SU642285A1 - Method of obtaining 1,1,1-trifluorine-2-chloropropane and 1,1,1-trifluorine-3-chloropropane - Google Patents
Method of obtaining 1,1,1-trifluorine-2-chloropropane and 1,1,1-trifluorine-3-chloropropaneInfo
- Publication number
- SU642285A1 SU642285A1 SU772522635A SU2522635A SU642285A1 SU 642285 A1 SU642285 A1 SU 642285A1 SU 772522635 A SU772522635 A SU 772522635A SU 2522635 A SU2522635 A SU 2522635A SU 642285 A1 SU642285 A1 SU 642285A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- chloropropane
- products
- trifluorine
- reactor
- atm
- Prior art date
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Проведение процесса в указанных услови х позвол ет в 30Q-40.) раз уве личить радиащюнно-химичссл.т выход целевых продуктов по сравненшо с известным способом. Помимо резкого уве личени абсолютных выходов целевых продуктов существенно растет селективность процесса: при оптимальном мольном соотношении ТФП/НС1 1:3 отношение выходов Л ,б, т.а.в 3 раза выше по сравнению с известным способом (|Г/1 1,5). Пример 1,в металлический реактор, выполненный из никел (объеCarrying out the process under the specified conditions allows 30Q-40 times.) The increase in the radioactive chemical yield of the target products in comparison with the known method. In addition to a sharp increase in the absolute yields of the target products, the selectivity of the process increases significantly: with an optimal molar ratio of DFT / HC1 of 1: 3, the ratio of yields L, b, i.e., is 3 times higher than the known method (| G / 1 1.5 ). Example 1, in a metal reactor made of nickel (
Зависимость радиационно-химических выходов целевых продуктов и их соотношени от условий облучени в смес х ТФП-НС1 разного состава {температура облучени 30°С. мощность дозы, 33 .,6 рад/с) 5 135 см2, толщина стенок б мм), снабженный вентилем и съемной термостатирующей рубашкой дл съема тепла, выдел ющегос в процессе реакции, ввод т под давлением 15-45 атм Нсе и ТФП при известном отношении(см.табл.) Облучение смеси провод т на источнике гамма-облучени (мощность дозы 33,6 рад/с, врем облучени 2 ч, температура В процессе облучени осуществл ют периодический отбор пробы продуктов реакции, которые анализируют хроматографически. Полученные данные приведены в табл.1. ТаблицаThe dependence of the radiation-chemical yields of the target products and their ratio on the irradiation conditions in DFT-HC1 mixtures of different composition {irradiation temperature 30 ° C. dose rate, 33., 6 rad / s) 5 135 cm2, wall thickness b mm), equipped with a valve and a removable thermostatic jacket to remove heat generated during the reaction, are injected under pressure of 15-45 atm Hse and DFT with the known relation (see tab.) The mixture is irradiated at the gamma irradiation source (33.6 rad / s dose rate, irradiation time 2 hours, temperature. During the irradiation process, periodic sampling of the reaction products is carried out, which are analyzed chromatographically. The data obtained are in table 1. Table
, Как видно из приведенной табл,1, .радиационно-химический выход продуктов носит экстремальный характер, достига максимума при соотношении ТФП/НС :3 , Отношение продуктов II/1 также мен етс в зависимости от .состава с 5,1 до 2,7 при увеличении отношени ТФП/НС1 с 1:5 до 1:0,33 соответственно, Пример 2, .В металлическийAs can be seen from the table below, 1, the radiation-chemical yield of the products is of an extreme nature, reaching a maximum at a ratio of DFT / HC: 3. The ratio of products II / 1 also varies depending on the composition from 5.1 to 2.7 by increasing the DFT / HC1 ratio from 1: 5 to 1: 0.33, respectively, Example 2,. In metal
Зависимость выходов целевых .продуктов от времени облучени и материала реактора при гамма-облучении смеси состава ТФП/НС1 1;3 (температура , мощность дозы 33,6 рад/сf давление 42 атм) Dependence of target product yields on irradiation time and reactor material in gamma irradiation of a mixture of DFT / HC1 1; 3 (temperature, dose rate 33.6 rad / sf pressure 42 atm)
Как видно из табл 2, выход целевьЕк продуктов зависит от материала реактора и падает в р ду никель,неТржавеющаа сталь титан Ст.З. As can be seen from Table 2, the yield of target products depends on the material of the reactor and falls into a row of nickel, not stressful steel, titanium, Art.
