Method and plant for preparing vinyl chloride from 1,2-dichloroethane

Patent metadata

Field	Value
Publication number	US-11820722-B2
Application number	US-202017607096-A
Country	US
Kind code	B2
Filing date	Apr 22, 2020
Priority date	Apr 30, 2019
Publication date	Nov 21, 2023
Grant date	Nov 21, 2023

Abstract

The present invention relates to a method for preparing vinyl chloride by catalytic thermal cracking of 1,2-dichloroethane, in which method the heat required for the thermal cracking is supplied via a liquid or condensing heat transfer medium. The present invention also relates to a plant for preparing vinyl chloride by catalytic thermal cracking of 1,2-dichloroethane, in which the heat required for the thermal cracking, as well as for the preceding preheating, evaporation and optionally overheating of the 1,2-dichloroethane, is supplied via a liquid or condensing heat transfer medium, said plant comprising at least one reactor in which the thermal cracking takes place and at least one first heating device by means of which heat is transported to the reaction medium in the reactor by means of the liquid or condensing heat transfer medium.

First claim

The invention claimed is:

1. A method for producing vinyl chloride by thermal cleavage of 1,2-dichloroethane, in which heat required for thermal cleavage is supplied via a liquid or condensing heat transfer medium, wherein the heat transfer medium is at least temporarily electrically heated, wherein at least one first heating device operated by combustion of at least one fuel and additionally at least one second heating device operated electrically are utilized to heat the liquid heat transfer medium, wherein the heat transfer medium is a mineral oil, a synthetic thermal oil, a silicon oil, or a molten salt, and the thermal cleavage of the 1,2-dichloroethane is carried out as a catalytic thermal cleavage in a temperature range from 200° C. to 400° C.

2. The method according to claim 1 , wherein the heat required for the thermal cleavage is temporarily exclusively provided by electrically heating the heat transfer medium.

3. The method according to claim 1 , wherein the 1,2-dichloroethane is preheated and/or evaporated and/or overheated by means of the heat transfer medium.

4. The method according to claim 1 , wherein the heat transfer medium is heated at least temporarily by the combustion of at least one fuel and partially by electrical heating.

5. The method according to claim 1 , wherein the heat transfer medium is conducted in a circuit and the at least one first heating device and the at least one second heating device operated electrically are integrated into this circuit.

6. The method according to claim 1 , wherein at least one first heating device and at least one second heating device operated electrically are connected in series or in parallel in a circuit.

7. The method according to claim 1 , wherein the heat transfer medium is conducted in a circuit into which a reactor is integrated, in which the catalytic thermal cleavage of 1,2-dichloroethane is carried out, wherein a heat exchange takes place between the reaction medium of the reactor and the heat transfer medium.

8. The method according to claim 1 , wherein the heat transfer medium is conducted in a circuit in which devices for preheating and/or evaporating and/or overheating are integrated in addition to the reactor in which the catalytic thermal cleavage of 1,2-dichloroethane is carried out, wherein a heat exchange takes place between the reaction medium and the heat transfer medium.

9. The method according to claim 8 , wherein the heat transfer medium is conducted in the circuit in countercurrent to the flow of the reaction medium through the reactor.

10. The method according to claim 1 , wherein the second heating device operated electrically is operated at least temporarily by electrical energy obtained from renewable sources.

11. The method according to claim 1 , wherein the second heating device operated electrically is operated in standby mode.

12. A plant for producing vinyl chloride by thermal cleavage of 1,2-dichloroethane, in which heat required for thermal cleavage is supplied via a liquid or condensing heat transfer medium, comprising at least one reactor in which catalytic thermal cleavage of 1,2-dichloroethane takes place and at least one first heating device by which a supply of heat to the reaction medium in the reactor takes place by the liquid or condensing heat transfer medium, wherein the system further comprises at least one electrical second heating device for heating the heat transfer medium, wherein the heat transfer medium is a mineral oil, a synthetic thermal oil, a silicon oil, or a molten salt, and the heating devices are configured to heat the heat transfer medium for the catalytic thermal cleavage of the 1,2-dichloroethane to be carried out in a temperature range from 200° C. to 400° C.

13. The plant according to claim 12 , wherein the reactor is integrated into a circuit of the heat transfer medium, wherein additionally at least the second electrical heating device is integrated into the circuit.

14. The plant according to claim 12 , wherein at least one first heating device operated via a fuel and further at least one second electrical heating device as well as at least one device for heating and/or evaporating and/or overheating the starting material 1,2-dichloroethane is integrated into the circuit of the heat transfer medium.

15. The plant according to claim 12 , wherein the circuit of the heat transfer medium comprises a pump integrated into a line system, at least one first heating device operated via a fuel, at least one second electrical heating device and the reactor, wherein means for transferring heat from the heat transfer medium to a reaction medium flowing through the reactor are provided.

16. The plant according to claim 14 , wherein the first heating device operated via a fuel and the electrical second heating device are arranged in series or in parallel in the circuit of the heat transfer medium.

Assignees

• Thyssenkrupp Ag
• Thyssenkrupp Ind Solutions Ag
• Vinnolit Gmbh & Co Kg

Inventors

• Benje Michael
• Kammerhofer Peter
• Krejci Klaus

Classifications

• C07C17/25 Primary

  by splitting-off hydrogen halides from halogenated hydrocarbons · CPC title

• B01J19/0013

  Controlling the temperature of the process · CPC title

• B01J2219/00132

  using electric heating or cooling elements · CPC title

• B01J2219/00157

  by means of a burner · CPC title

• C07C21/06

  Vinyl chloride · CPC title