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Process for rapid polymerization preparation of polymethyl methacrylate used for polymer fiber

A technology of polymethyl methacrylate and methyl methacrylate, which is applied in the field of high light-transmitting polymer materials, can solve the problems of PMMA degradation, increased POF non-inherent loss, deterioration of overall mechanical properties, etc., and achieves accelerated polymerization speed. , The effect of preventing temperature rise and shortening polymerization time

Inactive Publication Date: 2006-01-11
XI AN JIAOTONG UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The polymerization time is too long, and the early PMMA inevitably has to withstand high temperature for a long time, which can easily cause the degradation of PMMA, and the degraded PMMA will undoubtedly increase the extrinsic loss of POF produced in the future
Furthermore, the degradation of some PMMA macromolecules will increase the proportion of smaller molecular weight polymers in the product, that is, the molecular weight distribution of the entire product will broaden, which will greatly affect the mechanical properties of POF and make its overall mechanical properties worse.

Method used

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  • Process for rapid polymerization preparation of polymethyl methacrylate used for polymer fiber
  • Process for rapid polymerization preparation of polymethyl methacrylate used for polymer fiber

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preparation example Construction

[0019] According to the technical scheme of the present invention, the rapid polymerization preparation method of PMMA for polymer optical fiber comprises the following steps:

[0020] Raw materials:

[0021] Monomer: high-purity MMA; initiator: high-purity azobisisobutyronitrile (AIBN) or dibenzoyl peroxide (BPO); chain transfer agent: high-purity dodecyl mercaptan or n-butyl mercaptan; parts by mass Number MMA=100, AIBN or BPO 0.1%-0.7%; high-purity dodecanethiol or n-butanethiol 0.1%-0.9%, each raw material is prepared in proportion to the reaction material mixture before polymerization.

[0022] Aggregation:

[0023] The polymerization device consists of a reactor, a cold trap, and a vacuum pump (shown in the attached figure 1 ), operations such as heating, cooling, decompression, and temperature measurement can be easily carried out, and samples can be taken to measure the conversion rate of MMA monomer.

[0024] The whole aggregation process can be divided into 4 sta...

Embodiment 1

[0032] The monomer high-purity methyl methacrylate mass fraction is 100 parts, when the initiator selects high-purity azobisisobutyronitrile (AIBN) for use, and when the consumption is 0.1%, the chain transfer agent selects high-purity dodecanethiol or n-Butanethiol, when the dosage is 0.9%, the initial reaction temperature T 1 Be 80 ℃, measure the conversion rate of reaction once every 10min, when conversion rate reaches 20% (reaction carries out about 50min), stop heating, start decompression evaporation about 10min, the MMA that evaporates accounts for about 20wt% of MMA total amount, At this time, the internal temperature of the material drops to T 2 It is about 45°C (related to the ambient temperature), and then heated to the later reaction temperature T 3 65°C, keep it warm for 1h until the conversion rate is about 80%, continue to raise the temperature to 120°C, keep it warm for 0.5h, and then solidify after completion to end the reaction. Then the whole polymerizatio...

Embodiment 2

[0034]The mass fraction of high-purity methyl methacrylate monomer is 100 parts. When the initiator is selected from high-purity azobisisobutyronitrile (AIBN), and the consumption is 0.3%, the chain transfer agent is selected from high-purity dodecanethiol or n- Butanethiol, when the dosage is 0.7%, the initial reaction temperature T 1 Be 80 ℃, measure the conversion rate of reaction every 10min, when conversion rate reaches 20% (reaction carries out about 30min), stop heating, start decompression evaporation about 10min, the MMA that evaporates accounts for about 20wt% of MMA total amount, At this time, the internal temperature of the material drops to T 2 It is about 45°C (related to the ambient temperature), and then heated to the later reaction temperature T 3 50°C, keep it warm for 2 hours until the conversion rate is about 80%, continue to raise the temperature to 120°C, keep it warm for 0.5h, and then solidify after completion to end the reaction. Then the whole polym...

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Abstract

The invention provides a process for rapid polymerization preparation of polymethyl methacrylate used for polymer fiber by employing a polymerization plant comprising pipes connected reactor, cold trap, and vacuum pump, wherein the polymerization plant carries the operations of heating-up, cooling down, pressure relieve, temperature measurement and sampling monomer conversion rate, wherein the reaction of monomer high purity methyl methacrylate (MMA) can carry away a vast amount of polymerization heat fro inside the reaction mass, thus preventing the phenomenon of elevation of temperature inside the materials caused by polymerization heat accumulation.

Description

technical field [0001] The invention belongs to the technical field of high light-transmitting polymer materials used for broadband access and information communication in high-speed optical communication networks, and particularly relates to a polymethyl methacrylate (MMA) rapid bulk polymerization to prepare polymer optical fibers. Methyl Acrylate (PMMA) method. Background technique [0002] Modern communication network systems are rapidly developing towards large capacity and high speed. The development of multimedia communications such as digital video signals requires large signal capacity and wide bandwidth for network transmission, and the requirements for access network bandwidth are getting higher and higher. Therefore, it is urgent to widen the communication network, especially the local area network, to make it suitable for high-speed communication. At present, the development of optical fiber communication is extremely rapid, and its application has been widely ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F120/14
Inventor 钟力生徐传骧马素德
Owner XI AN JIAOTONG UNIV