Смесь целевых продуктов отдел ют (ОТ реакционной массы перегонкой при The mixture of the desired products is separated (FROM the reaction mass by distillation at
, Разделение 1 и II осуществл ют дистилл цией на ректификационной колонке . Температуры кипени .1 и 11 составл ют 30+0,5°С и 45+Ь,5°С соответственно .The separation of 1 and II is carried out by distillation on a distillation column. The boiling points .1 and 11 are 30 + 0.5 ° C and 45 + b, 5 ° C, respectively.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU772522635A SU642285A1 (en) | 1977-08-25 | 1977-08-25 | Method of obtaining 1,1,1-trifluorine-2-chloropropane and 1,1,1-trifluorine-3-chloropropane |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU772522635A SU642285A1 (en) | 1977-08-25 | 1977-08-25 | Method of obtaining 1,1,1-trifluorine-2-chloropropane and 1,1,1-trifluorine-3-chloropropane |
Publications (1)
Publication Number | Publication Date |
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SU642285A1 true SU642285A1 (en) | 1979-01-15 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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SU772522635A SU642285A1 (en) | 1977-08-25 | 1977-08-25 | Method of obtaining 1,1,1-trifluorine-2-chloropropane and 1,1,1-trifluorine-3-chloropropane |
Country Status (1)
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SU (1) | SU642285A1 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4947881A (en) * | 1989-02-24 | 1990-08-14 | Allied-Signal Inc. | Method of cleaning using hydrochlorofluorocarbons |
US5066418A (en) * | 1990-03-21 | 1991-11-19 | E. I. Du Pont De Nemours And Company | Binary azeotropic compositions of 3-chloro-1,1,1-trifluoropropane with methanol or ethanol, or trans-1,2-dichloroethylene |
US5211866A (en) * | 1991-11-26 | 1993-05-18 | Allied-Signal Inc. | Azeotrope-like compositions of 1-chloro-3,3,3-trifluoropropane and isopropanol |
US5213707A (en) * | 1991-11-26 | 1993-05-25 | Allied-Signal Inc. | Azeotrope-like compositions of 1-chloro-3,3,3-trifluoropropane and a mono- or dichlorinated C1 or C3 alkane |
US5227088A (en) * | 1991-11-26 | 1993-07-13 | Allied-Signal Inc. | Azeotrope-like compositions of 1-chloro-3,3,3-trifluoropropane and a C.sub.56 hydrocarbon |
-
1977
- 1977-08-25 SU SU772522635A patent/SU642285A1/en active
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4947881A (en) * | 1989-02-24 | 1990-08-14 | Allied-Signal Inc. | Method of cleaning using hydrochlorofluorocarbons |
US5066418A (en) * | 1990-03-21 | 1991-11-19 | E. I. Du Pont De Nemours And Company | Binary azeotropic compositions of 3-chloro-1,1,1-trifluoropropane with methanol or ethanol, or trans-1,2-dichloroethylene |
US5211866A (en) * | 1991-11-26 | 1993-05-18 | Allied-Signal Inc. | Azeotrope-like compositions of 1-chloro-3,3,3-trifluoropropane and isopropanol |
US5213707A (en) * | 1991-11-26 | 1993-05-25 | Allied-Signal Inc. | Azeotrope-like compositions of 1-chloro-3,3,3-trifluoropropane and a mono- or dichlorinated C1 or C3 alkane |
US5227088A (en) * | 1991-11-26 | 1993-07-13 | Allied-Signal Inc. | Azeotrope-like compositions of 1-chloro-3,3,3-trifluoropropane and a C.sub.56 hydrocarbon |
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