from the surface of the cans.

Full description

The line consists of the following main components: belt conveyor, buffer hopper, scraper conveyor for cold material, inclined belt conveyor, weight belt conveyor, screw conveyor, rotating drum, combustion chamber, vibration feeder, cyclone, two heat exchangers, high-temperature output conveyor, vibration feeder, dust cleaning unit.

The principle of operation of the line: crushed raw materials from the buffer bunker through the conveyor system enters the rotating drum of firing. The combustion chamber, in which two gas burners heat the air and flue gases to 800 degrees Celsius, pumps hot air into the drum, which rotates to mix raw materials for more efficient heating and evaporation of varnish, paint, water and organic elements. Flue gases from the rotating drum of firing through the pipe go back to the combustion chamber, where they are burned with gas burners with the addition of atmospheric air, while decomposing dangerous fumes into simple, safe compounds.

Waste flue gas is sucked out of the combustion chamber and through heat exchangers (to reduce the temperature of the exhaust gases) is fed to a dust cleaning plant consisting of cyclones for trapping large dust particles and an installation with bag filters for final cleaning of the exhaust gases. Cleaned scrap in hot form through a vibration feeder (conveyor) is supplied to the melting furnace (not included in the delivery kit).

The main technical characteristics: performance 4 t / h, maximum / minimum operating temperature 850 °/280 ° C, overall dimensions (DhShV) 54600 × 9600 × 35800 mm, weight 187561 kg.

Supplied in disassembled form.

GRI 1, 2(a) and 6

The pretreatment system of aluminum chips is a line designed for high-temperature heating of aluminum chips in order to remove oils (lubricating and cooling liquids), paint, emulsions, moisture.

Full description

The line consists of the following main components: hopper, scraper conveyor, centrifuge, sludge removal machine, centrifugal storage device for collecting aluminum chips from the centrifuge, weight belt conveyor, magnetic separator, feeding auger, rotating drying cylinder, unloading vibration conveyor, heat exchanger, afterburn chamber, cyclone, pneumatic conveyor for unloading material, conveyor for collecting particles (2 pieces).

Principle of operation: aluminum shavings with metal inclusions are loaded into a receiving bunker, from where, using a scraper conveyor, they are fed into a centrifuge designed to separate materials. From it, shavings are transferred to a rotating cylinder, in which, by heating hot flue gases circulating with the help of a fan from the afterburn chamber, paint, oils, emulsions are removed. In the afterburn chamber there are two burners that heat the air and flue gases to 800 degrees Celsius. From the cylinder, the shavings are unloaded and passes through the vibrosito, where a small fraction of aluminum is separated, and the shavings are fed into the pneumatic transport system and transferred to the storage bins.

Technical specifications: temperature inside the drying cylinder: ≈ 450-550 °C, cylinder performance: max. 3000 kg / h.

Overall dimensions (In x Sh x D): 9124x9484x25500 mm Mass - 110 tons. The line is delivered in disassembled form.

GRI 1, 2(a) and 6

Thermo-oil boiler is a complex of technological equipment that is used to provide heat to woodworking equipment (for example, in drying chambers for wood, lumber, veneer, in presses for the production of plywood, chipboard, MDF, OSB boards).

Full description

Principle of operation: fuel (waste woodworking: chips, bark, sawdust, firewood) is supplied by a transporter to the furnace chamber. Flames and hot furnace gases heat the coil through which thermooil circulates coming from the closed oil storage. Heated thermal oil pumps are supplied to heat exchangers (wood drying chambers (not included in the supply)) for heat transfer. The cooled thermo-oil goes back to the boiler. The furnace gases formed during the combustion process are fed into the steam generator to generate steam necessary for production needs.

The equipment consists of the following main components: fuel combustion system (heating chamber of the boiler, blow fan, gear blower fan, belt transporter for fuel supply, slag separator, dust collector, air heater, smoke pipe); circulating system (boiler housing, high-temperature pump, gear oil pump, oil-gas separator, closed expansion tank, collection of oil storage equipment, installation of electric pumps, electric pumping equipment, installation of thermometers for thermoplasters, installation of thermoplasters, equipment for thermoplaster control equipment, installation of thermoplasters and equipment for thermoplaster control equipment;

Technical characteristics: nominal thermal power of the boiler - 3500 kW, boiler performance - 158.45 t / h, oil pressure - 0.8 MPa, oil temperature - 300 ° C; steam generator performance - 1 t / h, steam pressure - 0.7 MPa, steam temperature - 175 ° C. Overall characteristics: boiler assembly (heating chamber and boiler body) weight - 56032 kg; steam generator weight - 2846 kg; air heater weight - 1230 kg. The equipment is supplied in disassembled form.

