Hydrogenated dimer acid refined material heat exchanger

By adopting the internal and external double-layer corrosion protection layer and multi-layer insulation structure in the hydrogenated dimer acid refined material heat exchanger, the problems of poor corrosion resistance and insufficient media insulation are solved, and more efficient energy utilization and lower energy consumption waste are achieved.

CN223005377UActive Publication Date: 2025-06-20LIANCHENG BAIXIN SCI & TECH CO LTD
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Patent Information

Application Number
CN202422217020.6
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-09-10
Publication Date
2025-06-20
Estimated Expiration
2034-09-10

AI Technical Summary

Technical Problem

The existing heat exchangers of hydrogenated dimer acid refined materials have poor anti-corrosion effect and insufficient thermal insulation of the medium, resulting in large waste of energy consumption.

Method used

A hydrogenated dimer acid refined material heat exchanger is designed, adopting an internal and external double-layer corrosion-proof layer and a multi-layer insulation structure, including a heat conducting pipe, an external corrosion-proof layer, an internal corrosion-proof layer and a multi-layer insulation layer to improve corrosion-proof and thermal insulation performance.

Benefits of technology

By enhancing the design of the anti-corrosion layer and the insulation layer, the anti-corrosion effect and insulation performance of the heat exchanger are significantly improved, and energy consumption and waste are reduced.

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Abstract

The utility model discloses a hydrogenated dimer acid refined material heat exchanger, which relates to the technical field of hydrogenated dimer acid production equipment, and comprises a coil pipe heat exchanger main body, and the coil pipe heat exchanger main body comprises an inner pipe and an outer pipe fixedly communicated with the inner pipe; the inner pipe comprises a heat conduction pipe, an outer anti-corrosion layer fixedly arranged on the outer side of the heat conduction pipe in an attached mode and a first inner anti-corrosion layer fixedly arranged on the inner side of the heat conduction pipe in an attached mode. The outer pipe comprises a stainless steel pipe, a second inner anti-corrosion layer fixedly arranged on the inner side of the stainless steel pipe in an attached mode and a heat preservation layer. The utility model has the advantages that the outer corrosion-resistant layer and the first inner corrosion-resistant layer are respectively arranged on the inner side and the outer side of the heat conduction pipe, the stainless steel pipe is adopted as the inner pipe for conveying heat exchange media, and the second inner corrosion-resistant layer is arranged in the stainless steel pipe, so that protection is provided after hydrogenated dimer acid is contacted with the flowing heat exchange media in the heat conduction pipe, and the corrosion-resistant effect is enhanced; the heat preservation layer is arranged outside the stainless steel pipe, temperature loss of media transmitted by the outer pipe is reduced, and energy consumption and waste are reduced.
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Description

Technical Field

[0001] The utility model relates to the technical field of hydrogenated dimer acid production equipment, and more specifically, to a heat exchanger for refined materials of hydrogenated dimer acid. Background Art

[0002] Hydrogenated dimer acid is a product obtained through chemical reactions and is usually used in the production of lubricant additives, resin modifiers, surfactants, etc. The refining process is to further purify and process the initial product to remove impurities and improve the product purity and performance. The heat exchanger plays a key role in temperature control during this process;

[0003] The heat exchanger for refined materials of hydrogenated dimer acid is a device used in chemical processes and is mainly used for heat exchange in the production process of hydrogenated dimer acid. During this process, the role of the heat exchanger is to cool or heat the hydrogenated dimer acid material through heat exchange to meet the specific temperature requirements of subsequent process steps {such as the "coiled tube heat exchanger" in the publication (publication) number: CN220460646U, an inclined reaction kettle with a heat exchanger that can be quickly disassembled} for use;

[0004] For the above-mentioned "coiled tube heat exchanger", the coiled tube part is built into the "reaction kettle", and the other part of the coiled tube passes through the outside of the "reaction kettle". When it is applied in the production of hydrogenated dimer acid, there are disadvantages such as poor anti-corrosion effect, and insufficient heat preservation of the transmission medium outside the coiled tube, resulting in large energy consumption and waste. Summary of the Utility Model

[0005] The purpose of the utility model is: to solve the above technical problems, the utility model provides a heat exchanger for refined materials of hydrogenated dimer acid.

[0006] The utility model specifically adopts the following technical solutions to achieve the above purpose:

[0007] The utility model provides a heat exchanger for refined materials of hydrogenated dimer acid, which includes a coiled tube heat exchanger main body, and the coiled tube heat exchanger main body includes an inner tube and an outer tube that is fixedly connected and communicated with it;

[0008] The inner tube includes a heat conduction tube, an outer anti-corrosion layer fixedly attached to the outside of the heat conduction tube, and a first inner anti-corrosion layer fixedly attached to the inside of the heat conduction tube;

[0009] The outer tube includes a stainless steel tube, a second inner anti-corrosion layer fixedly attached to the inside of the stainless steel tube, and a heat preservation layer fixedly attached to the outside of the stainless steel tube.

