SU927801A1 - Process for producing copolymers containing acrylamide and acrylonitrile links - Google Patents
Process for producing copolymers containing acrylamide and acrylonitrile links Download PDFInfo
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- SU927801A1 SU927801A1 SU792854672A SU2854672A SU927801A1 SU 927801 A1 SU927801 A1 SU 927801A1 SU 792854672 A SU792854672 A SU 792854672A SU 2854672 A SU2854672 A SU 2854672A SU 927801 A1 SU927801 A1 SU 927801A1
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Изобретение относитс к высокомолекул рным соединени м, в частности к получению полимеров, содержащих акриламидные и акрилонитрильные звень , которые могут примен тьс в химической промышленности и, в частности , при получении синтетических волокон на основе полиакрилонитрила.The invention relates to high molecular compounds, in particular to the preparation of polymers containing acrylamide and acrylonitrile units, which can be used in the chemical industry and, in particular, in the preparation of synthetic fibers based on polyacrylonitrile.
Известен способ получени полимеров , содержащих акриламидные и акрилонитрйльные звень , путем сополимеризации акрилонитрила с акриламидом в 51,5%-ном водном растворе роданистого натри , при в течение 30-60 мин 1.A method of producing polymers containing acrylamide and acrylonitrile units is known, by copolymerizing acrylonitrile with acrylamide in a 51.5% aqueous solution of sodium rhodanate, for 30-60 minutes 1.
Однако при этом конверси акрилонитрила достигает.85-90%, а конверси акриламида - полна . Следовательно в данном процессе требуетс удаление непрореагировавшего акрилонитрила и возвращение его на стадию полимеризации, что .усложн ет технологическую схему. Кроме того, акриламид - весьма дефицитный и дорогосто щий мономер.However, the conversion of acrylonitrile reaches .85-90%, and the conversion of acrylamide is complete. Consequently, this process requires the removal of unreacted acrylonitrile and its return to the polymerization stage, which complicates the technological scheme. In addition, acrylamide is a very scarce and expensive monomer.
Известен способ получени аналогичных полимеров путем гидролиза полиакрилонитрила в присутствии серной кислоты. Сернокислотный гидролиз полиакрилонитрила проводитс приA known method for producing similar polymers by hydrolysis of polyacrylonitrile in the presence of sulfuric acid. Sulfuric acid hydrolysis of polyacrylonitrile is carried out at
20-25 С и продолжительности процесса 5 ч, после чего из реакционной смеси полимер, содержащий акриламидные и акрилонитрильные звень , высаживаетс водой, а затем промываетс большим количеством воды дл удалени серной кислоты. Попытка сокращени продолжительности реакции за счет повышени температуры не приto водит к жела.емому результату, так как в этом случае получают полимеры , не содержащие акрилонитрильных звеньев 2.20-25 ° C and a process time of 5 hours, after which the polymer containing acrylamide and acrylonitrile units from the reaction mixture is precipitated with water and then washed with plenty of water to remove sulfuric acid. An attempt to shorten the reaction time due to an increase in temperature does not lead to the desired result, since in this case polymers are obtained that do not contain acrylonitrile units 2.
15 Недостатками способа вл ютс 15 The disadvantages of the method are
большое количество сточных вод, трудоемкое разделение реакционной смеси , утилизаци большого количества разбавленной серной кислоты, котора large amounts of wastewater, laborious separation of the reaction mixture, disposal of large quantities of dilute sulfuric acid, which
20 образуетс на стадии выделени полимера .20 is formed in the polymer isolation stage.
Наиболее близким к предлагаемому по технической сущности вл етс способ получени сополимеров, содержащих акриламидные и акрилонитрильные звень , гидролизом полиакрилонитрила в водном растворе роданистых солей, в присутствии катализатора неорганического или органическогоThe closest to the proposed technical essence is a method for producing copolymers containing acrylamide and acrylonitrile units by hydrolyzing polyacrylonitrile in an aqueous solution of rhodium salts in the presence of an inorganic or organic catalyst.
30 основани 3.30 bases 3.
Недостатком этого способа вл етс необходимость вымывани и/или нейтрализации основани после достижени заданной степени гидролиза, что усложн ет технологию.The disadvantage of this method is the need to wash out and / or neutralize the base after reaching the desired degree of hydrolysis, which complicates the technology.
Цель изобретени - упрощение технологии .The purpose of the invention is to simplify the technology.
Указанна цель достигаетс тем, что согласно способу получени сополимеров , содержащих акриламидные и акрилонитрильные звень , гидролизом полиакрилонитрила в водном растворе роданистых солей, в присутствйи катализатора, в качестве катализатора используют двуокись марганца или катализатора . на основе активированной металлической меди.This goal is achieved in that according to the method for producing copolymers containing acrylamide and acrylonitrile units by hydrolyzing polyacrylonitrile in an aqueous solution of rhodium salts, in the presence of a catalyst, manganese dioxide or a catalyst is used as a catalyst. based on activated metallic copper.
