SU624576A3 - Method of obtaining copolymers - Google Patents

Method of obtaining copolymers

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Publication number
SU624576A3
SU624576A3 SU752113541A SU2113541A SU624576A3 SU 624576 A3 SU624576 A3 SU 624576A3 SU 752113541 A SU752113541 A SU 752113541A SU 2113541 A SU2113541 A SU 2113541A SU 624576 A3 SU624576 A3 SU 624576A3
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USSR - Soviet Union
Prior art keywords
acrylonitrile
chain
styrene
weight
transmitter
Prior art date
Application number
SU752113541A
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Russian (ru)
Inventor
Ж.И.Бракк Вильям
Original Assignee
Лябофина С.А., (Фирма)
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Application filed by Лябофина С.А., (Фирма) filed Critical Лябофина С.А., (Фирма)
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Publication of SU624576A3 publication Critical patent/SU624576A3/en

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F279/00Macromolecular compounds obtained by polymerising monomers on to polymers of monomers having two or more carbon-to-carbon double bonds as defined in group C08F36/00
    • C08F279/02Macromolecular compounds obtained by polymerising monomers on to polymers of monomers having two or more carbon-to-carbon double bonds as defined in group C08F36/00 on to polymers of conjugated dienes
    • C08F279/04Vinyl aromatic monomers and nitriles as the only monomers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F212/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
    • C08F212/02Monomers containing only one unsaturated aliphatic radical
    • C08F212/04Monomers containing only one unsaturated aliphatic radical containing one ring
    • C08F212/06Hydrocarbons
    • C08F212/08Styrene
    • C08F212/10Styrene with nitriles
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/42Nitriles
    • C08F220/44Acrylonitrile

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Description

(54) СПОСОБ ПОЛУЧЕНИЯ СОПОЛИМЕРОВ(54) METHOD FOR OBTAINING COPOLYMERS

Изобретение относитс  к области получени  сополимеров на основе стирола и акрилонитрила, называемых смолы САН, По сравнению с гамополимерами стирола смолы САН обладают многими преимуществами . Так, дл  них свойственна меньша  термическа  деформаци , повышенна  стойкость к старению, лучшие механические свойства и блест щий внешний вид. Это улучшение некоторых качеств можно видеть уже тогда, когда содержание акрилонитрила в смолах САН составл ет 60%, но чаще готов т смолы САН, содержащие 25-90% акрилонитрила.. Сополимеры стирола с акрилонитрилом могут быть получены сополимериаацией радикального типа любым известным способом , т.е. суспензионным, эмульсионным или в массе. Дл  контрол  длины полимерной цепи, получаемой при радикальной полимеризаци без существенного вли ни  на скорость полимеризации в реакционную смесь ввод т регул торы или передатчики цепи. Вы бор регул тора цепи зависит от типа используемого мономера. В случае стирольных полимеров наиболее часто используемыми передатчиками цепи  вл ютс  меркаптаны,например трет.додецилмеркаптан . При полимеризации акрилонитрила можно использовать триэтиламин в качестве передатчика цепи. Так, известен способ получени  сополимера стирола с акрилонитрилом в присутствии передатчика цепи трет.додецилмеркаптана ij. Однако при получении сополимеров стирола с акрилонитрилом с указанными передатчиками цепи меркаптаны реагируют с акрилонитрилом, поэтому получают плохо воспроизводимые результаты, т.е регулирование длины цепи недостаточно эффективно. Цель изобретени  - аффективное регуирование молекул рного веса сополимера. Эта цель достигаетс  тем, что в качестве передатчика цепи используют О,015-5% от веса мономеров дитиобис (бенэогйазо а) ТБТ. Чтобы показать особую активность ТБТ в качестве регул тора молекул рного веса, были проведены сравнительные опыты, в которых испольашали раз личные смеси стирола и акрилонитрила и ввопили их в ампулы под давлением. Затем эти смеси подвергали термической полимеризации без азота, в течение 1 ч при перемешивании. В табл.1 приведены данные серии опытов, где используют смесь 20Q вес. стирола и 800 вес. % акрилонитрила и 105°С. попнмервзацию провод т при Количества передатчика цепи вычисле ны от веса мономеров в %%. Характеристическую в зкость определ ют дл  1 г смолы в 100 мл метилэтилкетона при 30°С. В табл. 2 приведены данные серии 1Л1ЫТОВ, где используют смесь 10 вес.% стирола и 90 вес. % акрилонитоила} полимеризацию провод т при 100 С. Коли чества передатчика цепи вычислены от деса мономеров |в %%. Характеристичес (кую в  зкость определ ют так же, как в 1-ой серии опытов.This invention relates to the field of producing copolymers based on styrene and acrylonitrile, called SAN resins. Compared with styrophol gamopolymers, SAN resins have many advantages. Thus, they are characterized by less thermal deformation, increased aging resistance, better mechanical properties and a brilliant appearance. This improvement in some qualities can be seen already when the content of acrylonitrile in SAN resins is 60%, but more often SAN resins are prepared containing 25-90% of acrylonitrile. Styrene copolymers with acrylonitrile can be obtained by copolymerization of the radical type by any known method, . suspension, emulsion or bulk. To control the length of the polymer chain obtained by radical polymerization without significantly affecting the rate of polymerization, chain regulators or transmitters are introduced into the reaction mixture. The choice of chain regulator depends on the type of monomer used. In the case of styrene polymers, the most commonly used chain transfer agents are mercaptans, for example, tert-dodecyl mercaptan. In the polymerization of acrylonitrile, triethylamine can be used as a chain transmitter. Thus, a method is known for producing a styrene copolymer with acrylonitrile in the presence of a tertiary dodecyl mercaptan ij chain transmitter. However, upon receipt of styrene copolymers with acrylonitrile with these chain transfer agents, the mercaptans react with acrylonitrile, therefore, poorly reproducible results are obtained, that is, chain length control is not effective enough. The purpose of the invention is the affective regulation of the molecular weight of the copolymer. This goal is achieved by using O, 015-5% of the weight of the monomers dithiobis (benogeyazo a) TBT as the transmitter of the chain. To show the special activity of TBT as a molecular weight regulator, comparative experiments were carried out in which different mixtures of styrene and acrylonitrile were used and injected into ampoules under pressure. Then these mixtures were subjected to thermal polymerization without nitrogen, for 1 h with stirring. Table 1 presents the data of a series of experiments where a mixture of 20Q weight is used. styrene and 800 weight. % Acrylonitrile and 105 ° C. Population conversion is carried out with the amount of transmitter chain calculated from the weight of monomers in %%. The intrinsic viscosity is determined for 1 g of resin in 100 ml of methyl ethyl ketone at 30 ° C. In tab. 2 shows the data series 1L1YTOV, where they use a mixture of 10 wt.% Styrene and 90 weight. % acrylonitol} Polymerization is carried out at 100 C. The number of transmitter chains is calculated from the desa of the monomers |%. Characteristic viscosity is determined in the same way as in the first series of experiments.

