SU367115A1 - METHOD OF OBTAINING BLOXOPOLYMERS - Google Patents
METHOD OF OBTAINING BLOXOPOLYMERSInfo
- Publication number
- SU367115A1 SU367115A1 SU1305284A SU1305284A SU367115A1 SU 367115 A1 SU367115 A1 SU 367115A1 SU 1305284 A SU1305284 A SU 1305284A SU 1305284 A SU1305284 A SU 1305284A SU 367115 A1 SU367115 A1 SU 367115A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- propylene
- polymerization
- propane
- carried out
- bloxopolymers
- Prior art date
Links
- 238000000034 method Methods 0.000 title description 4
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 14
- 238000006116 polymerization reaction Methods 0.000 description 11
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 10
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 10
- -1 polypropylene Polymers 0.000 description 7
- 239000001294 propane Substances 0.000 description 7
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 6
- 239000004743 Polypropylene Substances 0.000 description 6
- 229920001155 polypropylene Polymers 0.000 description 6
- 229920001400 block copolymer Polymers 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000000178 monomer Substances 0.000 description 4
- 229920002554 vinyl polymer Polymers 0.000 description 4
- 239000002904 solvent Substances 0.000 description 3
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 3
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- LDLDYFCCDKENPD-UHFFFAOYSA-N ethenylcyclohexane Chemical compound C=CC1CCCCC1 LDLDYFCCDKENPD-UHFFFAOYSA-N 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000000737 periodic effect Effects 0.000 description 2
- JTXAHXNXKFGXIT-UHFFFAOYSA-N propane;prop-1-ene Chemical group CCC.CC=C JTXAHXNXKFGXIT-UHFFFAOYSA-N 0.000 description 2
- WSSSPWUEQFSQQG-UHFFFAOYSA-N 4-methyl-1-pentene Chemical compound CC(C)CC=C WSSSPWUEQFSQQG-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical group CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 125000000753 cycloalkyl group Chemical group 0.000 description 1
- 239000003989 dielectric material Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000010408 film Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 150000002902 organometallic compounds Chemical class 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000012429 reaction media Substances 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003623 transition metal compounds Chemical class 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- 239000004711 α-olefin Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F297/00—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer
- C08F297/06—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the coordination type
- C08F297/08—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the coordination type polymerising mono-olefins
Landscapes
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Graft Or Block Polymers (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Polymerization Catalysts (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Description
1one
Изобретение относитс к способу получени блоксополимеров - полиалломеров.The invention relates to a process for the preparation of block copolymers - polyallomers.
Эти полимеры -примен ютс в различных област х техники благодар их ценным физико-механическим свойствам. Дл улучшени таких свойств полипропилена, как морозостойкость , теплостойкость, механических по .казателей и тому подобных, получают лолиалломеры на основе пропилена и других а-олефинов (этилена, бутена-1, изобутилена, 4-метилпентена-1 и других) при их последовательной .полимеризации.These polymers are used in various fields of technology due to their valuable physicomechanical properties. To improve the properties of polypropylene, such as frost resistance, heat resistance, mechanical characteristics and the like, lolyallomers based on propylene and other α-olefins (ethylene, butene-1, isobutylene, 4-methylpentene-1 and others) are obtained with their sequential. polymerization.
С целью придани полипропилену повышенной морозо- и теплостойкости в сочетании с повышенной ударопрочностью предлагаетс способ получени блоксополимеров на основе пропилена, предусматривающий применение в качестве сомономеров винилциклоалканов. Последовательную полимеризацию пропилена с винилциклоалканами провод т в среде пропана , алифатического или циклического углеводородного растворител , парафиновых фракций керосина и газолина при температуре 28-80°С (лучше 30-50°С) и давлении 1-40 ати. В качестве катализаторов примен ют соединени на основе солей переходных металлов IV-VHI групп периодической системы и органических соединений металлов I-П1 групп периодической системы элементов . Вначале провод т полимеризацию пропилена до треоуемой степени конверсии, затем непрореагировавший пропилен сдувают и в реакционную смесь ввод т определенное количество винилциклоалкана и продолжаютIn order to impart increased frost and heat resistance to polypropylene in combination with increased impact resistance, a method of producing propylene-based block copolymers is proposed, which involves the use of vinylcycloalkanes as comonomers. The sequential polymerization of propylene with vinylcycloalkanes is carried out in the medium of propane, an aliphatic or cyclic hydrocarbon solvent, paraffin fractions of kerosene and gasoline at a temperature of 28-80 ° C (preferably 30-50 ° C) and a pressure of 1-40 at. Compounds based on salts of transition metals of the IV-VHI groups of the periodic system and organic compounds of metals I-P1 of the groups of the periodic system of elements are used as catalysts. First, the polymerization of propylene is carried out to a triple degree of conversion, then the unreacted propylene is blown off and a certain amount of vinylcycloalkane is introduced into the reaction mixture and continued