GRI 1, 2(a) and 6

What import requires

Russian bans and restrictions

May apply

Whether a measure applies to your goods is determined by the provisos in the “code” column. Measures are taken from the register as of the date the act was published; the act is named on every line

8419 (за исключением 8419 11 000 0, 8419 19 000 0, 8419 20 000 0, 8419 34 000 0, 8419 35 000 0, 8419 39 000 8, 8419 81, 8419 89 300 0, 8419 90 850 9)Out of RussiaProhibited
Отдельные виды товаров — временный запрет на вывоз
Машины, оборудование промышленное или лабораторное с электрическим или неэлектрическим нагревом (исключая печи, камеры и другое оборудование товарной позиции 8514) для обработки материалов в процессе с изменением температуры, таком как нагрев, варка, жаренье, дистилляция, ректификация, стерилизация, пастеризация, пропаривание, сушка, выпаривание, конденсирование или охлаждение, за исключением машин и оборудования, используемых в бытовых целях; водонагреватели проточные или накопительные (емкостные), неэлектрические
Постановление Правительства РФ от 09.03.2022 № 311 — until Dec 31, 2027
8419 (за исключением 8419 11 000 0, 8419 19 000 0, 8419 20 000 0, 8419 34 000 0, 8419 35 000 0Out of RussiaPermit required
Промышленная продукция
Машины, оборудование промышленное или лабораторное с электрическим или неэлектрическим нагревом (исключая печи, камеры и другое оборудование товарной позиции 8514) для обработки материалов в процессе с изменением температуры, таком как нагрев, варка, жаренье, дистилляция
Постановление Правительства РФ от 09.03.2022 № 312 — until Dec 31, 2027

Veterinary and sanitary control

Goods fall under supervision by their type and characteristics

Sanitary and epidemiological supervision (control)
rule for the whole chapter 84
Материалы, оборудование, вещества, устройства, применяемые в сфере хозяйственно-питьевого водоснабжения и при очистке сточных вод, в плавательных бассейнах; Продукция машиностроения и приборостроения производственного, медицинского и бытового назначения, кроме запасных частей к транспортным средствам и бытовой технике (за исключением контактирующих с питьевой водой и пищевыми продуктами); Продукция, изделия, являющиеся источником ионизирующего излучения, в том числе генерирующего, а также изделия и продукция (товары), содержащие радиоактивные вещества; Строительное сырье и материалы, в которых гигиеническими нормативами регламентируется содержание радиоактивных веществ, в том числе производственные отходы для повторной переработки и использования в народном хозяйстве, лом черных и цветных металлов (металлолом); Оборудование, материалы для воздухоподготовки, воздухоочистки и фильтрации; Иная продукция (товары), в отношении которой одним из государств – членов Евразийского экономического союза введены временные санитарные меры
Решение Коллегии Евразийской экономической комиссии от 17.09.2019 № 154

Conformity assessment

May apply

Whether the goods fall under a regulation depends on their name and characteristics. Check them against the list

ТР ТС 010/2011Safety of machinery and equipment
- Оборудование технологическое для пищевой, мясомолочной и рыбной промышленности — declaration of conformity or certificate of conformity (part of the heading)
- Оборудование технологическое для предприятий торговли, общественного питания и пищеблоков: оборудование для механической обработки продуктов питания, в том числе оборудование для плодоовощных баз и фабрик-заготовочных; оборудование тепловое для предприятий общественного питания, пищеблоков, а также плодоовощных баз и фабрик-заготовочных — declaration of conformity or certificate of conformity (part of the heading)
- Оборудование химическое, нефтегазоперерабатывающее — declaration of conformity or certificate of conformity (part of the heading)
- Воздухонагреватели и воздухоохладители — declaration of conformity or certificate of conformity (part of the heading)
- Оборудование для переработки полимерных материалов — declaration of conformity or certificate of conformity (part of the heading)
- Оборудование криогенное, компрессорное, холодильное, автогенное, газоочистное: установки воздухоразделительные и редких газов; аппаратура для подготовки и очистки газов и жидкостей, аппаратура тепло- и массообменная криогенных систем и установок; компрессоры (воздушные и газовые приводные); установки холодильные — declaration of conformity or certificate of conformity (part of the heading)
- Оборудование технологическое и аппаратура для нанесения лакокрасочных покрытий на изделия машиностроения — declaration of conformity or certificate of conformity (part of the heading)

Checked: the consolidated list of Government Decree No. 2425 and the lists of 42 technical regulations out of 52 adopted. The others have no list by HS code, so see the full list of regulations.

