A 3-cyanoreactor to absorber piping arrangement

CN224912119UActive Publication Date: 2026-10-30ANHUI RUIBANG BIOLOGICAL SCI & TECH CO LTD
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Patent Information

Application Number
CN202522646567.2
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2025-12-15
Publication Date
2026-10-30
Estimated Expiration
2035-12-15

AI Technical Summary

Technical Problem

[0003]本实用新型的目的在于提供一种3-氰反应器至吸收塔管道装置,可避免工艺气体在直角处集聚而堵塞弯型管道,可解决反应物料在弯型管道内堵塞而影响反应收率计算的问题,可以解决现有技术中的问题

Benefits of technology

[0013]本实用新型先是往吸收塔中加入吸收液,开启循环泵并打开喷淋装置,然后各种反应原料从进料管道进入反应器中进行反应,反应得到的物料沿着弯型管道进入吸收塔被吸收,部分未被吸收的工艺气体沿着排气管道进入下一步工序被吸收,其中,在工艺气体进行反应吸收的过程中,循环泵将吸收塔中加入的吸收液抽出,并经过软管输送至喷淋管,经喷淋头对弯型管道的直角处集聚的工艺气体进行喷淋,可避免工艺气体在直角处集聚而堵塞弯型管道,可解决反应物料在弯型管道内堵塞而影响反应收率计算的问题,且喷淋头喷射的喷淋液使用的是吸收塔中的吸收液,这样可以充分利用吸收液,也不会浪费更多的吸收液。

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Abstract

The utility model discloses a kind of 3-cyanogen reactor to absorption tower piping device, belong to chemical reaction technical field, including reactor, reactor is connected absorption tower by bent pipe, right angle of bent pipe is equipped with spraying device, spraying device is used to avoid process gas to gather at right angle and block bent pipe;The side of absorption tower is provided with circulating pump, the liquid inlet of circulating pump is connected with the lower end of absorption tower by pipeline, the liquid outlet of circulating pump is connected with the upper end of absorption tower by pipeline, and the liquid outlet of circulating pump is also connected with spraying device by hose on the pipeline connection.The utility model solves the existing process gas cooling at elbow right angle, accumulation, prone to pipe blockage, not only directly affect the progress of reaction, and also have influence on the yield calculation of reaction problem.The utility model can avoid process gas to gather at right angle and block bent pipe, can solve the problem of reaction material in bent pipe blockage and affect reaction yield calculation.
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Description

Technical Field

[0001] This utility model relates to the field of chemical reaction technology, specifically to a pipeline device from a 3-cyanide reactor to an absorption tower. Background Technology

[0002] The existing pipeline from the 3-cyanopyridine reactor to the absorption tower is arranged along the platform floor. During the experiment, the process gas temperature is approximately 370℃. The process gas cools and accumulates at the right-angle bends, which can easily lead to pipeline blockage. This not only directly affects the reaction but also the yield calculation. Utility Model Content

[0003] The purpose of this invention is to provide a pipeline device from a 3-cyanide reactor to an absorption tower, which can prevent process gas from accumulating at right angles and clogging the curved pipeline, and can solve the problem of reactant blockage in the curved pipeline affecting the calculation of reaction yield. This invention can solve the problems in the prior art.

[0004] To achieve the above objectives, this utility model provides the following technical solution:

[0005] A 3-cyanide reactor to absorption tower pipeline device includes a reactor, the reactor being connected to the absorption tower via a bent pipe, and a spray device installed at the right angle of the bent pipe, the spray device being used to prevent process gas from accumulating at the right angle and clogging the bent pipe.

[0006] A circulation pump is installed on one side of the absorption tower. The inlet of the circulation pump is connected to the lower end of the absorption tower through a pipeline, and the outlet of the circulation pump is connected to the upper end of the absorption tower through a pipeline. A spraying device is also connected to the pipeline connected to the outlet of the circulation pump through a hose.

[0007] Preferably, the upper end of the reactor is connected to the feed pipe via a flange, and the bottom of the reactor is connected to the bent pipe via a flange.

[0008] Preferably, the upper end of the absorption tower is connected to an exhaust pipe via a flange, and the bottom of the absorption tower is connected to a bent pipe via a flange.

[0009] Preferably, the spraying device includes a spray pipe and a spray head. The spray pipe is located at the right angle of the curved pipe, and the spray head is installed on the spray pipe. The spray pipe is connected to a flexible hose.