полимеризацию. При применении в качестве растворител пропана дл полимеризации используют пропан-пропиленовые и пропанвинилциклоалкановые смеси, а реакцию провод т при давлении 10-40 (лучше 15-polymerization. When propane is used as a solvent for polymerization, propane-propylene and propane-vinylcycloalkane mixtures are used, and the reaction is carried out at a pressure of 10-40 (preferably 15-
20) ати. При применении других инертных органических растворителей используют чистые мономеры и полимеризацию провод т при 1-40 (лучше 1-20) ати. Сополимеризацию прекраш,ают путем подачи в реакционную среду изопропилового спирта. Отмытые от остатков катализатора и высушенные в вакууме блоксополимеры обладают по сравнению с полипропиленом, полученным в аналогичных услови х, повышенной морозостойкостью , теплостойкостью, удельной ударной в зкостью и, как правило, большим относительным удлинением (см. таблицу). Получаемые блоксополимеры - полиалломеры могут примен тьс дл производства изделий с повышенным сопротивлением удара при низких температурах, а также в качестве диэлектриков , волокно- и пленкообразуюш,их материалов с повышенной тепло- и морозостойкостью. Пример 1. В автоклав емкостью 1 л,20) ATI. When using other inert organic solvents, pure monomers are used and the polymerization is carried out at 1-40 (preferably 1-20) at. The copolymerization is terminated by feeding isopropyl alcohol into the reaction medium. Washed from catalyst residues and vacuum-dried block copolymers, compared with polypropylene obtained under similar conditions, have increased frost resistance, heat resistance, specific toughness and, as a rule, greater elongation (see table). The resulting copolymers - polyallomers can be used for the production of products with increased impact resistance at low temperatures, as well as dielectrics, fiber and film forming, their materials with high heat and cold resistance. Example 1. In a 1 liter autoclave,
снабженный электромагнитной мешалкой иequipped with an electromagnetic stirrer and
рубашкой, оттренированный под вакуумом в течение 1 час и продутый сухим очищенным аргоном или пропаном, загружают без доступа влаги и кислорода воздуха 300 г конденсированной пропан-пропиленовой смеси (содержание мономера 80 вес. %). Повышают температуру в реакторе до и подают каталитический -комплекс, состо щий из 4,06 г TiCls (б-форма алюмотермического восстановлени , STiCls Aids) и 6,8 г 98%-кого А1(С2Н5)2С1. Начальное давление 12 ати. Полимеризацию пропилена провод т при перемещивании в течение 30 мин и температуре 40°С. Реакцию контролируют по убыли давлени и хроматографическн. Через 30 мин из реактора сбрасывают непрореагировавщий пропилен вместе с пропаном, автоклав продувают пропаном, а затем загружают 180 г конденсированного пропана и 48 г винилциклогексана . Реакцию полимеризации винилциклогексана на «живых макроцеп х полипропилена провод т 2 час при температуре 40°С. Затем в автоклав ввод т после сдувки пропана 50 мл изопропилового спирта. Суспензию выгружают из автоклава, отфильтроБывают , промывают от остатков катализатора и сушат до посто нного веса при температуре 80°С и остаточном давлении 1 мм рт. ст.jacket, drained under vacuum for 1 hour and purged with dry purified argon or propane, load 300 g of condensed propane-propylene mixture (monomer content is 80 wt.%) without moisture and oxygen access. The temperature in the reactor is increased before and the catalytic-complex consisting of 4.06 g of TiCls (b-form of aluminothermic reduction, STiCls Aids) and 6.8 g of 98% A1 (C2H5) 2C1 are fed. The initial pressure is 12 ati. The polymerization of propylene is carried out while moving for 30 minutes and at a temperature of 40 ° C. The reaction is monitored by pressure drop and chromatographic. After 30 minutes, unreacted propylene is dropped from the reactor along with propane, the autoclave is blown with propane, and then charged 180 g of condensed propane and 48 g of vinylcyclohexane. The reaction of polymerization of vinylcyclohexane on live macroplate x of polypropylene is carried out for 2 hours at a temperature of 40 ° C. After propane is blown, 50 ml of isopropyl alcohol are then introduced into the autoclave. The suspension is discharged from the autoclave, filtered, washed from the catalyst residues and dried to constant weight at a temperature of 80 ° C and a residual pressure of 1 mm Hg. Art.
Выход лолиалломера 114 г, теплостойкость по Вика 107°С, морозостойкость -30°С, удельна ударна в зкость 7,24 кгсм/см. Дл полипропилена, полученного в аналогичных услови х, соответствующие показатели равны: 92°С, - 15°С и 5,73 кгсм/см.The output of loliallomer is 114 g, Vicat heat resistance is 107 ° C, cold resistance is -30 ° C, specific impact viscosity is 7.24 kgcm / cm. For polypropylene produced under similar conditions, the corresponding figures are: 92 ° C, –15 ° C and 5.73 kgcm / cm.
