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Preparation method of isocyanates

A technology of isocyanate and diisocyanate, which is applied in the preparation of isocyanate derivatives, the preparation of organic compounds, chemical instruments and methods, etc., can solve the problems of reduced production efficiency, low concentration of salt formation, and reduced economic efficiency, so as to avoid yellowing change, the effect of low reaction temperature

Active Publication Date: 2017-11-10
WANHUA CHEM GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The preparation of isocyanates by liquid phase phosgenation can be divided into cold and hot phosgenation and salt-forming phosgenation. One disadvantage is that it is impossible to reduce the generation of urea by-products; the salt formation method first reacts the corresponding amine with acid gas such as hydrogen chloride, carbon dioxide, etc. to obtain amine hydrochloride or carbonate, and then reacts the amine salt with phosgene, Can effectively inhibit urea by-products in the photochemical process
[0004] Chinese published patent CN200680022170 reports that the salt formation process is carried out at 0.01Mpa above atmospheric pressure and at a temperature of 120°C. Although high-temperature pressurization can reduce the viscosity of hydrochloride and improve the conversion rate and space-time efficiency of salt formation, there are two defects. On the one hand, it is only suitable for diamines with high stability at high temperatures, and will seriously affect the color number of the salt-forming and photochemical solutions; on the other hand, the rate of salt-forming at high temperatures is extremely fast, so the heat transfer and Diamine wrapping problem
[0005] The British published patent GB1086782A mentions that the condition of salt-forming phosgenation is that diamine and hydrogen chloride form a salt at 0-60°C, the reaction concentration of hydrochloride is below 5.5wt%, and the conversion rate is very high, although low temperature and low concentration can reduce by-products generation, but the space-time yield is not high, and a large amount of solvent needs to be removed by distillation, which reduces its economy
[0006] Chinese published patent CN1045578A discloses the use of aliphatic esters as solvents, and the salt-forming temperature is controlled at 0-30°C. This can significantly reduce the generation of monochloroisocyanates in the photochemical process, but the aliphatic esters selected in this method The price of the solvent is higher than that of traditional benzene-based solvents, and the stability of the photochemical process at high temperature is poor
[0007] At present, the main factor limiting the industrialization of salt-forming liquid-phase phosgenation is the low salt-forming concentration of the raw material diamine, which leads to the inability to improve the space-time benefit and economic benefit, especially for short-chain aliphatic or alicyclic diamines in the formation process. The concentration in the salting process should not be too high. Due to the small molecular weight, the viscosity of the obtained hydrochloride slurry increases rapidly, which brings about unfavorable conditions such as stirring, dispersing, and heat transfer difficulties.
For example, in the salt-forming process, if the concentration of diamine in the inert solvent is set to 6-10%, then the organic solvent in which the raw material amine is dissolved is mixed with hydrogen chloride gas, as the reaction proceeds, the hydrochloride The viscosity of the slurry rises rapidly. In the later stage of the reaction, the hydrochloride will form agglomerates on the bottom and wall of the kettle, and it is difficult to disperse it by stirring, resulting in a decrease in production efficiency.
[0008] Therefore, it is necessary to develop a new method for the preparation of isocyanate by salt-forming liquid phase phosgenation to solve the disadvantages of hydrochloride agglomeration, difficulty in dispersing, and low production efficiency.

Method used

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  • Preparation method of isocyanates

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0070] Add 50 g (0.1 mol, about 0.5 mol of hydroxyl groups) of hydroxyl-terminated hyperbranched polyester HyPer H101 into 75 g of solvent butyl acetate to make the solid content 40 wt%. Add 87gTDI (0.5mol) and catalyzer dibutyltin dilaurate 0.06g in the four-neck flask equipped with stirrer, thermometer and condensing tube, under constant stirring at constant speed, slowly add the prepared HyPer H101 butyl acetate solution dropwise, drop At the end of the addition, the temperature was slowly raised to 60°C. When the system-NCO content was 50% of the initial NCO content, 300g of butyl acetate was added to reduce the viscosity of the system, and the above mixed solution was added to 54g of 4-(aminomethyl)pyridine (0.5mol ), the end-capping reaction was carried out at 80°C, and the NCO content of the system was 1wt%. The reaction was completed, and the polyester hyperdispersant 1 with a solid content of 34wt% was obtained, and its molecular weight was 1911.

