Method for continuously producing high-molecular-weight polyether by adopting micro-channel reactor

A micro-channel reactor, micro-reactor technology, applied in chemical instruments and methods, chemical/physical/physical-chemical reactors, chemical/physical/physical-chemical processes, etc., can solve the complex process, low reaction speed, synthesis cycle long-term issues

Inactive Publication Date: 2020-11-13
XIHUA UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

CN102532513A has reported that its catalytic characteristic of KOH system catalyst is gentle reaction, reaction speed is low, and synthesis cycle is longer, often need to improve reaction speed by ways such as increasing catalyst and propylene oxide concentration, raising reaction temperature, but these measures have increased olefin mostly. The probability of propanol side reactions, forming a vicious circle
However, the whole process is complicated, and the catalyst needs to be preactivated separately in the batch reactor, that is, the double metal cyanide complex catalyst, the initiator and the epoxy compou

Method used

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  • Method for continuously producing high-molecular-weight polyether by adopting micro-channel reactor

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0089] Embodiment 1: (synthesis of low molecular weight polyether Mn=2400)

[0090] (1) The device used: a continuous microreactor system, refer to figure 1System device diagram connection, you can choose 2 micro-reaction units. Among them, the microreactor can use one or more microreactors from Guizhou Microchem Technology Co., Ltd., Dalian Microchem Chemical Co., Ltd., and Chemtrix BV in the Netherlands. The micromixer can use Guizhou Microchem Technology Co., Ltd. One or more of the Micromixers of Ltd. Adjust the length of the delay tube to determine the reaction residence time, the heat exchange medium is high-temperature heat transfer oil, and the neutralization tank is a 5L conventional alkoxylation small-scale reactor.

[0091] (2) First prepare low-molecular-weight polyether F in the microreactor system: add 100g of propylene glycol as an initiator to the pre-treatment tank in advance, add catalyst 0.1% sodium metal, and degas between -0.05MPa±0.05MPa, After the nit...

Embodiment 2

[0095] Embodiment 2: (synthesis of high molecular weight polyether polyol Mn=5000)

[0096] (1) The device used: a continuous microreactor system, refer to figure 1 The system device diagram is connected, and there are 3 micro-reaction units. Among them, one or more microreactors from Guizhou Microchem Technology Co., Ltd., Dalian Microchem Chemical Co., Ltd., and ChemtrixBV from the Netherlands can be used for the microreactor. Guizhou Microchem Technology Co., Ltd., Dalian Microchem Chemical Co., Ltd. One or more of the company's Micromixers. Adjust the length of the delay tube to determine the reaction residence time. The heat exchange medium is high-temperature heat transfer oil. Both the collection tank and the neutralization tank are 5L conventional alkoxylation small-scale reactors.

[0097] (2) First prepare low-molecular-weight poly-F in the microreactor system: add 100g of propylene glycol as an initiator to the pre-treatment tank in advance, add a catalyst of 0.2%...

Embodiment 3

[0101] Embodiment 3: (synthesis of high molecular weight polyether polyol Mn=8000)

[0102] (1) The device used: a continuous microreactor system, refer to figure 1 The connection of the system device diagram, there are 4 micro-reaction units. Among them, one or more microreactors from Guizhou Microchem Technology Co., Ltd., Dalian Microchem Chemical Co., Ltd., and ChemtrixBV from the Netherlands can be used for the microreactor. Guizhou Microchem Technology Co., Ltd., Dalian Microchem Chemical Co., Ltd. One or more of the company's Micromixers. Adjust the length of the delay tube to determine the reaction residence time. The heat exchange medium is high-temperature heat transfer oil. The collection tank, neutralization tank and post-treatment tank are all 5L conventional alkoxylation small-scale reactors.

[0103] (2) First prepare low-molecular-weight poly-F in the microreactor system: add 100g glycerol as an initiator to the pre-treatment tank in advance, add catalyst 0.3...

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Abstract

The invention relates to a method for producing high-molecular-weight polyether by adopting a micro-channel reactor. The method adopts a micro-reactor, a micro-mixer, a pretreatment kettle, a preheating pipe, a delay pipe, a metering pump A, a metering pump B, an epoxy compound storage tank B, a collection kettle, a neutralization kettle, a desalting device, a post-treatment kettle, a back pressure valve and a pressure gauge. The micro-reactor is provided with a plurality of micro-channels, two micro-reactor feed ports and a micro-reactor discharge port; the micro-reactor, the micro-mixer andthe delay pipe form a micro-reaction unit; the desalting device comprises a post-treatment kettle and a filtering machine; and the pressure gauge is arranged between the micro-mixer and the back pressure valve. The method is advanced and scientific, the micro-reactor system adopted in the method is rapid and uniform in mixing, the over-temperature phenomenon is avoided, side reactions are reduced,low-unsaturation-degree and high-molecular-weight polyether can be continuously produced, direct large-scale production can be achieved, and the method has high safety performance and is suitable forindustrial production.

Description

technical field [0001] The invention relates to a method for producing high-molecular-weight polyether by adopting a microchannel reactor, specifically, a method for continuously preparing high-molecular-weight polyether with low unsaturation and narrow molecular weight distribution. Background technique [0002] Narrow molecular weight distribution and high molecular weight polyether have the characteristics of stable quality and performance, and have application prospects in the fields of soft foam polyurethane, high resilience polyurethane, polyurethane elastomer, special coatings, rubber, hydraulic oil, metal cutting fluid, and quenching agent for aircraft materials. Vast, its consumption accounts for about 80% of the total polyether polyol production. In addition, high molecular weight polyether is mainly used in the production of foam stabilizers, water reducers, defoamers, demulsifiers and lubricants. [0003] At present, most of the catalysts used in polymer polyeth...

Claims

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Application Information

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IPC IPC(8): C08G65/28B01J19/00
CPCC08G65/2609B01J19/0053B01J19/0093
Inventor 王会镇卜兴兵赵雨张竹王梦兰罗莎莎周霞李兴东
Owner XIHUA UNIV
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