Dual use

Expert review needed

Goods fall under control by their technical characteristics, regardless of the code. Supplying without a licence when one is required is a criminal offence

Раздел 1 · Категория 1. Специальные материалы и связанные с ними оборудование и снаряжение
- Испытательное, контрольное и производственное оборудование → Оборудование, приведенное ниже, для производства или контроля конструкций из композиционных материалов объемной или слоистой структуры, определенных в пункте 1.1.2, или волокнистых или нитевидных материалов, определенных в пункте 1.3.10, а также специально разработанные для него компоненты и вспомогательные устройства: → Оборудование, специально разработанное или приспособленное для производства армирующих волокон:1.2.1.4.2 Оборудование для химического осаждения элементов или соединений из паровой фазы на нагретую нитевидную подложку в целях производства карбидкремниевых волокон;
Раздел 1 · Категория 2. Обработка материалов
- Испытательное, контрольное и производственное оборудование → Начало действия редакции - 14.06.2024. Оборудование, специально разработанное для осаждения неорганических покрытий, слоев, их обработки и активного управления процессом их нанесения и модификации поверхности, например для формирования подложек, определенных в колонке 2 таблицы к пункту 2.5.3.4, с использованием процессов, определенных в колонке 1 названной таблицы, а также специально разработанные для такого оборудования автоматизированные компоненты установки, позиционирования, манипулирования и регулирования: См. пред. ред.2.2.5.1 Производственное оборудование для химического осаждения из паровой фазы (CVD), имеющее все нижеследующее:
- 2.2.5.4 Производственное оборудование плазменного напыления, обладающее любой из следующих характеристик:
- 2.2.5.5 Производственное оборудование осаждения распылением, обеспечивающее плотность тока 0,1 мА/мм 2 или более, со скоростью осаждения 15 мкм/ч или более;
Раздел 1 · Категория 3. Электроника
- Системы, оборудование и компоненты3.1.3 Терморегулирующие системы охлаждения диспергированной жидкостью, использующие оборудование с замкнутым контуром для перемещения и регенерации жидкости в герметичной камере, в которой жидкий диэлектрик распыляется на электронные компоненты при помощи специально разработанных распыляющих сопел, применяемых для поддержания температуры электронных компонентов в пределах их рабочего диапазона, а также специально разработанные для них компоненты
Раздел 4 · вывоз по соображениям национальной безопасности · Категория 7. Морское дело
- Испытательное, контрольное и производственное оборудование7.2.2 Вулканизирующие аппараты для изготовления обтекателей очень больших размеров (более 9 м длиной и более 4,5 м диаметром)

Checked: one control list of six: dual-use goods (Russian Government Decree No. 1299 of 19.07.2022). The other five lists (nuclear, nuclear dual-use, missile, chemical, biological) are not checked here.

EAEU non-tariff regulation

Unified list of non-tariff measures (EEC Board Decision No. 30 of 21.04.2015). List entries selected by code

1.1banon import and exportpartial match
Озоноразрушающие вещества и продукция, содержащая озоноразрушающие вещества, запрещенные к ввозу и вывозу*
1 list entry
Льдогенераторы, молокоохладители
2.16licensing regimeon import and exportpartial match
Радиоэлектронные средства и (или) высокочастотные устройства гражданского назначения, в том числе встроенные либо входящие в состав других товаров
1 list entry
Высокочастотные устройства, оборудование и аппаратура

Tariff preferences

The code is on the EAEU list of preferential goods: for goods originating in a beneficiary country the duty is lower

Least developed countrieszero rate0%

46 countries

Burkina Faso, Guinea, Eritrea, Congo - Kinshasa, Timor-Leste, Afghanistan, Mauritania, Yemen, Cambodia, Lesotho, Laos, Bangladesh, Nepal, Tanzania, Palestinian Territories, Angola, Benin, Burundi, Haiti, Gambia, Guinea-Bissau, Djibouti, Zambia, Kiribati, Liberia, Madagascar, Malawi, Mali, Mozambique, Niger, Rwanda, Senegal, Myanmar (Burma), Sudan, Sierra Leone, Uganda, Chad, South Sudan, Syria, Solomon Islands, Comoros, Togo, Tuvalu, Ethiopia, Somalia, Central African Republic

The preference requires a document of origin and compliance with the direct consignment rule; customs checks the right to it at declaration.

