Preparation method and system of mono-isocyanate

A monoisocyanate and isocyanate technology, applied in the field of monoisocyanate preparation, can solve the problems of increased total organic matter, urea or hydrochloride, poor economy, etc., and achieve the effect of low solid waste and high yield

Active Publication Date: 2018-04-20
WANHUA CHEM GRP CO LTD
View PDF24 Cites 8 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although this scheme can obtain isocyanate with low boiling point, because the cracking temperature of carbamate is higher than that of carbamoyl chloride, this process is more likely to lead to an increase in the polymer of monoisocyanate, resulting in a decline in the overall yield
[0010] At the same time, in the process of preparing monoisocyanate by phosgenation method, excessive phosgene is generally used to promote the complete reaction, so as to avoid further reaction of unreacted amine with photochemical product hydrogen chloride or isocyanate and its carbamoyl chloride to form urea species or hydrochlorides, resulting in reduced yield and equipment blockage
If this part of excess phosgene is to be recovered, due to the relatively low boiling point of monoisocyanate, a small amount of isocyanate will be entrained in the reaction tail gas and dephosgene tail gas, and these monoisocyanates will often bring great difficulties to the subsequent recovery of phosgene
If this part of phosgene is not recovered, on the one hand, the economy of the whole process is poor, and in addition, because the entrained monoisocyanate enters the phosgene decomposition system, it is easy to cause the increase of the total organic matter in the phosgene decomposition wastewater, resulting in the difficulty of subsequent wastewater treatment and cost increase
Therefore, in the traditional process of preparing monoisocyanate, the molar ratio of phosgene to amine is often low, which easily leads to the generation of urea or hydrochloride, thereby affecting the overall yield and device operating efficiency

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Preparation method and system of mono-isocyanate
  • Preparation method and system of mono-isocyanate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0069] Embodiment 1 methyl isocyanate

[0070]In this example, according to the process described above, methyl isocyanate is prepared by gas-phase phosgenation, and the phosgene gasified and heated to 350°C is heated to 350°C with a flow rate of 2000kg / h at a flow rate of 250kg / h. The methylamine gas is sent to the gas phase phosgenation reactor at the same time for phosgenation reaction, the reaction pressure is 10KPa (gauge pressure), the reaction temperature is 350°C, the mixed gas obtained from the gas phase phosgenation reaction is absorbed by the inert solvent chloroform After obtaining the phosgenation reaction solution and the gas phase phosgenation reaction tail gas with a concentration of 20%, the temperature of the reaction solution is controlled at 32°C; The phosgene is removed by gas stripping to obtain the reaction solution with phosgene removed and the tail gas stripped with hydrogen chloride; the reaction solution with phosgene removed is sent to a cracker for...

Embodiment 2

[0073] Embodiment 2 ethyl isocyanate

[0074] In this example, according to the process described in Example 1, ethyl isocyanate was prepared by gas-phase phosgenation, and the phosgene gasified and heated to 320 ° C was used at a flow rate of 900 kg / h, and the flow rate was 150 kg / h and heated to Ethylamine gas at 320°C is simultaneously fed into the gas phase phosgenation reactor for phosgenation reaction, the reaction pressure is 5KPa (gauge pressure), the reaction temperature is 340°C, the mixed gas obtained from the gas phase phosgenation reaction is absorbed by the inert solvent toluene After obtaining the phosgenation reaction liquid and the gas phase phosgenation tail gas with a concentration of 20%, the temperature of the reaction liquid is controlled at 50°C; The phosgene is removed by gas stripping to obtain the reaction liquid and hydrogen chloride stripping tail gas; the reaction liquid is sent to the cracker for cracking, the cracking temperature is 135 ° C, and ...

Embodiment 3

[0077] Embodiment 3 isopropyl isocyanate

[0078] In this example, according to the process described in Example 1, isopropyl isocyanate is prepared by gas phase phosgenation, and the phosgene gasified and heated to 330 ° C is heated at a flow rate of 900 kg / h and a flow rate of 200 kg / h The isopropylamine gas up to 330°C is simultaneously sent into the gas phase phosgenation reactor for phosgenation reaction, the reaction pressure is 0KPa (gauge pressure), the reaction temperature is 350°C, the mixed gas obtained from the gas phase phosgenation reaction is inert solvent chlorine Obtain concentration after benzene absorption and be 20% phosgenation reaction liquid and gas phase phosgenation reaction tail gas, during reaction liquid temperature control at 60 ℃; ) to carry out air stripping to catch phosgene, and obtain the reaction liquid and the hydrogen chloride stripping tail gas that have completely removed phosgene; send the reaction liquid that has completely removed phos...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The invention relates to a preparation method and system of mono-isocyanate. According to the method, an excessive amount of phosgene is subjected to phosgenation reaction with corresponding amine, and after obtained reaction liquid is subjected to gas stripping through hydrogen chloride and phosgene is removed, the fact that the phosgene is completely separated with isocyanate is realized, and the purpose that the excessive amount of phosgene can be recycled is achieved. Pyrolysis gas obtained by performing pyrolysis on reaction liquid with phosgene being stripped is captured through an inertsolvent, solution of corresponding isocyanate is obtained, and qualified isocyanate can be obtained through subsequent separation. A process for preparing mono-isocyanate through the method has the characteristics of high yield and low solid waste amount.

Description

technical field [0001] The invention relates to a method and system for preparing monoisocyanate. The process of preparing monoisocyanate by using the method and system has the characteristics of high yield and no solid waste. Background technique [0002] Monoisocyanates are widely used in pesticides, pharmaceutical intermediates and organic synthesis. [0003] Methyl isocyanate and butyl isocyanate are a kind of important pesticide intermediates, wherein methyl isocyanate is mainly used in the synthesis of carbamate pesticides, such as: Kebaiqi, methadone, medox, isoprocarb (leafhopper San), Zhongdingwei (Sisha), Jiatuqi, Shashaqi, Haoanqi, Thiodimethodil, Prothiocarbafuran, and Dingsialon, etc.; Butyl isocyanate is used in the phosgenation method to prepare benzoyl It can be used as a catalyst for urea herbicides, and it can also be used for the synthesis of pesticide fungicide benomyl. [0004] In addition, ethyl isocyanate is an important pharmaceutical intermediate, ...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Applications(China)
IPC IPC(8): C07C263/10C07C263/20C07C265/04
CPCC07C263/10C07C263/20C07C265/04
Inventor 俞勇李同和李建峰尚永华刘德刚黎源李文滨黄真真乔小飞赵一鸣
Owner WANHUA CHEM GRP CO LTD
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products