METHOD AND PLANT FOR PREPARING VINYL CHLORIDE FROM 1,2-DICHLOROETHANE

Abstract

Disclosed is 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, wherein, the heat transfer medium is heated at least in part by means of waste heat from a plant for combusting liquid and/or gaseous residues of a chemical plant. The invention also relates to a plant for preparing vinyl chloride by catalytic thermal cracking of 1,2-dichloroethane. The heat required for thermal cracking can be obtained from cheaply available waste heat. For example, it is possible to temporarily heat the heat transfer medium exclusively by means of the second heating device operated by waste heat, wherein said waste heat can, for example, be waste heat from a plant for preparing vinyl chloride.

Claims

1-17. (canceled)

18. A method for producing vinyl chloride by catalytic thermal cleavage of 1,2-dichloroethane, in which the heat required for thermal cleavage is supplied via a liquid or condensing heat transfer medium, wherein the heat transfer medium is at least temporarily and/or at least partially or completely heated by the waste heat from a plant for the incineration of liquid and/or gaseous residues from a chemical plant.

19. The method according to claim 18, wherein the 1,2-dichloroethane is preheated and/or evaporated and/or overheated by the heat transfer medium.

20. The method according to claim 18, wherein the heat transfer medium is heated at least temporarily and/or at least partially by the combustion of at least one fuel and partially by heating it via waste heat.

21. The method according to claim 18, wherein at least one first heating device operated by combustion of at least one fuel and additionally at least one second heating device operated via waste heat are utilized to heat the liquid heat transfer medium.

22. The method according to claim 21, 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 via waste heat are integrated into this circuit.

23. The method according to claim 22, wherein at least one first heating device and at least one second heating device operated via waste heat are connected in series in the circuit.

24. The method according to claim 18, 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.

25. The method according to claim 24, wherein the heat transfer medium is conveyed in the circuit in countercurrent to the flow of the reaction medium through the reactor.

26. The method according to claim 23, wherein the second heating device operated via waste heat is operated at least temporarily by energy obtained from the waste heat from a plant for producing vinyl chloride.

27. The method according to claim 18, wherein the thermal cleavage of the 1,2-dichloroethane is carried out in a temperature range from 200° C. to 400° C.

28. A plant for producing vinyl chloride by catalytic thermal cleavage of 1,2-dichloroethane, in which the heat required for preheating, evaporation, overheating and/or thermal cleavage of 1,2-dichloroethane is supplied via a liquid or condensing heat transfer medium, comprising at least one reactor in which the thermal cleavage takes place and at least one first heating device by which the reaction medium in the reactor is heated by the heat transfer medium, wherein the system further comprises at least one second heating device operated by waste heat from a plant for the incineration of liquid and/or gaseous residues of a chemical plant for heating the reaction medium.

29. The plant according to claim 28, wherein the reactor is integrated into a circuit of the heat transfer medium, wherein additionally at least the second heating device operated by waste heat is integrated into the circuit.

30. The plant according to claim 29, wherein at least one first heating device operated via a fuel and further at least one second heating device operated by waste heat are integrated into the circuit of the heat transfer medium.

31. The plant according to claim 29, 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 heating device operated by waste heat, and the reactor, wherein provisions are made for transferring heat from the heat transfer medium to a reaction medium flowing through the reactor.

32. The plant according to claim 29, wherein the first heating device operated via a fuel and the second heating device operated by waste heat are arranged in series or in parallel in the circuit of the heat transfer medium.

33. The plant according to claim 28, wherein the reactor comprises a tube bundle heat exchanger in which the tubes are filled with catalyst.

34. The plant according to claim 33, wherein the heat transfer medium flows through a jacket space of the reactor in a circuit.

35. The plant according to claim 28, wherein at least one device for preheating and/or evaporating and/or overheating of the 1,2-dichloroethane is integrated into the circuit of the heat transfer medium.

Description

[0048] Shown are:

[0049] FIG. 1 a schematically simplified plant scheme of a plant according to the invention for producing vinyl chloride by catalytic thermal cleavage from 1,2-dichloroethane.

[0050] Reference is made below to FIG. 1 and an exemplary embodiment variant of the method according to the invention is explained in more detail on the basis of this. The representation according to FIG. 1 is greatly simplified schematically and only those plant components are shown which are of importance in the context of the present invention. The plant comprises a reactor 1, to which a reactor inlet flow of 1,2-dichloroethane (EDC) is supplied, for example, via at least one line 2, which 1,2-dichloroethane is pyrolyzed in the reactor 1 under the action of heat to form monomeric vinyl chloride (VCM), wherein hydrogen chloride is formed in addition to the vinyl chloride. The named products of the method leave the reactor 1 in a reactor outlet flow 3.

[0051] The reactor 1 is integrated into a circuit flow 4 of a heat transfer medium such that heat is supplied to the reactor via the liquid heat transfer medium, for example, a heat transfer oil, which preferably flows in countercurrent to the reaction medium, in order to heat the reaction medium flowing through the reactor to a temperature of, for example, 300° C. to 400° C., at which the catalytic thermal cleavage of 1,2-dichloroethane to vinyl chloride takes place in reactor 1.

[0052] The circuit flow 4 of the heat transfer medium is explained in more detail below. The line circuit 4 of the heat transfer medium comprises a pump 5 to convey the heat transfer medium in the circuit, wherein this first flows through a first heating device 6 downstream of the pump 5, which first heating device is fired with a fossil fuel, for example, in order to heat the heat transfer medium. After that, the heat transfer medium 4 flows through a second heating device 7, in which the heat transfer medium, if the second heating device 7 is in operation, can be heated with the aid of thermal energy from the waste heat from a chemical plant, for example, from a plant for producing vinyl chloride.

[0053] In the embodiment, the first heating device 6 and the second heating device 7 are arranged one behind the other in the flow direction in the line system of the heat transfer medium circuit flow 4 and are thus connected in series. As an alternative to this, however, both heating devices can also be connected in parallel to one another, that is, different from what is shown in FIG. 1, the two heating devices are integrated into a line system such that the heat transfer medium can flow through at least only one of the two heating devices, bypassing the respective other heating device.

[0054] In the variant shown in FIG. 1, with the arrangement of both heating devices in series and also in the variant not shown with parallel connection, valves not shown in FIG. 1 can be provided to switch the heating devices on and off or to shut off the lines at suitable points in the line circuit 4. In addition, one or more regulating devices can be provided (also not shown in FIG. 1) in order to regulate the respective heat output supplied by the first and/or the second heating device according to the need for heating the reaction medium in the reactor 1.

[0055] A further variant, not shown in FIG. 1, comprises a device in which the reactor inlet flow 3 can be preheated, vaporized and overheated by means of the heat content of the flow 4, wherein these options do not necessarily have to be implemented, but can be implemented in any combination.

LIST OF REFERENCE NUMBERS

[0056] 1 reactor [0057] 2 reactor inlet flow [0058] 3 reactor outlet flow [0059] 4 heat carrier medium circuit flow [0060] 5 circulating pump [0061] 6 first heating device [0062] 7 second heating device operated via waste heat