Таблица 6 В табл. 3 приведены данные серии опытов, где используют смесь,содержащую 7 г стирола, 63 г акрилонитрила и 30 г этилбензола. Полимеризацию провод т при 105°С. Количества передатчика цепи вычислены , счита  на вес мономера и растворител . Характеристическую в зкость определ ли, использу  1 г смолы в 100 мл диметилформамида при . В табл. 4 приведены данные серии опьй тов, где используют смесь 75 вес. % стирола и 25 вес. % акрилонитрила. Полимеризацию провод т при 100 С. Количества передатчика цепи вычисле .ны от веса мономеров. Приме р 1. Осуществл ют термическую полимеризацию в присутствии азота в течение 1 ч и с перемешиванием смеси 20 вес. % стирола и 80 вес. % акрилонитрила при температуре 105 С в присутствии 0,015 % дитиобис(бензотиазсла ).. Степень конверсии мономеров 8,3%, характеристическа  в зкость 1,15. П р и м е р 2. Опыт провод т по примеру 1, использу  5% дитиобис(бензотиазола ). Степень конверсии мономеров 7,5%, характеристическа  в зкость 0,3.Table 6 In table. 3 shows the data of a series of experiments where a mixture containing 7 g of styrene, 63 g of acrylonitrile and 30 g of ethylbenzene is used. The polymerization is carried out at 105 ° C. The amounts of chain transfer are calculated based on the weight of the monomer and solvent. The intrinsic viscosity was determined using 1 g of resin in 100 ml of dimethylformamide at. In tab. 4 shows the data of the series of opts, where a mixture of 75 wt. Is used. % styrene and 25 wt. % Acrylonitrile. The polymerization is carried out at 100 C. The amounts of the transmitter of the chain are calculated on the weight of the monomers. Example 1. Thermal polymerization is carried out in the presence of nitrogen for 1 hour and with stirring the mixture for 20 wt. % styrene and 80 wt. % acrylonitrile at a temperature of 105 ° C in the presence of 0.015% dithiobis (benzothiazla). Monomer conversion rate 8.3%, characteristic viscosity 1.15. EXAMPLE 2 The test was carried out as in Example 1, using 5% dithiobis (benzothiazole). The degree of conversion of monomers is 7.5%, the characteristic viscosity is 0.3.

МеркаптобензоФормула изобретени  Способ получени  сополимерсв путем радикальной сополимеризации стирола с акрилонитрилом в присутствии передатчика цепи, отличающийс  тем, целью эффективного регулировани  мспекул рного в:еса сополимера, в качеТабпицаЙMercaptobenzo Formula of the Invention A method for producing copolymers by radical copolymerization of styrene with acrylonitrile in the presence of a chain transmitter, characterized in that it effectively regulates the mass of the copolymer as:

ТаблицаЗTable3

Таблнца4 стве передатчика цепи используют 0,0155% от веса мономеров дитиобис{бенао тиазо а). Источники информации, прин тые во внимание при экспертизе: 1. Патент США Ne 3560418 . 26О-17, 1968.The chain transmitter of the chain uses 0.0155% of the weight of dithiobis monomers {benao tiazo a). Sources of information taken into account in the examination: 1. US patent Ne 3560418. 26O-17, 1968.

SU752113541A 1974-03-01 1975-02-28 Method of obtaining copolymers SU624576A3 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
BE141534A BE811750A (en) 1974-03-01 1974-03-01 PROCESS FOR PREPARING ABS RESINS.

Publications (1)

Publication Number Publication Date
SU624576A3 true SU624576A3 (en) 1978-09-15

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Family Applications (1)

Application Number Title Priority Date Filing Date
SU752113541A SU624576A3 (en) 1974-03-01 1975-02-28 Method of obtaining copolymers

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BE (1) BE811750A (en)
SU (1) SU624576A3 (en)

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BE811750A (en) 1974-07-01

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