Embodiment 2

[0072]Add 60 g (0.1 mol, about 0.5 mol of hydroxyl group) of hydroxyl-terminated hyperbranched polyester HyPer H201 into 115 g of solvent butyl acetate to make the solid content 35 wt%. Add 87g TDI (0.5mol) and catalyst stannous octoate 0.08g in the four-neck flask equipped with stirrer, thermometer and condenser tube, under constant stirring at a constant speed, slowly add the HyPerH201 butyl acetate solution prepared dropwise at a constant temperature, and the dropwise addition ends slowly Heat up to 70°C, when the system-NCO content is 52% of the initial NCO content, add 300g butyl acetate to reduce the viscosity of the system, and add 80g 8-amino-2-methylquinoline (0.5mol) to the above mixed solution During the end-capping reaction at 70°C, the NCO content of the system was 0.3wt%, and the reaction was completed to obtain a polyester hyperdispersant 2 with a solid content of about 35wt%, and its molecular weight was 2261.

Embodiment 3

[0074] Add 83 g (0.09 mol, about 0.45 mol of hydroxyl group) of hydroxyl-terminated hyperbranched polyester HyPer H301 into 140 g of solvent butyl acetate to make the solid content 37%. Add 125gMDI (0.5mol) and 0.06g of catalyst stannous octoate into a four-necked flask equipped with a stirrer, a thermometer and a condenser tube, and slowly add the configured HyPerH301 butyl acetate solution dropwise at a constant temperature under constant stirring, and the dropwise addition ends slowly. Heat up to 80°C, when the system-NCO content is 51% of the initial NCO content, add 300g butyl acetate to reduce the viscosity of the system, and add the above mixed solution to 60g 4-amino-2-picoline (0.55mol) , Carry out capping reaction at 60°C, the NCO content of the system is 0.15wt%, the reaction is completed, and the polyester hyperdispersant 3 with a solid content of about 38% is obtained, and its molecular weight is 2710.

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Abstract

The invention discloses a preparation method of isocyanates. A high-concentration isocyanate actinic solution is prepared based on a salification phosgenation reaction, and a polyester hyperdispersant is added in a diamine salification procedure; and anchoring groups of the hyperdispersant are converted into tertiary amine salts which are adsorbed to the surface of diamine hydrochloride particles in the salification procedure, and steric hindrance is formed through the solvation chain, so that hydrochloride particles are separated, thereby avoiding the phenomena of aggregation, agglomeration and the like, obviously enhancing the salification concentration and effects, and further greatly enhancing the yield of the isocyanate product.

Description

technical field [0001] The invention relates to a method for preparing high-concentration isocyanate, in particular to adding a polyester hyperdispersant in the reaction process of diamine and hydrogen chloride, which can effectively increase the salt-forming concentration and efficiency of diamine, thereby preparing isocyanate. Background technique [0002] Aliphatic and cycloaliphatic diisocyanate (ADI) has become the research focus of major polyurethane companies and scientific research institutions around the world. Its products are widely used in coatings, car paints, Adhesives and medical materials and other fields. [0003] The preparation of isocyanates by liquid phase phosgenation can be divided into cold and hot phosgenation and salt-forming phosgenation. One disadvantage is that it is impossible to reduce the generation of urea by-products; the salt formation method first reacts the corresponding amine with acid gas such as hydrogen chloride, carbon dioxide, etc....

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C263/10C07C265/14B01F17/00B01F17/32C09K23/00C09K23/32
CPCC07C263/10C09K23/00
Inventor 陈浩尚永华李建峰李同和俞勇黎源华卫琦
Owner WANHUA CHEM GRP CO LTD
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