Payments on import

Duty for this code: 0%. On top of the duty, on import into Russia you pay VAT of 22% (unless the goods are VAT-exempt) of the customs value including the duty (Article 160 of the Tax Code) and the customs processing fee — a fixed amount by value band. Customs value: the price of the goods, delivery to the border, local costs.

Import VAT in EAEU countries

Russia22%Tax Code of Russia, Art. 164(3) (Federal Law No. 425-FZ of 28.11.2025)
Kazakhstan16%Tax Code of Kazakhstan, Art. 503(1), from 01.01.2026
Belarus20%Tax Code of Belarus, Art. 122
Armenia20%Tax Code of the Republic of Armenia
Kyrgyzstan12%Tax Code of the Kyrgyz Republic

Standard rate; each country has reduced rates and exemptions for some goods. The duty for the code above is the union one, the same for all

May be VAT-exempt

The exemption under list No. 1042 applies if the goods match the description and are registered as a medical device:

8419 — Оборудование санитарно-гигиеническое, средства перемещения и перевозки 94 5100 (оборудование дезинфекционное; оборудование стерилизационное; оборудование моечное, оборудование для санитарной обработки; оборудование для очистки и обогащения воздуха; средства перемещения и перевозки медицинские (носилки, тележки и другие)
8419 89 989 0 — Приборы и аппараты для медицинских лабораторных исследований 94 4300 (анализаторы состава и свойств биологических жидкостей медицинские; приборы и аппараты для санитарно-гигиенических и бактериологических исследований измерительные; приборы и аппараты для клинико-диагностических лабораторных исследований, кроме анализаторов; приборы и аппараты для санитарно-гигиенических и бактериологических исследований, кроме измерительных; комплексы и комплекты (наборы) для клинико-диагностических лабораторных исследований; комплексы и комплекты (наборы) для санитарно-гигиенических и бактериологических исследований; приборы и аппараты вспомогательные для клинико-диагностических, санитарно-гигиенических и бактериологических исследований общего назначения)
8419 89 989 0 — Оборудование для кабинетов и палат, оборудование для лабораторий и аптек 94 5200 (термостаты электрические; установки стоматологические универсальные; оборудование кабинетов и палат; оборудование стоматологическое, зубопротезное, оториноларингологическое; оборудование рентгенологическое, радиологическое и травматологическое; оборудование лабораторное и аптечное; оборудование и агрегаты медицинские разные)

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28.29.60 — Установки для обработки материалов с использованием процессов, включающих изменение температуры, не включенные в другие группировки

Correspondence keys of the Russian Ministry of Economic Development, edition of 20.07.2023. The ministry’s caveat: Ключи отражают возможные соответствия между кодами на уровне первых шести знаков ТН ВЭД ЕАЭС (основанной на ГС) и кодами ОКПД 2 (основанного на КПЕС) по состоянию на 1 января 2022 года. Предлагаемые соответствия не являются исчерпывающими и предназначены для использования в качестве вспомогательного материала для облегчения работы по установлению возможных вариантов корреляции кодов классификаторов в отношении соответствующих категорий товаров.

Настоящие переходные ключи (сопоставительные таблицы) разработаны на основе данных агентства Евростат Комиссии Европейского союза по корреляции кодов Гармонизированной системы описания и кодирования товаров (ГС) 2022 года и Статистической классификации продукции по видам экономической деятельности в Европейском союзе (КПЕС) 2008 года. Ключи отражают возможные соответствия между кодами на уровне первых шести знаков ТН ВЭД ЕАЭС (основанной на ГС) и кодами ОКПД 2 (основанного на КПЕС) по состоянию на 1 января 2022 года. Предлагаемые соответствия не являются исчерпывающими и предназначены для использования в качестве вспомогательного материала для облегчения работы по установлению возможных вариантов корреляции кодов классификаторов в отношении соответствующих категорий товаров. Услуги не являются объектом классификации в ТН ВЭД ЕАЭС и не включены в переходные ключи. По мере внесения изменений в ОКПД 2 и ТН ВЭД ЕАЭС переходные ключи при необходимости подлежат актуализации.

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