DE899191C - Process for the production of vinyl chloride from dichloroethanes - Google Patents
Process for the production of vinyl chloride from dichloroethanesInfo
- Publication number
- DE899191C DE899191C DEF6337A DEF0006337A DE899191C DE 899191 C DE899191 C DE 899191C DE F6337 A DEF6337 A DE F6337A DE F0006337 A DEF0006337 A DE F0006337A DE 899191 C DE899191 C DE 899191C
- Authority
- DE
- Germany
- Prior art keywords
- vinyl chloride
- production
- dichloroethanes
- reaction
- distillation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/25—Preparation of halogenated hydrocarbons by splitting-off hydrogen halides from halogenated hydrocarbons
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00002—Chemical plants
- B01J2219/00004—Scale aspects
- B01J2219/00006—Large-scale industrial plants
Description
Gegenstand de|S Patents 857 957 ist ein Verfahren zur Herstellung von Vinylchlorid aus Dichlo-räthanen, bai welchem der Ausgangsstoff unter erhöhtem Druck auf hohe Temperaturen erhitzt und das Reaktionsgemisch nach dem A1> kühlen unter erhöhtem Druck fraktioniert destilliert wird.The subject of the | S patent 857 957 is a process for the production of vinyl chloride from dichloroethanes, in which the starting material is heated to high temperatures under increased pressure and the reaction mixture is fractionally distilled after cooling under increased pressure.
Es wurde nun gefunden, daß das; Verfahren auch noch Vorteile bietet, wenn man nach der Umsetzung unter Drude die Reaktionsgas ei entspannt und sie entweder einer Tieftemperaturdestillation unterzieht oder den Chlorwasserstoff vorher mit einem Absorptionsmittel entfernt und das Vinylchlorid dann durch Destillation vom nicht umgesetzten Dichloräthan abtrennt.It has now been found that this; Procedure too still offers advantages if the reaction gas is released under pressure after the reaction and either subjecting it to cryogenic distillation or previously with the hydrogen chloride an absorbent removed and then the vinyl chloride by distillation of the unreacted Separates dichloroethane.
B e i s ρ i e 1B e i s ρ i e 1
Durch ein Rohr aus Edelstahl von 1000 mm Länge und 6 mm lichter Weite werden, stündlich 6000 g H, 2 Dichloräthandampf gegeben. Die Reaktioiistemperatur beträgt etwa 6oo°. Der Druck während der Umsetzung wird auf 20 atü gehalten. Die den Ofen verlassenden. Reaktionsgase werden auf 700 abgekühlt und auf Normaldruck entspannt. Bei einer nachfolgenden Tieftemperaturdestillation werden stündlich 1090 g Chlorwasserstoff, 182101g Vinylchlorid und 3050 g nicht umgesetztes Dichloräthan erhalten. Bei diesem Umsatz entsteinen stündlich nur etwa 4 1 Spaltgas. Der Umsatz betragt 49 °/o, die Ausbeute an VinylchloridAre passed through a stainless steel tube of 1000 mm length and 6 mm internal diameter, 6000 g per hour is H, optionally 2 Dichloräthandampf. The reaction temperature is about 600 °. The pressure during the reaction is kept at 20 atmospheres. Those leaving the oven. Reaction gases are cooled to 70 0 and depressurized to atmospheric pressure. A subsequent low-temperature distillation gives 1090 g of hydrogen chloride, 182101 g of vinyl chloride and 3050 g of unreacted dichloroethane per hour. With this conversion, only about 4 liters of cracked gas pitted per hour. The conversion is 49% and the yield of vinyl chloride
98,0%. Das nicht umgesetzte Dichloräthan kann wteder der gleichen Reaktion unterworfen werden.98.0%. The unreacted dichloroethane can can be subjected to the same reaction.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEF6337A DE899191C (en) | 1950-12-27 | 1951-06-02 | Process for the production of vinyl chloride from dichloroethanes |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE302148X | 1950-12-27 | ||
DEF6337A DE899191C (en) | 1950-12-27 | 1951-06-02 | Process for the production of vinyl chloride from dichloroethanes |
Publications (1)
Publication Number | Publication Date |
---|---|
DE899191C true DE899191C (en) | 1953-12-10 |
Family
ID=25785894
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEF6337A Expired DE899191C (en) | 1950-12-27 | 1951-06-02 | Process for the production of vinyl chloride from dichloroethanes |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE899191C (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1100616B (en) * | 1957-09-10 | 1961-03-02 | Hoechst Ag | Process for the production of vinyl chloride by thermal cleavage of ethylene chloride |
DE1210800B (en) * | 1964-03-03 | 1966-02-17 | Huels Chemische Werke Ag | Process for the production of vinyl chloride by thermal cleavage of dichloroethane |
-
1951
- 1951-06-02 DE DEF6337A patent/DE899191C/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1100616B (en) * | 1957-09-10 | 1961-03-02 | Hoechst Ag | Process for the production of vinyl chloride by thermal cleavage of ethylene chloride |
DE1210800B (en) * | 1964-03-03 | 1966-02-17 | Huels Chemische Werke Ag | Process for the production of vinyl chloride by thermal cleavage of dichloroethane |
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