Method for continuously producing polycarbonate-polyether polyol in channelization mode through liquid phase method

A technology of polyether polyol and polycarbonate, which is applied in the field of continuous production of polycarbonate-polyether polyol by liquid phase method, can solve the problem of large variation of amplification effect, high proportion of cyclic carbonate, time-consuming Loss and other issues, to achieve the effect of improving mass transfer and heat transfer capacity and effect, increasing the content of carbonate units, and improving reaction equipment

Active Publication Date: 2020-06-30
HANGZHOU POLY MATERIAL SCI & TECH CO LTD
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The first is about catalyzer, when adopting zinc-cobalt DMC catalyzer to synthesize polycarbonate-polyether polyol, the problem of existence is, in industry, add catalyzer and the epoxy monomer mass ratio of adding will at least ≤ 1/1000 (namely When the catalyst dosage is less than or equal to 1000ppm, that is, 0.1wt%, the overall production cost and catalyst residual cost are relatively low and have economic value
Or there are very few that still maintain a weak activity, but the reaction time is greatly prolonged (more than 12 hours) to obtain a polymer. This is due to the fact that the reaction time is actually caused by a higher proportion of the initiator. The time of the activation process of the substance (extended by several hours)
It takes longer reaction time and more energy consumption, which increases the production cost
[0006] The second is about the initiator. In addition to the catalyst, when using zinc-cobalt DMC catalyst to synthesize polycarbonate-polyether polyol, under the condition of a higher proportion of initiator addition, the synthesized polycarbonate-polyether polyol structure The structural proportion of polycarbonate will be reduced (<50%), that is, the fixation rate of carbon dioxide will be reduced
Because the addition of a higher proportion of initiator will cause a large number of catalyst active sites to be quenched or occupied, the macroscopic manifestation is that the catalyst activity is reduced or even deactivated
The reduction of the carbon dioxide fixation rate indicates that the proportion of the low-cost carbon dioxide raw material in the polymer is reduced, which means that the proportion of the higher-cost epoxide is increased, which leads to an increase in the production cost of the polymer on the one hand, and on the other hand, is beneficial to energy saving and emission reduction. (Consumption of CO2) is also less effective
If the temperature is too high, the content of carbonate chains will be low, the molecular wei

Method used

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  • Method for continuously producing polycarbonate-polyether polyol in channelization mode through liquid phase method
  • Method for continuously producing polycarbonate-polyether polyol in channelization mode through liquid phase method
  • Method for continuously producing polycarbonate-polyether polyol in channelization mode through liquid phase method

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Embodiment 1

[0045] A method for the continuous production of polycarbonate-polyether polyols in pipelines by liquid phase method,

[0046] The method comprises the steps of:

[0047] (1) The raw material is pumped in from the inlet of the pipeline reactor, and the pipeline reactor includes a heating section group and a cooling section group, and the heating section group is placed at the inlet end of the pipeline reactor, and the cooling section group is placed at the inlet end of the pipeline reactor. The segment group is placed at the outlet end of the pipelined reactor, and the raw materials include initiator, epoxy compound, catalyst and carbon dioxide, so that in the presence of the catalyst, the initiator, epoxy compound and carbon dioxide are formed in the pipelined reactor. Contact in the reactor to form a copolymerization reaction system, thereby carrying out the polymerization reaction to obtain a polymerization reaction product stream comprising polycarbonate-polyether polyol a...

Embodiment 2

[0080] Embodiment 2 With reference to Example 1, the difference is that the raw materials are mixed into a reaction liquid in the pipeline reactor, and carbon dioxide is added through the heating section group of the pipeline reactor, so that the pressure of the pipeline reactor is 1-20MPa , the purpose is to make the pipeline reactor have enough carbon dioxide and mix it with other polymerization raw materials evenly, and also by adding carbon dioxide, on the one hand, the temperature of the polymerization reaction can be precisely controlled, and on the other hand, the pipeline reactor can avoid A dead zone occurs.

Embodiment 3

[0090] Embodiment 3 With reference to Example 1, the difference is that the raw materials are mixed into a reaction solution in the pipeline reactor, and an epoxy compound is added to the pipeline reactor from the heating section group of the pipeline reactor, so that the step In (1) and (2), in the pipelined reactor, the concentration of the epoxy compound is at 20-50wt%, and the purpose is to make the pipelined reactor have enough epoxy compounds and react with other polymerization reactions The raw materials are mixed evenly, and the temperature of the polymerization reaction can be precisely controlled by adding epoxy compounds, secondly, the pipeline reactor can avoid dead zones, and finally, the viscosity of the polycarbonate can be controlled by adjusting the viscosity of the polymerization reaction product stream to an appropriate range. - Molecular weight of polyether polyols and their distribution.

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Abstract

The invention discloses a method for continuously producing polycarbonate-polyether polyol in a channelization mode by a liquid phase method, wherein the method comprises the following steps: (1) pumping a raw material from an inlet of a channelization reactor, making an initiator, an epoxy compound and carbon dioxide contact in the channelization reactor in the presence of a catalyst, and carrying out polymerization reaction; and (2) enabling part or all of the polymerization reaction product material flow in the step (1) to flow through a cooling section group, separating out part of polycarbonate-polyether polyol, and continuing to carry out polymerization reaction on the rest of the polymerization reaction product material flow in the channelization reactor, or circulating back to thestep (1), wherein the catalyst is a zinc-cobalt double-metal cyanide complex catalyst obtained by reacting water-soluble metal salts of zinc and cobalt in a water-soluble solvent, when the catalyst issynthesized, the catalyst is modified by mixed acid, and the organic acid is selected from any one or more of succinic acid, glutaric acid, phthalic acid, iminodiacetic acid, pyromellitic acid and butane tetracarboxylic acid.

Description

technical field [0001] The invention relates to the field of synthesis of polycarbonate-polyether polyols, in particular to a method for continuous production of polycarbonate-polyether polyols through liquid-phase pipelines. Background technique [0002] Polycarbonate-polyether polyol is a kind of polyol with carbonate group in the molecule and hydroxyl group at the end of the molecular chain. carbon dioxide (CO 2 ) and epoxy compound regulation copolymerization method is CO 2 Adding an initiator during the copolymerization reaction with epoxide, and controlling the molecular weight of the product by controlling the chain transfer of the reaction. Carbon dioxide, one of the main greenhouse gases, has attracted attention as a carbon-resource that can replace traditional fossil fuels for the synthesis of many important chemicals due to its cheap, easy-to-obtain, non-toxic and non-flammable advantages. Studies have shown that 20wt% CO 2 CO 2 Compared with the preparation ...

Claims

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Application Information

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IPC IPC(8): C08G64/32C08G64/34C08G65/26C08G65/28
CPCC08G64/205C08G64/323C08G64/326C08G64/34C08G65/2609C08G65/2612C08G65/2615C08G65/2663C08G65/2696C08G2650/24Y02P20/584
Inventor 毛红兵王慧君王自修
Owner HANGZHOU POLY MATERIAL SCI & TECH CO LTD
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