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Vacuum cooling crystallization system for adipic acid production

A vacuum cooling and crystallization system technology, which is applied in crystallization separation, solution crystallization, separation/purification of carboxylic acid compounds, etc., can solve problems such as personnel health and environmental pollution, achieve strong equipment compatibility, and solve personnel health and environmental pollution Effect

Inactive Publication Date: 2020-11-13
HENAN SHENMA NYLON CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] In order to solve the above-mentioned technical problems, the object of the present invention is to propose a vacuum cooling crystallization system for the production of adipic acid, which realizes the cooling crystallization of the material through the cooperation of the vacuum degree and the feeding and discharging speed; in addition, the system passes The combined use of the follow-up spray recovery device can absorb the nitrous gas volatilized in the feed liquid, thereby completely solving the problems of personnel health and environmental pollution caused by the volatilization of nitrous gas in the prior art

Method used

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  • Vacuum cooling crystallization system for adipic acid production

Examples

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Effect test

Embodiment 1

[0029] A vacuum cooling crystallization system for adipic acid production, such as figure 1 As shown, the system includes a crystallization tank 1 , a vacuum pump 20 , a spray recovery device 3 and a pipeline connecting the crystallization tank 1 , the vacuum pump 20 and the spray recovery device 3 .

[0030] The upper part of the crystallization tank 1 is provided with a feed pipe 4, one end of the feed pipe 4 communicates with the crystallization tank 1, and the other end of the feed pipe 4 is connected with the adipic acid feed pump; the feed pipe 4 is provided with an electrical connection The feed regulating valve 6 and the feed flow meter 11 can feed back the opening and closing of the feed regulating valve 6 through the feed flow meter 11 . The bottom of the crystallization tank 1 is provided with a discharge pipe 5; one end of the discharge pipe 5 is connected with the crystallization tank 1, and the other end of the discharge pipe 5 is connected with the downstream ad...

Embodiment 2

[0044] A vacuum cooling crystallization system for the production of adipic acid. The difference from Example 1 is that the spray recovery device used in the system is composed of three-stage absorption towers connected in series, and the middle part of each absorption tower is provided with three sections of packing layers. The used The packing is Taylor packing;

[0045] Each absorption tower contains a set of independent spray and water pump circulation system, the spray liquid used is water; the nitrous gas sucked from the crystallization tank enters from the lower part of the absorption tower through the vacuum pump outlet pipe, and is absorbed by water spray. Finally, the gas containing nitrous gas that has not been completely absorbed is discharged from the exhaust port on the top of the tower and enters the bottom of the next absorption tower; the gas containing nitrous gas that finally enters from the first absorption tower, of which the nitrous gas After the gas is a...

Embodiment 1

[0046] The setting of the single-stage absorption tower in Example 1 is suitable for the case where the processing capacity is small, and the nitrous gas extracted by the vacuum pump can be neutralized and absorbed by the lye. When the production scale of adipic acid is large, the single-stage absorption tower is not enough to absorb all the nitrous gas pumped out by the vacuum pump, and more nitrous gas is generated during the cooling process, and the direct neutralization reaction will cause lye and nitrous gas Therefore, multi-stage absorption towers are set up in series, and water is used to absorb nitrous gas to obtain nitric acid again; at the same time, packing layers are set in sections in each absorption tower to improve the absorption rate of nitrous gas; According to the measurement of the analyzer, the content of nitrous gas at the end of the vacuum pump outlet pipe is 3000ppm. After being absorbed in series by three-stage absorption towers, the content of nitrous g...

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Abstract

The invention belongs to the technical field of adipic acid production equipment, and particularly relates to a vacuum cooling crystallization system for adipic acid production. The system comprises acrystallizing tank for placing feed liquid, a vacuum pump, a spray recovery device and a pipeline for connecting the crystallizing tank, the vacuum pump and the spray recovery device, and a feeding pipe is arranged at the upper part of the crystallizing tank and is communicated with the crystallizing tank; a discharge pipe is arranged at the bottom of the crystallizing tank and is communicated with the crystallizing tank; a bypass branch pipe is arranged between the feeding pipe and the discharging pipe; a coil pipe is arranged on the side wall of the crystallizing tank, the inlet end of thecoil pipe is connected with a steam inlet wire arranged outside the crystallizing tank, and the outlet end of the coil pipe is connected with a steam outlet wire arranged outside the crystallizing tank; and a stirring device for mixing feed liquid is also arranged in the crystallizing tank. The system is matched with a subsequent spray recovery device for use, so that nitrite gas volatilized fromfeed liquid can be absorbed in the crystallization process, and the problems of personnel health and environmental pollution caused by volatilization of the nitrite gas in the prior art are thoroughlysolved.

Description

technical field [0001] The invention belongs to the technical field of adipic acid production equipment, and in particular relates to a vacuum cooling crystallization system for adipic acid production. Background technique [0002] In the production of adipic acid, nitric acid oxidizes KA oil with the most efficient process and the highest reaction yield. Therefore, nitric acid is often used as an oxidant in the production of adipic acid. Based on the purpose of stable production, easy control, reducing side reactions, and increasing the yield of adipic acid, in the adipic acid production process, an excess of nitric acid is usually added, and the nitric acid will be recovered step by step at the end of the synthesis of adipic acid. [0003] However, usually when adipic acid enters the crystallization recovery system, there will still be 5-10% nitric acid in the solution. Since most of the cooling crystallization equipment currently used is an open coil crystallizer, nitrous...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D9/02B01D53/54B01D53/78C07C51/43C07C55/14
CPCB01D9/00B01D53/54B01D53/78C07C51/43C07C55/14
Inventor 赵铎史红军陈聚良华东旭代世磊赵振忠刘镇江孙浩杰马晓鹏王永雷吕自豪孙涛涛李迎军
Owner HENAN SHENMA NYLON CHEM