В предлагаемом способе катализатор удал етс из реакционной массы фильтрованием и может быть использован многократно.In the proposed method, the catalyst is removed from the reaction mass by filtration and can be used many times.
В результате гидролиза получаютс полимеры, содержащие 5-50% акриламидных звеньев. .При этом врем проведени реакции 30-60 мин. В случае применени частично гидратированного полиакрилонитрнла в производстве синтетического волокна, полученна в результате гидролиза реакционна масса может непосредственно быть использована дл формовани волокна.As a result of hydrolysis, polymers are obtained containing 5-50% acrylamide units. At the same time, the reaction time is 30-60 minutes. In the case of using partially hydrated polyacrylonitrile in the production of synthetic fiber, the reaction mass obtained by hydrolysis can be directly used to form the fiber.
Пример 1.30Г сплава Дьюара (50% Си, 45% А и 5% Zn) обрабатывают 200 мл 25%-ного водного раствора едкого натра при 20-25 С 15 ч. Осадок отфильтровывают и проливают водой до нейтральной реакции и полученный скелетный медный катализатор используют при гидролизе полиакрилонитрила.Example 1.30G Dewar alloy (50% Cu, 45% A and 5% Zn) is treated with 200 ml of a 25% aqueous solution of caustic soda at 20–25 ° C for 15 h. The precipitate is filtered and shed with water until neutral and the resulting skeletal copper catalyst used in the hydrolysis of polyacrylonitrile.
В стекл нную ампулу помешают 2 г скелетного медного катализатора и 0,3 г полиакрилонитрила (характеристическа в зкость 3,9 дл/г), растворенного в 15 мл 52%-ного водного раствора роданистого кеши и выдерживают при перемешивании 30 мин при 80 с. Из реакционной смеси полимер высаживают водой, затем промывают водой до отрицательной реакции , на роданид кали и после сушки анализируют ИК-спектроскопически, а также определ ют содержание в нем азота, по которому суд т о составе сополимера. Выделено 0,32 г полимера , который содержит 5% акриламидных звеньев и 95% акрилонитрильных звеньев. Характеристическа в зкость 4,0 дл/г.In a glass vial, 2 g of a skeletal copper catalyst and 0.3 g of polyacrylonitrile (intrinsic viscosity 3.9 dl / g) dissolved in 15 ml of a 52% aqueous solution of rhodanite cache and stirred for 30 minutes at 80 s. From the reaction mixture, the polymer is precipitated with water, then washed with water until a negative reaction, potassium rhodium, and after drying, analyzed by IR spectroscopy, and the content of nitrogen in it is determined by which the composition of the copolymer is judged. 0.32 g of polymer was isolated, which contains 5% acrylamide units and 95% acrylonitrile units. Inherent viscosity 4.0 dl / g.
Результаты примеров 2-4, проведенных по методике примера 1, представлены в табл. 1.The results of examples 2-4, carried out according to the method of example 1, are presented in table. one.
Таблица 1Table 1
Пример 5. В ампулу Помещают 2 г двуокиси марганца и Ю мл 8,2%ного раствора полиакрилонитрила 45 (характеристическа в зкость 4,0 дп/г) в 52%-ном водном растворе роданистого натри . Ампулу выдерживают при 80°С 1 ч, после чего в зкую реакционную массу разбавл ют Ю мл водно8 ,2Example 5. 2 g of manganese dioxide and 10 ml of a 8.2% solution of polyacrylonitrile 45 (intrinsic viscosity 4.0 dp / g) in a 52% aqueous solution of rhodium sodium are placed in a vial. The ampoule is kept at 80 ° C for 1 h, after which the viscous reaction mass is diluted with 10 ml of water;
4,0 8,2 4.0 8.2
го раствора роданистого натри . Катализатор отфильтровывают и полимер высаживают водой. В полученном полимере (0,35 г) найдено 32% акриламидных звеньев и бв% акрилонитрильных звеньев. Результаты опытов 6-9 приведены в табл. 2.th solution of rhodium sodium. The catalyst is filtered off and the polymer is precipitated with water. In the polymer obtained (0.35 g), 32% acrylamide units and bv% acrylonitrile units were found. The results of experiments 6-9 are given in table. 2
Таблица 2table 2
3636
.30.thirty
41 40 5241 40 52
100 100
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SU792854672A SU927801A1 (en) | 1979-11-11 | 1979-11-11 | Process for producing copolymers containing acrylamide and acrylonitrile links |
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Cited By (1)
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WO2011097184A3 (en) * | 2010-02-05 | 2011-11-24 | International Battery, Inc. | Rechargeable battery using an aqueous binder |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2011097184A3 (en) * | 2010-02-05 | 2011-11-24 | International Battery, Inc. | Rechargeable battery using an aqueous binder |
US8076026B2 (en) | 2010-02-05 | 2011-12-13 | International Battery, Inc. | Rechargeable battery using an aqueous binder |
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