WO2002020443A1 - Procédé de production de 1,2-dichloroéthane - Google Patents
Procédé de production de 1,2-dichloroéthane Download PDFInfo
- Publication number
- WO2002020443A1 WO2002020443A1 PCT/RU2001/000093 RU0100093W WO0220443A1 WO 2002020443 A1 WO2002020443 A1 WO 2002020443A1 RU 0100093 W RU0100093 W RU 0100093W WO 0220443 A1 WO0220443 A1 WO 0220443A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- diχlορeτana
- liquid
- ethylene
- reaction
- dichloroethane
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/013—Preparation of halogenated hydrocarbons by addition of halogens
- C07C17/02—Preparation of halogenated hydrocarbons by addition of halogens to unsaturated hydrocarbons
Definitions
- a well-known method includes securing
- 35 is a selectivity of the reaction to the coolant and ethylene, which is 98-99% known as the coolant, tobacco and ethylene.
- One of the causes of an incomplete condition for ethylene is its failure to absorb (absorpt) in the liquid, and there is no outlet for it.
- Gaz ⁇ vaya ⁇ aza in case e ⁇ m ⁇ azbivae ⁇ sya in ⁇ sn ⁇ vn ⁇ m on ⁇ u ⁇ nye ⁇ uzy ⁇ i and ⁇ n ⁇ si ⁇ eln ⁇ neb ⁇ lsh ⁇ e ⁇ liches ⁇ v ⁇ mel ⁇ i ⁇ ⁇ uzy ⁇ ey, ⁇ e ⁇ mu ⁇ luchennaya gaz ⁇ zhid ⁇ s ⁇ naya mixture imee ⁇ s ⁇ avni ⁇ eln ⁇ b ⁇ lshuyu ⁇ bschuyu and non-specific ⁇ ve ⁇ n ⁇ s ⁇ ⁇ n ⁇ a ⁇ a between ⁇ azami. 5
- the liquid phase is discharged into the electric device with such a way that it is able to draw it in by the means of the discharge from the oil.
- the known method does not increase the efficiency of ethylene, but also does not ensure an increase in the efficiency of
- FIG. 1 shows a schematic of a reactor that implements the proposed method, with normal distributors and with an open dispersion
- ⁇ ⁇ ezul ⁇ a ⁇ e ⁇ a ⁇ iches ⁇ i is ⁇ lyuchae ⁇ sya v ⁇ zni ⁇ n ⁇ venie ⁇ b ⁇ ch- ny ⁇ ⁇ ea ⁇ tsy, ⁇ a ⁇ ⁇ a ⁇ ⁇ ni not "us ⁇ evayu ⁇ " ⁇ iz ⁇ y ⁇ i, blag ⁇ da ⁇ ya what ⁇ ez ⁇ v ⁇ z ⁇ as ⁇ ae ⁇ sele ⁇ ivn ⁇ s ⁇ ⁇ tsessa ⁇ a ⁇ ⁇ ⁇ l ⁇ u (d ⁇ 99.9%), and ⁇ a ⁇ ⁇ e ⁇ ilenu (d ⁇ 99.9%). Practically excluded is also the massive "start-up" of large gas blasts of ethylene, in view of the very small
- the proposed method is compared with the use of the solution to increase the conversion rate for electricity (up to 98%), to increase the output of the distribution unit.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Junction Field-Effect Transistors (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
L'invention concerne le domaine du génie chimique et peut être utilisée dans la production de 1,2-dichloroéthane par chloration directe de l'éthylène dans le dichloroéthane liquide. Le but de l'invention est d'accroître la conversion de l'éthylène et d'améliorer la sélectivité de la réaction du chlore et de l'éthylène. Pour réaliser ce procédé, on utilise un réacteur constitué d'un corps vertical (1) et d'une tube central (2) de réaction où s'effectue la circulation forcé du dichloroéthane liquide dans un circuit à circulation verticale dont le débit estimé est Q, sans tenir compte du début d'ébullition du dichloroéthane dans la zone de réaction (5). On introduit ensuite dans le réacteur le chlore et l'éthylène gazeux par des buses de distribution (4) et (6) disposées dans le tube (2). Le chlore et l'éthylène gazeux sont dispersés au préalable dans le dichloroéthane liquide par des buses (11) et (12) d'éjecteurs, et le dichloroéthane liquide est introduit dans la chambre d'admission de chaque éjecteur avec un débit Q¿1 ?représentant entre 1 et 20 % du débit estimé Q de l'écoulement du dichloroéthane liquide.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2001248934A AU2001248934A1 (en) | 2000-09-11 | 2001-02-27 | Method for producing 1,2-dichloroethane |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
RU2000123451A RU2186759C2 (ru) | 2000-09-11 | 2000-09-11 | Способ получения 1,2-дихлорэтана |
RU2000123451 | 2000-09-11 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2002020443A1 true WO2002020443A1 (fr) | 2002-03-14 |
Family
ID=20239954
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/RU2001/000093 WO2002020443A1 (fr) | 2000-09-11 | 2001-02-27 | Procédé de production de 1,2-dichloroéthane |
Country Status (3)
Country | Link |
---|---|
AU (1) | AU2001248934A1 (fr) |
RU (1) | RU2186759C2 (fr) |
WO (1) | WO2002020443A1 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006053895A1 (fr) * | 2004-11-19 | 2006-05-26 | Solvay (Societe Anonyme) | Reacteur et procede de reaction d’au moins deux gaz en presence d’une phase liquide |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3839475A (en) * | 1971-05-20 | 1974-10-01 | Allied Chem | Process for the production of ethylene dichloride |
