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Process for producing radical polymer and microapparatus for chemical reaction

A manufacturing method, free radical technology, applied in the field of free radical polymer manufacturing, can solve problems such as uneven polymerization temperature, difficulty in easy implementation of chemical reactions, and low production efficiency

Inactive Publication Date: 2006-09-06
IDEMITSU KOSAN CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, in such radical polymerization, since a large amount of heat of reaction is generated during polymerization, regardless of whether the reaction method is a batch type or a continuous type, in order to remove the heat of reaction, it usually takes time under mild reaction conditions. Carried out, there is a problem that the production efficiency is low
In addition, in conventional polymerization methods, due to the heat of reaction, the polymerization temperature in the reaction place tends to become non-uniform, and in the case of a continuous type, the reaction liquid is difficult to become laminar flow, so the residence time varies locally, and as a result , the obtained polymer tends to be a mixture of polymers with various molecular weights
[0008] In the fabrication of microchemical reaction devices (microreactors), high-level processing technologies such as photolithography, etching, and precision machining are generally required to fabricate microscopic flow channels. Therefore, it is important to easily implement chemical reactions using microreactors. difficult

Method used

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  • Process for producing radical polymer and microapparatus for chemical reaction
  • Process for producing radical polymer and microapparatus for chemical reaction

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0051] 1.55 g of 2,2'-azobisisobutyronitrile was dissolved in 100 ml of toluene to prepare a radical polymerization initiator solution. As the toluene, toluene obtained by bubbling dehydrated grade toluene with argon for 30 minutes or more was used. Methyl methacrylate use: Methyl methacrylate that was washed with 1 mol / L sodium hydroxide aqueous solution 3 times, washed with distilled water 3 times, dried with sodium sulfate, and then subjected to argon bubbling for 30 minutes or more. The radical polymerization initiator solution and methyl methacrylate were filled into respective syringe pumps (syfing pumps) under an argon atmosphere, and after they were combined using a tee joint, they were introduced into a reaction tube made of stainless steel with an inner diameter of 0.5 mm middle. The reaction tube is 10 m long, and the first 9 m is immersed in a constant temperature bath with a temperature of 100°C, and the remaining 1 m is immersed in an ice bath. At the outlet of ...

Embodiment 3

[0058] In Example 1, the same procedure as in Example 13 was carried out except that 5.3 ml of the polymerization solution was collected over 6 minutes. 0.6897 g of a solid comprising methyl methacrylate polymer was obtained. Table 1 shows the results. There was one polymer peak.

Embodiment 4

[0060] In Example 1, the same procedure as in Example 1 was carried out except that 2.2 ml of the polymerization solution was collected over 6 minutes. 0.5213 g of a solid containing methyl methacrylate polymer was obtained. Table 1 shows the results. There was one polymer peak.

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Abstract

An object of the present invention is to provide a method for effectively producing, within a short period of time, a radical polymer having controlled molecular weight distribution or a narrow molecular weight distribution profile, the method including polymerizing a radical-polymerizable monomer. Another object of the invention is to provide a microreactor which can be readily fabricated. The invention attains the objects through provision of a method for producing a radical polymer, which method includes feeding a radical polymerization initiator and a radical-polymerizable monomer into a reaction tube having an inner diameter of 2 mm or less and performing polymerization in the reaction tube in a homogeneous liquid state under flow conditions, and a microreactor having a jacket for allowing a temperature-regulating fluid to pass therethrough and a plurality of round tubes which are arranged in parallel in the jacket, each having an inner diameter of 2 mm or less, wherein reaction temperature in the round tubes can be regulated through flowing of the temperature-regulating fluid in the jacket.

Description

technical field [0001] The invention relates to a manufacturing method and a micro chemical reaction device of a free radical polymer. In more detail, the present invention relates to the polymerization of radically polymerizable monomers in a flow-through manner using a fine reaction tube with an inner diameter of 2mm or less, and by precisely controlling the polymerization temperature at a prescribed temperature, it can be efficiently carried out in a short time. A method of producing a radical polymer with a controlled molecular weight distribution or a narrow molecular weight distribution, and a microchemical reaction device that can be produced without requiring high-level processing technology using easily available components. Background technique [0002] Recently, interest in microreactors has been on the rise. The microreactor generally refers to a device in which a reaction is carried out in a fine microchannel with an internal structure of about 1 μm to 1 mm, an...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F2/01
Inventor 岩崎猛吉田润一
Owner IDEMITSU KOSAN CO LTD
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