Production system of dehydrated caprolactam and method thereof

A caprolactam and production system technology, applied in the field of caprolactam dehydration production system, can solve the problems of high comprehensive energy consumption, large energy consumption, water content changes, etc., achieve high steam utilization rate and reduce steam consumption

Active Publication Date: 2013-03-27
SEDIN NINGBO ENG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The existing caprolactam dehydration process and production system are usually evaporation and flash evaporation, and the water in the caprolactam aqueous solution is evaporated and removed by the evaporator. However, as the water content of caprolactam decreases, the dehydration temperature required for the caprolactam material gradually increases. High, it will lead to the decomposition and deterioration of caprolactam, and at the same time, due to the change of water content, the heat grade required for evaporation will be different
Theref

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  • Production system of dehydrated caprolactam and method thereof

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Embodiment 1

[0025] The invention discloses a production system for caprolactam dehydration, such as figure 1 As shown, it includes a feed preheater 1, a first-effect evaporator 2, a second-effect evaporator 3, a three-effect evaporator 4, a rectification tower 5 and a caprolactam dehydration storage tank 6, and the feed preheater 1 passes through a one-effect exchange Heater 7 is connected to the inlet of first-effect evaporator 2, the lower end material outlet of first-effect evaporator 2 is connected to the inlet of second-effect evaporator 3 through second-effect heat exchanger 8, and the upper end steam outlet of first-effect evaporator 2 is connected to second-effect evaporator 2. The lower end material outlet of the second effect evaporator 3 is connected to the inlet of the third effect evaporator 4 through the third effect heat exchanger 9, and the upper steam outlet of the second effect evaporator 3 is connected to the third effect heat exchanger 9 , The material outlet at the lo...

Embodiment 2

[0029] The invention discloses a production system for caprolactam dehydration, such as figure 1 As shown, it includes a feed preheater 1, a first-effect evaporator 2, a second-effect evaporator 3, a three-effect evaporator 4, a rectification tower 5 and a caprolactam dehydration storage tank 6, and the feed preheater 1 passes through a one-effect exchange Heater 7 is connected to the inlet of first-effect evaporator 2, the lower end material outlet of first-effect evaporator 2 is connected to the inlet of second-effect evaporator 3 through second-effect heat exchanger 8, and the upper end steam outlet of first-effect evaporator 2 is connected to second-effect evaporator 2. The lower end material outlet of the second effect evaporator 3 is connected to the inlet of the third effect evaporator 4 through the third effect heat exchanger 9, and the upper steam outlet of the second effect evaporator 3 is connected to the third effect heat exchanger 9 , The material outlet at the lo...

Embodiment 3

[0033] A kind of production method of caprolactam dehydration of the present invention, as figure 1 shown, including the following steps:

[0034] (1) Send the 30% caprolactam aqueous solution into the feed preheater 1, and then send it to the first-effect evaporator 2 after being heated by the first-effect heat exchanger 7, at a temperature of 115°C and a pressure of 0.2MPaG. Evaporation operation, the bottom of the first-effect evaporator 2 obtains a caprolactam aqueous solution with a concentration of 38%, and the water vapor evaporated from the top of the first-effect evaporator 2 is sent to the second-effect heat exchanger 8 as a heating heat source;

[0035](2) After the caprolactam aqueous solution with a concentration of 38% is heated by the second-effect heat exchanger 8, it is sent to the second-effect evaporator 3 by using the pressure difference or potential difference, and evaporated at a temperature of 105°C and a pressure of 0.05MPaG Operation, the bottom of th...

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Abstract

The invention discloses a production system of dehydrated caprolactam and a method thereof. The system is characterized by comprising a first-efficiency heat exchanger, a first-efficiency evaporator, a second-efficiency heat exchanger, a second-efficiency evaporator, a third-efficiency heat exchanger and a third-efficiency evaporator which are sequentially connected and then connected with a rectifying tower. The production method comprises the following steps of: pre-heating the materials and then sending the materials to the first-efficiency evaporator for evaporation under the conditions of a temperature of 115-125 DEG C and a pressure range from 0.2 to 0.35MPaG; heating the materials and sending the materials to the second-efficiency evaporator for evaporation under the conditions of a temperature of 105-110 DEG C and a pressure range from 0.05 to 0.1MPaG; heating the materials and sending the materials to the third-efficiency evaporator for evaporation under the conditions of a temperature of 85-95 DEG C and a pressure range from 0.05 to 0.08MPaG; and sending the materials to the rectifying tower for rectification under the conditions of a temperature of 90 DEG C and a pressure range from 0.05 to 0.08MPaG, wherein the dehydrated caprolactam with less than 0.001% of water is obtained at the bottom of the rectifying tower. The invention has the advantages that multiple effective and gradient utilization of steam is realized through rational control of pressure and temperature, a large amount of cold and heat are saved, and the thermal decomposition of the caprolactam is reduced at a lower operating temperature.

Description

technical field [0001] The invention relates to a production system and method for caprolactam dehydration. Background technique [0002] Caprolactam (CPL for short) is one of the important organic chemical raw materials. Its main purpose is to produce polyamide chips (usually called nylon-6 chips or nylon-6 chips) through polymerization, which can be further processed into nylon fibers, engineering plastics, plastics, etc. film. The industrial production of caprolactam is to make cyclohexanone oxime undergo Beckmann rearrangement reaction under the condition of fuming sulfuric acid to generate caprolactam. After the rearrangement reaction, the mixed aqueous solution containing fuming sulfuric acid and caprolactam is neutralized with ammonia water to produce Ammonium sulfate, then separate and purify ammonium sulfate and crude amide. Usually, the organic solvent benzene is used for the first extraction, and then the water is used for the second extraction to release the ca...

Claims

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Application Information

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IPC IPC(8): B01D1/26B01D1/30B01D3/14C07D223/10C07D201/16
CPCY02P20/10
Inventor 谷新春梁正王宇光马文华颜焕敏王爱芳
Owner SEDIN NINGBO ENG
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