[0010] Preferably, a motor is installed on the outer wall of the curved pipe, the output shaft of the motor is mounted on a support frame, and the support frame is installed on the inner wall of the curved pipe.

[0011] Preferably, one end of the spray pipe is located inside the support frame, and the spray pipe is connected to the output shaft of the motor. The spray pipe is driven by the motor to rotate on the support frame to adjust the spray angle.

[0012] Compared with the prior art, the beneficial effects of this utility model are as follows:

[0013] This invention first involves adding absorbent liquid to the absorption tower, starting the circulation pump and opening the spray device. Then, various reaction raw materials enter the reactor through the feed pipe to react. The reacted material enters the absorption tower along the curved pipe to be absorbed. Some unabsorbed process gas enters the next process through the exhaust pipe to be absorbed. During the process gas reaction and absorption, the circulation pump extracts the absorbent liquid added to the absorption tower and delivers it to the spray pipe through a hose. The spray head sprays the process gas that accumulates at the right angle of the curved pipe, which can prevent the process gas from accumulating at the right angle and clogging the curved pipe. This solves the problem of reaction material clogging in the curved pipe and affecting the reaction yield calculation. Furthermore, the spray liquid used by the spray head is the absorbent liquid in the absorption tower, which can make full use of the absorbent liquid and avoid wasting more absorbent liquid. Attached Figure Description

[0014] Figure 1 This is a structural diagram of the pipeline device from the 3-cyanide reactor to the absorption tower of this utility model;

[0015] Figure 2 For the present utility model Figure 1 Enlarged view of point A in the image;

[0016] Figure 3 For the present utility model Figure 2 A partial cross-sectional schematic diagram;

[0017] Figure 4 For the present utility model Figure 3 Enlarged view of point B in the image;

[0018] Figure 5 This is a top-down schematic diagram of the spray device installed inside the curved pipe of this utility model.

[0019] In the diagram: 1. Reactor; 11. Feed pipe; 2. Bent pipe; 21. Motor; 22. Support frame; 3. Absorption tower; 31. Exhaust pipe; 4. Spraying device; 41. Spray pipe; 42. Spray head; 5. Circulating pump; 6. Hose. Detailed Implementation

[0020] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments. Obviously, the described embodiments are only some embodiments of the present utility model, and not all embodiments. Based on the embodiments of the present utility model, all other embodiments obtained by those of ordinary skill in the art without creative effort are within the protection scope of the present utility model.

[0021] To address the issue of existing process gases accumulating and cooling at right-angle bends, which can easily lead to pipe blockage and directly affect both the reaction process and yield calculations, please refer to [reference needed]. Figures 1-5 The following technical solution is provided in this embodiment:

[0022] A 3-cyanide reactor to absorber pipeline device includes a reactor 1, which is connected to an absorber 3 via a bent pipe 2.

[0023] The upper end of reactor 1 is connected to feed pipe 11 via flange, and the bottom of reactor 1 is connected to bent pipe 2 via flange.

[0024] The upper end of the absorption tower 3 is connected to the exhaust pipe 31 via a flange, and the bottom of the absorption tower 3 is connected to the bent pipe 2 via a flange.

[0025] A spray device 4 is installed at the right angle of the bent pipe 2. The spray device 4 is used to prevent process gas from accumulating at the right angle and clogging the bent pipe 2.

[0026] A circulation pump 5 is installed on one side of the absorption tower 3. The inlet of the circulation pump 5 is connected to the lower end of the absorption tower 3 through a pipeline, and the outlet of the circulation pump 5 is connected to the upper end of the absorption tower 3 through a pipeline. The pipeline connected to the outlet of the circulation pump 5 is also connected to the spray device 4 through a hose 6.

[0027] It should be noted that during the process gas reaction and absorption, the circulating pump 5 extracts the absorbent added to the absorption tower 3 and delivers it to the spray device 4 through the hose 6. The spray device 4 sprays the process gas that accumulates at the right angle of the bend pipe 2, which can prevent the process gas from accumulating at the right angle and clogging the bend pipe 2. This solves the problem of the reactants clogging in the bend pipe 2 and affecting the reaction yield. Moreover, the spray liquid sprayed by the spray device 4 is the absorbent in the absorption tower 3, so the absorbent can be fully utilized and no more absorbent is wasted.