[0010] As a preferred technical solution of the utility model, the material of the heat conduction tube is copper or aluminum alloy.

[0011] As a preferred technical solution of the present utility model, the material of the outer anti-corrosion layer is stainless steel or titanium alloy.

[0012] As a preferred technical solution of the utility model, the first inner anti-corrosion layer and the second inner anti-corrosion layer are nickel-plated layers.

[0013] As a preferred technical solution of the utility model, the thermal insulation layer includes a moisture-proof layer fixedly mounted on the outside of the stainless steel pipe, an anti-heat escape layer fixedly mounted on the outside of the moisture-proof layer, and a protective layer fixedly mounted on the outside of the anti-heat escape layer.

[0014] As a preferred technical solution of the utility model, the moisture-proof layer is an aluminum foil layer;

[0015] The anti-heat-escape layer is a rock wool layer;

[0016] The protective layer is a rubber-plastic thermal insulation material layer.

[0017] The beneficial effects of the utility model are as follows:

[0018] By using the heat-conducting pipe 21 as the heat exchange body for the inner tube 2, arranging the outer anti-corrosion layer 22 and the first inner anti-corrosion layer 23 on the inner and outer sides of the heat-conducting pipe 21 respectively, and using the stainless steel pipe 31 for the inner tube 2 to transport the heat exchange medium, and arranging the second inner anti-corrosion layer 32 in the stainless steel pipe 31, protection is provided after the contact between the hydrogenated dimer acid and the heat exchange medium flowing in the heat-conducting pipe 21, so as to enhance the anti-corrosion effect; and an insulation layer is arranged outside the stainless steel pipe 31 to reduce the temperature loss of the medium transmitted by the outer tube 3 to reduce energy waste. BRIEF DESCRIPTION OF THE DRAWINGS

[0019] Figure 1 It is a schematic diagram of the implementation structure of the utility model.

[0020] Figure numerals: coil heat exchanger body -1, inner tube -2, outer tube -3, heat transfer tube -21, outer anti-corrosion layer -22, first inner anti-corrosion layer -23, stainless steel tube -31, second inner anti-corrosion layer -32, moisture-proof layer -33, anti-heat escape layer -34, protective layer -35. DETAILED DESCRIPTION

[0021] like Figure 1 As shown, the utility model proposes: a heat exchanger for hydrogenated dimer acid refined materials, including a coil heat exchanger body 1, the coil heat exchanger body 1 includes an inner tube 2 and an outer tube 3 connected and fixed thereto (as shown in the figure, a production equipment is provided, the production equipment is such as a reactor, etc.; the coil heat exchanger body 1 is applied to the production equipment, the inner tube 2 is placed inside the production equipment, and the outer tube 3 is exposed to connect to an external medium, the medium can be cold and hot water or cold and hot air, etc.);

[0022] The inner tube 2 includes a heat-conducting tube 21, an outer anti-corrosion layer 22 fixedly attached to the outside of the heat-conducting tube 21, and a first inner anti-corrosion layer 23 fixedly attached to the inside of the heat-conducting tube 21, so as to provide protection after contact between hydrogenated dimer acid and the heat-exchanging medium flowing in the heat-conducting tube 21, and enhance the anti-corrosion effect;

[0023] Among them, the material of the heat-conducting tube 21 is copper or aluminum alloy, etc., to provide good heat conduction and enhance the heat exchange effect;

[0024] The material of the outer anti-corrosion layer 22 is stainless steel or titanium alloy, etc. (the outer anti-corrosion layer 22 can be covered with a thin layer of stainless steel or titanium alloy on the outside of the heat-conducting tube 21 by means of explosion welding, socketing or chemical vapor deposition (CVD), etc.). The stainless steel can be 316L stainless steel, etc.;

[0025] The first inner anti-corrosion layer 23 is a nickel-plated layer, etc. (the nickel-plated layer is set: a nickel metal layer is deposited on the inner wall of the heat-conducting tube 21 by electroplating or electroless plating process), providing good heat conductivity and corrosion resistance protection;

[0026] The outer tube 3 includes a stainless steel tube 31 and a second inner anti-corrosion layer 32 fixedly attached to the inside of the stainless steel tube 31, providing protection after contact with the heat-exchanging medium flowing in the stainless steel tube 31;