Пример 2. Полимеризацию пропилена провод т, как в примере 1, в течение 120 мин при температуре 30°С в присутствии каталитического комплекса, состо щего из 4 г TiCls и 8 г А1(С2Н5)2С1. Стадию полимеризации винилдиклогексана на «живых полипропиленовых макроцеп х провод т в течение 3 час при температуре 30°С. Выход полиалломера 203 г, теплостойкость по Вика 106°С, морозостойкость -32°С, удельна ударна в зкость 14,7 кгсм/см.Example 2. The polymerization of propylene was carried out as in Example 1 for 120 minutes at a temperature of 30 ° C in the presence of a catalytic complex consisting of 4 g of TiCls and 8 g of Al (C2H5) 2C1. The stage of polymerization of vinyl diclohexane on live polypropylene macrochip x is carried out for 3 hours at a temperature of 30 ° C. The output of polyallomer is 203 g, Vic heat resistance is 106 ° C, cold resistance is -32 ° C, specific impact viscosity is 14.7 kgcm / cm.
Физико-механические свойства некоторыхPhysicomechanical properties of some
блоксополимероБ на основе пропиленаpropylene block copolymerB
и винилЦИКлоалкановand vinyl cycloalkanes
Предмет изобретени Subject invention
Способ получени блоксополимеров последовательной полимеризацией пропилена и виниловых мономеров в среде инертного углеводородного растворител с применением катализатора , состо щего из соединений переходных металлов IV-VIII группы и металлоорганических соединений металлов I-III груплы , отличающийс тем, что, с целью увеличени ударопрочности при низких температурах и теплостойкости конечных продуктов, в качестве виниловых мономеров примен ют винилциклоалканы , например вин лциклогексан .The method of producing block copolymers by sequential polymerization of propylene and vinyl monomers in an inert hydrocarbon solvent using a catalyst consisting of group IV-VIII transition metal compounds and organometallic compounds of metals I-III, in order to increase the impact resistance at low temperatures and heat resistance of the final products, vinylcycloalkanes are used as vinyl monomers, for example, vin lcyclohexane.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU1305284A SU367115A1 (en) | 1968-12-27 | 1968-12-27 | METHOD OF OBTAINING BLOXOPOLYMERS |
| FR6944563A FR2027194A1 (en) | 1968-12-27 | 1969-12-23 | |
| GB6272369A GB1282728A (en) | 1968-12-27 | 1969-12-23 | Crystalline block copolymers consisting of propylene units and vinyl monomer units and a process of producing the same |
| DE19691964883 DE1964883C3 (en) | 1968-12-27 | 1969-12-24 | Crystalline block copolymers made from propylene units and vinylcycloalkane units |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU1305284A SU367115A1 (en) | 1968-12-27 | 1968-12-27 | METHOD OF OBTAINING BLOXOPOLYMERS |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU367115A1 true SU367115A1 (en) | 1973-01-23 |
Family
ID=20444653
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU1305284A SU367115A1 (en) | 1968-12-27 | 1968-12-27 | METHOD OF OBTAINING BLOXOPOLYMERS |
Country Status (4)
| Country | Link |
|---|---|
| DE (1) | DE1964883C3 (en) |
| FR (1) | FR2027194A1 (en) |
| GB (1) | GB1282728A (en) |
| SU (1) | SU367115A1 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6124449A (en) * | 1984-07-13 | 1986-02-03 | 住友化学工業株式会社 | Oriented composite polypropylene film |
| KR900016267A (en) * | 1989-04-25 | 1990-11-13 | 노기 사다오 | Titanium trichloride composition for the production of olefin polymers and process for the preparation thereof |
| US5077341A (en) * | 1989-06-19 | 1991-12-31 | Chisso Corporation | Process for producing a high-stiffness polypropylene and a highly stereoregular polypropylene |
| DE60130890T2 (en) * | 2001-09-26 | 2008-08-14 | Hilti Ag | Inductive sensor arrangement and method for detecting iron objects |
-
1968
- 1968-12-27 SU SU1305284A patent/SU367115A1/en active
-
1969
- 1969-12-23 GB GB6272369A patent/GB1282728A/en not_active Expired
- 1969-12-23 FR FR6944563A patent/FR2027194A1/fr not_active Withdrawn
- 1969-12-24 DE DE19691964883 patent/DE1964883C3/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| FR2027194A1 (en) | 1970-09-25 |
| DE1964883A1 (en) | 1970-09-17 |
| DE1964883B2 (en) | 1978-11-09 |
| GB1282728A (en) | 1972-07-26 |
| DE1964883C3 (en) | 1979-07-12 |
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