[0028] In this embodiment, the spraying device 4 includes a spray pipe 41 and a spray head 42. The spray pipe 41 is located at the right angle of the curved pipe 2, and the spray head 42 is installed on the spray pipe 41. The spray pipe 41 is connected to the hose 6. A motor 21 is installed on the outer wall of the curved pipe 2. The output shaft of the motor 21 is installed on the support frame 22. The support frame 22 is installed on the inner wall of the curved pipe 2. One end of the spray pipe 41 is located inside the support frame 22, and the spray pipe 41 is connected to the output shaft of the motor 21. The spray pipe 41 is driven by the motor 21 to rotate on the support frame 22 to adjust the spraying angle.

[0029] It should be noted that when the spraying device 4 sprays the spraying liquid, the motor 21 can drive the spraying pipe 41 to rotate on the support frame 22 to adjust the spraying angle. This can better spray the process gas that accumulates at the right angle of the curved pipe 2, so that the process gas no longer accumulates at the right angle of the curved pipe 2, thus avoiding blockage of the curved pipe 2 and affecting the calculation of the reaction yield.

[0030] Working principle: First, absorbent liquid is added to absorption tower 3, circulation pump 5 is turned on and spray device 4 is opened. Then, various reaction raw materials enter reactor 1 from feed pipe 11 to react. The reacted material enters absorption tower 3 along curved pipe 2 and is absorbed. Some unabsorbed process gas enters the next process through exhaust pipe 31 to be absorbed. During the process gas reaction and absorption, circulation pump 5 extracts the absorbent liquid added to absorption tower 3 and delivers it to spray pipe 41 through hose 6. Spray head 42 sprays the process gas that accumulates at the right angle of curved pipe 2, which can prevent process gas from accumulating at the right angle and clogging curved pipe 2. It can solve the problem of reaction material clogging in curved pipe 2 and affecting the reaction yield calculation. Moreover, the spray liquid sprayed by spray head 42 is the absorbent liquid in absorption tower 3, so the absorbent liquid can be fully utilized and no more absorbent liquid is wasted.

[0031] It should be noted that, in this document, relational terms such as "first" and "second" are used only to distinguish one entity or operation from another, and do not necessarily require or imply any such actual relationship or order between these entities or operations. Furthermore, the terms "comprising," "including," or any other variations thereof are intended to cover non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements includes not only those elements but also other elements not expressly listed, or elements inherent to such process, method, article, or apparatus.

[0032] Although embodiments of the present invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made to these embodiments without departing from the principles and spirit of the present invention, the scope of which is defined by the appended claims and their equivalents.

Claims

1. A pipeline system from a 3-cyanide reactor to an absorption tower, comprising a reactor (1), characterized in that: The reactor (1) is connected to the absorption tower (3) through a curved pipe (2). A spray device (4) is installed at the right angle of the curved pipe (2). The spray device (4) is used to prevent process gas from accumulating at the right angle and clogging the curved pipe (2). A circulation pump (5) is provided on one side of the absorption tower (3). The inlet of the circulation pump (5) is connected to the lower end of the absorption tower (3) through a pipe. The outlet of the circulation pump (5) is connected to the upper end of the absorption tower (3) through a pipe. The outlet of the circulation pump (5) is also connected to the spray device (4) through a flexible hose (6).

2. The pipeline device from a 3-cyanide reactor to an absorption tower according to claim 1, characterized in that: The upper end of the reactor (1) is connected to the feed pipe (11) via a flange, and the bottom of the reactor (1) is connected to the bent pipe (2) via a flange.

3. The pipeline device from a 3-cyanide reactor to an absorption tower according to claim 2, characterized in that: The upper end of the absorption tower (3) is connected to the exhaust pipe (31) via a flange, and the bottom of the absorption tower (3) is connected to the bent pipe (2) via a flange.

4. The pipeline device from a 3-cyanide reactor to an absorption tower according to claim 3, characterized in that: The spray device (4) includes a spray pipe (41) and a spray head (42). The spray pipe (41) is located at the right angle of the curved pipe (2). The spray head (42) is provided on the spray pipe (41), and the spray pipe (41) is connected to the hose (6).

5. The pipeline device from a 3-cyanide reactor to an absorption tower according to claim 4, characterized in that: A motor (21) is installed on the outer wall of the curved pipe (2), and the output shaft of the motor (21) is installed on the support frame (22), which is installed on the inner wall of the curved pipe (2).

6. The pipeline device from a 3-cyanide reactor to an absorption tower according to claim 5, characterized in that: One end of the spray pipe (41) is located inside the support frame (22), and the spray pipe (41) is connected to the output shaft of the motor (21). The spray pipe (41) is driven by the motor (21) to rotate on the support frame (22) to adjust the spray angle.