Preparation method of diphenylmethane series diamine and polyamine with low macromolecular impurity content

A technology of diphenylmethane and impurity content, applied in the preparation of amino compounds, chemical instruments and methods, preparation of organic compounds, etc., can solve equipment pipeline blockage, poor mechanical mixing of formaldehyde, continuous and stable operation of product DAM quality effects, etc. question

Active Publication Date: 2019-03-08
WANHUA CHEM GRP CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] In the process of continuous production of DAM in large-scale industrial equipment, macromolecular resin-like solid substances are easily produced during the reaction process of acid-catalyzed aniline and formaldehyde. On the other hand, it will be brought into the product DAM, affecting the quality of DAM
In fact, it has been recognized that the above-mentioned solid product is mainly due to poor mechanical mixing of formaldehyde in the reaction process, and there is a local excess of formaldehyde relative to aniline, thereby producing a macromolecular resinous substance, which is difficult to dissolve in solvents such as aniline and hydrochloric acid. Blockage of equipment pipelines due to the presence of solid forms
[0007] In this regard, many patents at home and abroad have mentioned related technologies to improve this problem from the perspective of mechanical stirring or the reduction of the total proportion of formaldehyde to aniline. For example, EP2486975 (A1) discloses the use of a special mixer reactor in the preparation of MDA. , CN101279923A patent improved the mixing reaction equipment, CN106458844A patent carried out formaldehyde feeding operation and control improvement during start-up and shutdown, etc., the above-mentioned method controlled the generation of macromolecular resin impurities to a certain extent, and solved the problem of short-term and medium-term solid impurities. The problem of equipment blockage, but this kind of excessive polymerization product that is still continuously generated accumulates in the system in the form of solid suspension during the high-load and long-term operation of the production device, which will still affect the long-term continuous and smooth operation of the device and the quality of the product DAM make an impact

Method used

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  • Preparation method of diphenylmethane series diamine and polyamine with low macromolecular impurity content
  • Preparation method of diphenylmethane series diamine and polyamine with low macromolecular impurity content
  • Preparation method of diphenylmethane series diamine and polyamine with low macromolecular impurity content

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] a) Add 14.5 g of acidic formaldehyde depolymerization catalyst hydrochloric acid (mass concentration 34%) into 109.5 g of clear and transparent formaldehyde aqueous solution (store at 50°C for 72 hours, formaldehyde mass concentration is 37%, pH is 3) and stir, condense and reflux 1. In the reactor replaced by nitrogen, heat at 50° C., 80° C., 90° C., 100° C. and 300 rpm for 2.5 hours in sequence.

[0034] b) Weigh 279.0g of aniline (mass concentration ≥ 99%) and 88.6g of hydrochloric acid (mass concentration 34%), and add them to another set of reactor with stirring and condensing reflux after nitrogen replacement, at 50°C and 300rpm React for 5 minutes, then add the depolymerized formaldehyde solution in step a) for 20 minutes, the stirring speed is 300 rpm, and the reaction temperature is controlled at 60°C. After the formaldehyde solution is added for 20 minutes, raise the system temperature to 80°C and continue At 40 minutes, the clear and transparent reaction solu...

Embodiment 2

[0040] a) Add 2.9 g of acidic formaldehyde depolymerization catalyst hydrochloric acid (mass concentration 34%) into 101.3 g of clear and transparent formaldehyde aqueous solution (store at 50°C for 60 hours, formaldehyde mass concentration is 40%, pH is 3.5) and stir and condense Reflux in the reactor replaced by nitrogen, heat and reflux at 55°C and 300rpm for 1h, then add 4.2g isopropanol (mass concentration ≥ 99%) at 0.5ml / min, keep stirring and heat up to 1°C / min Heating to reflux at 85°C for 1.5h.

[0041] b) Weigh 279.0g of aniline (mass concentration ≥ 99%) and 100.2g of hydrochloric acid (mass concentration 34%), and add them to another set of reactor with stirring and condensing reflux after nitrogen replacement, at 50°C and 300rpm React at low temperature for 5 minutes, then add the depolymerized formaldehyde solution for 15 minutes, stir at 300 rpm, control the reaction temperature at 60°C, raise the system temperature to 80°C 20 minutes after the formaldehyde solu...

Embodiment 3

[0045] a) Add 17.4 g of acidic formaldehyde depolymerization catalyst sulfuric acid (mass concentration 38%) into 119.2 g of clear and transparent formaldehyde solution (store at 55°C for 52 hours, formaldehyde mass concentration is 34%, pH is 3) and stir and condense Reflux in the reactor replaced by nitrogen, heat and reflux at 50°C and 300rpm for 1h, then add 2.2g of anhydrous methanol (mass concentration ≥ 99%) at 0.5ml / min, keep stirring and heat up to 1°C / min Heating to reflux at 85°C for 1.5h.

[0046] b) Weigh 279.0g of aniline (mass concentration ≥ 99%) and 106.4g of sulfuric acid (mass concentration 38%), and add them to another set of reactor with stirring and condensing reflux after nitrogen replacement, at 50°C and 300rpm Then add the depolymerized formaldehyde solution for 20 minutes, the stirring speed is 300 rpm, and the reaction temperature is controlled at 60°C. After the formaldehyde solution is added for 20 minutes, raise the system temperature to 80°C and ...

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Abstract

The invention relates to a preparation method of diphenylmethane series diamine and polyamine with low macromolecular impurity content. According to the method, the content ratio of monomer formaldehyde in formaldehyde is controlled in 40-60wt% before aniline and the formaldehyde are reacted under the condition of an acid catalyst. Before the formaldehyde and the aniline or aniline hydrochloride are mixed, a state of formaldehyde water solution is changed, low-polymerized formaldehyde in water solution is depolymerized, the content of the monomer formaldehyde in the water solution is controlled to reach a more favorable range, macromolecular resin solid impurities generated in condensation reaction are decreased, blocking caused by aggregation of macromolecular polymers in a device and a pipeline is remarkable relieved in medium and long term continuous production processes of DAM is obviously relieved, and the content of macromolecular impurities in the DAM is decreased.

Description

technical field [0001] The invention belongs to the technical field of DAM preparation, and relates to a production method of higher-quality diphenylmethane series diamines and polyamines, in particular to a preparation of diphenylmethane series diamines and polyamines (DAM) with low macromolecule impurity content method. Background technique [0002] The preparation process of DAM is generally known, and it is conventionally carried out by reacting aniline and formaldehyde in the presence of an acidic catalyst in a continuous, semi-continuous or discontinuous process. This method is described in many patents and publications (see, for example, HJ. Twitchett, Chem. Soc. Rev. 3 (2), 209 pages (1974), M, V, Moore's Kirk-othmer Encycle. Chem. Technol. Third Edition, New York, 2, pp. 338-348 (1978)). In industrial production, aniline is usually reacted with hydrochloric acid first, and then formaldehyde is added to the reaction system to obtain DAM hydrochloride under acid-cat...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C209/78C07C211/50C07C209/82
CPCC07C209/78C07C209/82C07C211/50
Inventor 李永锋吴雪峰邢津铭张宏科崔成成陈良进徐丹
Owner WANHUA CHEM GRP CO LTD
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