[0027] And a heat-insulating layer fixedly attached to the outside of the stainless steel tube 31, reducing the temperature loss of the medium transmitted by the outer tube 3 to reduce energy waste;

[0028] Among them, the second inner anti-corrosion layer 32 is a nickel-plated layer, etc.;

[0029] To implement the above-mentioned heat-insulating layer for use, it is proposed that, as Figure 1 shown, the specific structure and composition method of the heat-insulating layer can be: the heat-insulating layer includes a moisture-proof layer 33 fixedly attached to the outside of the stainless steel tube 31, which can greatly reduce moisture penetration and improve corrosion resistance;

[0030] A heat anti-loss layer 34 fixedly attached to the outside of the moisture-proof layer 33, suppressing heat transfer to reduce heat loss in the stainless steel tube 31;

[0031] And a protective layer 35 fixedly attached to the outside of the heat anti-loss layer 34, protecting the heat anti-loss layer 34;

[0032] Among them, the moisture-proof layer 33 is an aluminum foil layer, etc.; the aluminum foil layer has good moisture-proof performance and can provide a certain degree of heat insulation;

[0033] The heat anti-loss layer 34 is a rock wool layer, etc.; the rock wool layer has good heat insulation performance;

[0034] The protective layer 35 is a layer of rubber and plastic thermal insulation material, etc.; the layer of rubber and plastic thermal insulation material is preferably flexible to facilitate wrapping and fitting to the heat leakage prevention layer 34; the layer of rubber and plastic thermal insulation material refers to a thermal insulation layer made of rubber and plastic (a blend of rubber and plastic) material.

[0035] The foregoing has shown and described the basic principles, main features and advantages of the present invention. For those skilled in the art, it is obvious that the present invention is not limited to the details of the above-described exemplary embodiments, and without departing from the spirit or basic characteristics of the present invention, the present invention can be implemented in other specific forms. Therefore, from any point of view, the embodiments should be regarded as exemplary and non-limiting. The scope of the present invention is defined by the appended claims rather than the above description. Therefore, it is intended to embrace all changes falling within the meaning and scope of the equivalent elements of the claims in the present invention. Any reference signs in the claims should not be construed as limiting the claims involved.

[0036] In addition, it should be understood that although this specification is described in terms of embodiments, not every embodiment only contains an independent technical solution. This narrative manner of the specification is only for clarity. Those skilled in the art should regard the specification as a whole, and the technical solutions in each embodiment can also be appropriately combined to form other embodiments that can be understood by those skilled in the art.

Claims

1. A heat exchanger for refining materials of hydrogenated dimer acid, comprising a coiled tube heat exchanger body (1), wherein the coiled tube heat exchanger body (1) comprises an inner tube (2) and an outer tube (3) connected and fixed thereto; It is characterized in that The inner tube (2) comprises a heat conducting tube (21), an outer anti-corrosion layer (22) fixedly attached to the outer side of the heat conducting tube (21), and a first inner anti-corrosion layer (23) fixedly attached to the inner side of the heat conducting tube (21); The outer tube (3) comprises a stainless steel tube (31), a second inner anti-corrosion layer (32) bonded and fixed to the inner side of the stainless steel tube (31), and a thermal insulation layer bonded and fixed to the outer side of the stainless steel tube (31).

2. A heat exchanger for refining materials of hydrogenated dimer acid according to claim 1, characterized in that: The heat conducting pipe (21) is made of copper or aluminum alloy.

3. A heat exchanger for hydrogenated dimer acid refining materials according to claim 1, characterized in that: The material of the outer anti-corrosion layer (22) is stainless steel or titanium alloy.

4. A heat exchanger for refining materials of hydrogenated dimer acid according to claim 1, characterized in that: The first inner anti-corrosion layer (23) and the second inner anti-corrosion layer (32) are nickel-plated layers.

5. A heat exchanger for refining materials of hydrogenated dimer acid according to claim 1, characterized in that: The thermal insulation layer comprises a moisture-proof layer (33) fixedly attached to the outside of the stainless steel pipe (31), a heat-preventing layer (34) fixedly attached to the outside of the moisture-proof layer (33), and a protective layer (35) fixedly attached to the outside of the heat-preventing layer (34).

6. A heat exchanger for refining materials of hydrogenated dimer acid according to claim 5, characterized in that: The moisture-proof layer (33) is an aluminum foil layer; The anti-heat-escape layer (34) is a rock wool layer; The protective layer (35) is a rubber-plastic thermal insulation material layer.

Citation Information

Patent Citations

  • Inclined reaction kettle with quickly detachable heat exchanger

    CN220460646U