DE1905517B2 (de) * | 1969-02-05 | 1977-01-27 | Hoechst Ag, 6000 Frankfurt | Vorrichtung zur herstellung von 1,2-dichloraethan |
GB1529249A (en) * | 1975-07-07 | 1978-10-18 | Syntex Inc | 21-acetals and mixed acetals of steroidal 21-aldehydes intermediates and methods of preparation |
-
2000
- 2000-09-11 RU RU2000123451A patent/RU2186759C2/ru not_active IP Right Cessation
-
2001
- 2001-02-27 WO PCT/RU2001/000093 patent/WO2002020443A1/fr active Application Filing
- 2001-02-27 AU AU2001248934A patent/AU2001248934A1/en not_active Abandoned
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1905517B2 (de) * | 1969-02-05 | 1977-01-27 | Hoechst Ag, 6000 Frankfurt | Vorrichtung zur herstellung von 1,2-dichloraethan |
US3839475A (en) * | 1971-05-20 | 1974-10-01 | Allied Chem | Process for the production of ethylene dichloride |
GB1529249A (en) * | 1975-07-07 | 1978-10-18 | Syntex Inc | 21-acetals and mixed acetals of steroidal 21-aldehydes intermediates and methods of preparation |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006053895A1 (fr) * | 2004-11-19 | 2006-05-26 | Solvay (Societe Anonyme) | Reacteur et procede de reaction d’au moins deux gaz en presence d’une phase liquide |
EA011397B1 (ru) * | 2004-11-19 | 2009-02-27 | Солвей (Сосьете Аноним) | Реактор и способ осуществления реакции по меньшей мере двух газов в присутствии жидкой фазы |
EA014143B1 (ru) * | 2004-11-19 | 2010-10-29 | Солвей (Сосьете Аноним) | Реактор и способ осуществления реакции по меньшей мере двух газов в присутствии жидкой фазы |
US7943099B2 (en) | 2004-11-19 | 2011-05-17 | Solvay (Societe Anonyme) | Reactor and method for reacting at least two gases in the presence of a liquid phase |
Also Published As
Publication number | Publication date |
---|---|
AU2001248934A1 (en) | 2002-03-22 |
RU2186759C2 (ru) | 2002-08-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US7416172B2 (en) | Submerged gas evaporators and reactors | |
US20070025889A1 (en) | Reactors, reactor assemblies and production processes | |
US4418651A (en) | System for heating and utilizing fluids | |
US4230668A (en) | Process and apparatus for producing halogenated unsaturated hydrocarbons | |
US20240208886A1 (en) | Process for the production of chlorinated hydrocarbons | |
JPH0777608B2 (ja) | ガスを接触させる方法と装置 | |
US4783564A (en) | Method for the preparation of 1,2-dichloroethane | |
WO2002020443A1 (fr) | Procédé de production de 1,2-dichloroéthane | |
US6156921A (en) | Method and apparatus for direct oxygen injection with a reactant stream into a fluidized bed reactor | |
US6841707B2 (en) | Method and apparatus for producing decabromodiphenyl alkanes | |
US3522017A (en) | Reactor for conducting controlledtemperature gas phase reactions with mixing | |
US4554392A (en) | Method of preparing 1,2-dichloroethane from ethylene and chlorine gas | |
TWI734811B (zh) | 製造鹵化丙烷之方法 | |
US3480416A (en) | Gas preparation process and apparatus | |
US20110230683A1 (en) | Process and apparatus for producing ethylenically unsaturated halogenated hydrocarbons | |
US2176453A (en) | Process and apparatus for treating hydrocarbon material | |
US4931012A (en) | Phase contactor/process for generating high temperature gaseous phase | |
US3350171A (en) | Vapour phase oxidation | |
US4996035A (en) | Preparation of nitrosyl fluoride | |
KR102706899B1 (ko) | 할로겐화 프로판을 제조하는 방법 | |
WO1997019895A1 (fr) | Procede de production de dioxyde de titane et reacteur chimico-plasmique pour la mise en oeuvre de ce procede | |
RU2299204C2 (ru) | Способ приготовления смесей о-ксилола с воздухом для получения фталевого ангидрида | |
US2090766A (en) | Process for treating mineral oils | |
RU2149154C1 (ru) | Способ получения 1,2-дихлорэтана | |
CN110342712A (zh) | 一种应用于mtbe萃取水的处理系统及方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AU BR CA CN DE ES GB ID IN JP KR SG TR UA US |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR |
|
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) |
Free format text: (EXCEPT AU, BR, ES, GB, ID, IN, SG, TR, UA, EP (AT, BE, CH, CY, DE, DK, ES, FI, FR, GB, GR, IE, IT,LU, MC, NL, PT, SE, TR)) |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
REG | Reference to national code |
Ref country code: DE Ref legal event code: 8642 |
|
122 | Ep: pct application non-entry in european phase | ||
NENP | Non-entry into the national phase |
Ref country code: JP |