Coagulation method and equipment for halogenated butyl rubber

A technology of halogenated butyl rubber and coagulation method, which is applied in the field of butyl rubber synthesis, which can solve the problems of increasing the load of the first coagulation tank to remove hexane, consuming large and low-pressure steam, and poor flexibility of the device, so as to reduce steam consumption , Reduction of circulating water consumption, and the effect of process optimization

Active Publication Date: 2022-02-08
ZHEJIANG CENWAY MATERIALS CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The main problems of adopting the above scheme are: ① high energy consumption, due to the low injection efficiency of the steam jet pump, a large amount of low-pressure steam needs to be consumed to maintain the low pressure of the second and third condensation kettles; ② high material consumption, due to the low pressure of the second 2. The hexane-containing gas sucked by the third condensation tank needs to be returned to the first condensation tank, which obviously increases the load of the first condensation tank to remove hexane
In addition, the system adopts a process of connecting three kettles in series. The second and third coagulation kettles have similar functions. When one of the equipment is abnormal due to mechanical failure or process fluctuation, the whole line must be shut down for processing, and the flexibility of the device is very poor.

Method used

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  • Coagulation method and equipment for halogenated butyl rubber
  • Coagulation method and equipment for halogenated butyl rubber

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] Such as figure 1 As shown, a device suitable for coagulation of halobutyl rubber. Including the first coagulation tank 1, the second coagulation tank 2, the third coagulation tank 3, the first delivery pump 10, the second delivery pump 20, the third delivery pump 30, the first water ring vacuum pump 100, and the second water ring vacuum pump 200 , condenser 300 and heat pump system 400; the top outlet of the first condensation kettle 1 is connected with the inlet of the condenser 300 through the first gas phase pipe 4; the bottom outlet of the first condensation kettle 1 is connected with the first colloidal particle water pipe 7 The feed port of the second condensation kettle 2 is connected; the top outlet of the second condensation kettle 2 is connected with the inlet of the condenser 300 through the second gas phase pipe 5; the bottom outlet of the second condensation kettle 2 is connected through the second colloidal water pipe 8 is connected with the feed port of ...

Embodiment 2

[0035]The equipment used in this embodiment is the same as that in Embodiment 1, but the control process is different.

[0036] Specifically, the only difference is that this embodiment adopts a two-pot differential pressure process.

[0037] More specifically: in this embodiment, the material inlet of the second coagulation tank 2 is closed, and the valve on the first regulating pipeline 40 is opened. In this way, the colloidal water pumped out from the first coagulation tank 1 directly enters the third coagulation tank 3 for operation.

Embodiment 3

[0039] The equipment used in this embodiment is the same as that in Embodiment 1, but the control process is different.

[0040] Specifically, the only difference is that this embodiment adopts a two-pot differential pressure process.

[0041] More specifically: in this embodiment, the material inlet of the third coagulation tank 3 is closed, and the valve on the second regulating pipeline 50 is opened. In this way, the colloidal water pumped out from the second coagulation tank 2 directly enters the solid-liquid separation device for operation.

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Abstract

The invention relates to a coagulation method of halogenated butyl rubber, which belongs to the technical field of butyl rubber synthesis. After the butyl rubber glue has undergone a halogenation reaction, and then undergoes a neutralization reaction, it enters the first coagulation kettle, and hot water is also passed into the first coagulation kettle, so that the first gas phase containing hexane is generated in the first coagulation kettle. The first gas phase is condensed by the condenser and then enters the hexane purification system for treatment; the colloidal water in the first coagulation tank is sent to the second coagulation tank through the first delivery pump, so that the second gas phase containing hexane is produced in the second coagulation tank, The second gas phase is extracted from the second condensation tank by the first water ring vacuum pump, condensed by the condenser, and then enters the hexane purification system for treatment. Using a mechanical heat pump to recycle the steam waste heat at the top of the first condensation tank will not only reduce the steam consumption in the production process of halogenated butyl, but also reduce the amount of circulating water used for condensing steam.

Description

technical field [0001] The invention relates to a coagulation method of halogenated butyl rubber, which belongs to the technical field of butyl rubber synthesis. Background technique [0002] Coagulation is an important step in the production of halobutyl rubber. It is the operation of removing hexane by neutralizing and adding additives to the coagulation tank after neutralizing the glue generated by the polymerization reaction. It also facilitates subsequent dehydration. In the prior art, the coagulation usually adopts a three-pot differential pressure process, and the second and third coagulation pots need to maintain a relatively low pressure to ensure the removal of hexane. The existing process uses a steam jet pump as a vacuum device to maintain the lower pressure of the second and third condensation tanks, and the steam medium and the pumped hexane-containing gas are returned to the first condensation tank to replenish the first condensation tank. Steam, thereby re...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F6/12C08F8/20C08F210/12
CPCC08F6/12C08F8/20C08F210/12C08L23/28
Inventor 周文祥任纪文张阳彭照亮叶媛园
Owner ZHEJIANG CENWAY MATERIALS CO LTD
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