SU178368A1 - METHOD OF OBTAINING CHLORINE VINYL - Google Patents
METHOD OF OBTAINING CHLORINE VINYLInfo
- Publication number
- SU178368A1 SU178368A1 SU834852A SU834852A SU178368A1 SU 178368 A1 SU178368 A1 SU 178368A1 SU 834852 A SU834852 A SU 834852A SU 834852 A SU834852 A SU 834852A SU 178368 A1 SU178368 A1 SU 178368A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- ethylene
- water vapor
- chlorine
- chlorine vinyl
- obtaining chlorine
- Prior art date
Links
- 239000000460 chlorine Substances 0.000 title description 6
- 229910052801 chlorine Inorganic materials 0.000 title description 6
- -1 CHLORINE VINYL Chemical class 0.000 title 1
- 239000005977 Ethylene Substances 0.000 claims description 8
- VGGSQFUCUMXWEO-UHFFFAOYSA-N ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 238000005660 chlorination reaction Methods 0.000 claims description 5
- BZHJMEDXRYGGRV-UHFFFAOYSA-N vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 description 6
- ZAMOUSCENKQFHK-UHFFFAOYSA-N chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 5
- 239000007789 gas Substances 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N HCl Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- GZETWZZNDACBTQ-UHFFFAOYSA-N [Cl].C=C Chemical compound [Cl].C=C GZETWZZNDACBTQ-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- CTUDRLGCNRAIEA-UHFFFAOYSA-L calcium;chloride;hydroxide Chemical compound [OH-].[Cl-].[Ca+2] CTUDRLGCNRAIEA-UHFFFAOYSA-L 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
Description
Известен способ получени хлористого винила хлорированием этилена в присутствии хлористого винила при температуре 400- 450°С, соотношении хлор - этилен - хлорвинил , равном 1 : 2,8 : 2,2, и времени реакции 5 сек. Выход продукта составл ет 93-98%.A known method of producing vinyl chloride by chlorination of ethylene in the presence of vinyl chloride at a temperature of 400-450 ° C, a ratio of chlorine to ethylene-chlorovinyl is 1: 2.8: 2.2, and the reaction time is 5 seconds. The product yield is 93-98%.
Цель изобретени - упростить процесс. Достигаетс это тем, что хлорирование этилена ведут в присутсгвии вод ного пара, что исключает возможность сажеобразовани и необходимость циркул ции непрореагировавших и избыточных газов, а также сокращает врем реакции, аппаратурное оформление значительно упрощаетс .The purpose of the invention is to simplify the process. This is achieved by the fact that the chlorination of ethylene is carried out in the presence of water vapor, which eliminates the possibility of soot formation and the need for the circulation of unreacted and excess gases, and also shortens the reaction time, the instrumentation is greatly simplified.
Способ заключаетс в хлорировании этилена в присутствии вод ного пара. Соотношение этилен - хлор - вод ной пар равно 1:1: 4- 5. Выход продукта составл ет 95%.The method involves the chlorination of ethylene in the presence of water vapor. The ratio of ethylene to chlorine water vapor is 1: 1: 4-5. The product yield is 95%.
Пример. В реакционный аппарат, представл ющий собой полую трубку, снабженную электрообогревом, ввод т предварительно подогретый до температуры реакции этилен и смесь хлора с вод ным паром. ТемпературуExample. Preheated to the reaction temperature ethylene and a mixture of chlorine with steam are introduced into the reaction apparatus, which is a hollow tube, equipped with electrical heating. Temperature
реакции поддерживают в пределах 400- 450°С. Мол рное соотношение реагентов этилен- хлор - вод ной пар 1:1:4,5, врем пребывани смеси в зоне реакции 2-3 сек.the reaction is maintained within 400-450 ° C. The molar ratio of the reactants ethylene chlorine to water vapor is 1: 1: 4.5, the residence time of the mixture in the reaction zone is 2-3 seconds.
Реакционные газы на выходе из хлоратора проход т холодильник, где коиденсируетс вод ной пар и образуетс 25-28%-на сол на кислота. Затем газы промывают раствором щелочи, сушат хлористым кальцием и едким кали и конденсируют. Выход хлористого винила составл ет 90-95% от вступившего в реакцию хлора или этилена. Конверси хлора за проход составл ет lOOVoПредмет изобретени The reaction gases at the outlet of the chlorinator pass through a cooler where water vapor is co-sensitized and 25-28% hydrochloric acid is formed. Then the gases are washed with alkali solution, dried with calcium chloride and potassium hydroxide and condensed. The yield of vinyl chloride is 90-95% of the chlorine or ethylene reacted. The chlorine conversion per pass is lOOVo.
Claims (2)
Publications (1)
Publication Number | Publication Date |
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SU178368A1 true SU178368A1 (en) |
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