Process and apparatus for the pyrolysis of hydrocarbon gas

Abstract

A hydrocarbon gas to be decomposed, optionally mixed with water vapor, is allowed to flow through the gap between various porous tubes 4 constituting a group of porous tubes provided extending vertically in a decomposition reaction column 1 while air or oxygen is jetted homogeneously from the interior to the exterior of the porous tubes in the direction perpendicular to the stream of the hydrocarbon gas to be decomposed, optionally mixed with water vapor. The mixture is then ignited to form a diffusion flame layer B on the outer surface of the porous tubes 4. With the diffusion flame layer as a heat source, the hydrocarbon gas to be decomposed, optionally mixed with water vapor, undergoes pyrolysis.

Description

BACKGROUND OF INVENTION

[0001] 1. Field of Invention

[0002] The present invention relates to a process for pyrolyzing a hydrocarbon gas, optionally mixed with water vapor, to produce an olefin-based organic compound or a synthetic gas containing hydrogen or an olefin-based organic compound and an apparatus therefor.

[0003] 2. Related Art

[0004] In order to produce a desired olefin-based organic compound (ethylene, acetylene, propylene, butene, etc.) from a paraffinic organic compound, it has heretofore been normally practiced to decompose a paraffinic organic compound having a long-chain chemical composition to an olefinic organic compound having a short-chain chemical composition through a pyrolysis apparatus.

[0005] As the foregoing pyrolysis apparatus there has been mainly used a type of pyrolysis apparatus arranged such that a gaseous paraffinic organic compound and water vapor are allowed to flow through a tube in a heating oven, whereby the tube is externally heated so that naphtha is pyrolyzed to produce an olefin-based organic compound.

[0006] Further, the olefin-based organic compound produced in the pyrolysis apparatus is transferred from the pyrolysis apparatus to a rapid cooling apparatus to be rapidly cooled therein.

[0007] The process to be conducted in the conventional pyrolysis apparatus requires heating to high temperature (from about 700° C. to 900° C.), unavoidably causing the rise in the facility cost and the caulking of the interior of tube. In order to inhibit caulking, it is necessary that water vapor be allowed to flow through the tube together with the paraffinic organic compound.

[0008] Further, in the conventional equipment, the pyrolysis apparatus and the rapidly cooling apparatus are separately provided from each other. Thus, the equipment becomes to intricate, and in order to start the rapidly cooling apparatus, there is required the time of period from the pyrolysis a hydrocarbon gas, optionally mixed with water vapor.

SUMMARY OF INVENTION

[0009] An object of the invention is to provide a process for the pyrolysis of a hydrocarbon gas which requires no high temperature heating and thus can be effected at a reduced facility cost and undergoes no caulking and an apparatus therefor.

[0010] Another object of the present invention is to provide an apparatus for the pyrolysis of a hydrocarbon gas for rapidly cooling the pyrolyzed gas to reduce the equipment cost and to increase a yielding ratio of useful gas.

[0011] In accordance with the invention, the foregoing object can be accomplished as follows. In other words, a hydrocarbon gas to be decomposed, optionally mixed with water vapor, is allowed to come in direct contact with air or oxygen to form a diffusion flame layer. The hydrocarbon gas is then allowed to undergo radical reaction with the diffusion flame layer as a heat source to produce an olefinic organic compound gas or a synthetic gas containing an olefinic organic compound.

[0012] In order to form the foregoing diffusion flame layer, a hydrocarbon gas to be decomposed, optionally mixed with water vapor, is allowed to flow uniformly through the gap between various porous tubes constituting a group of porous tubes extending vertically in a decomposition reaction column. Air or oxygen is then homogeneously jetted from the interior to the exterior of the porous tubes in the direction perpendicular to a stream of the hydrocarbon gas to be decomposed, optionally mixed with water vapor. The hydrocarbon gas to be decomposed, optionally mixed with water vapor, is then ignited to form a diffusion flame layer on the outer surface of the porous tubes. Alternatively, air or oxygen is allowed to flow uniformly through the gap between various porous tubes constituting a group of porous tubes extending vertically in a decomposition reaction column. A hydrocabon gas to be decomposed, optionally mixed water vapor, supplied into the porous tubes. Air or oxygen is then homogeneously jetted from the exterior to the interior of the porous tubes in the direction perpendicular to a stream of a hydrocarbon gas to be decomposed, optionally mixed with water vapor.

[0013] Further, according to the present invention, the apparatus is provided with a gas rapidly cooing device adjacent to the pyrolysis portion having the porous tubes.

BRIEF DESCRIPTION OF DRAWINGS

[0014] FIG. 1 is a diagram illustrating the concept of the apparatus for the pyrolysis of a hydrocarbon gas according to the first example of the invention.

[0015] FIG. 2 is an enlarged view of Portion A of FIGS. 1 and 3.

[0016] FIG. 3 is a diagram illustrating the concept of the apparatus for the pyrolysis of a hydrocarbon gas, optionally mixed with water vapor, according to the second example of the invention.

[0017] FIG. 4 is a partially sectional enlarged view of the double tube portion of FIG. 3.

[0018] FIG. 5 is a diagram illustrating the solid starting material gasification apparatus connected to the pyrolysis apparatus according to the invention.

[0019] FIG. 6 is a diagram illustrating the concept of the apparatus for the pyrolysis of a hydrocarbon gas with a gas rapidly cooling column according to the third example of the invention.

[0020] FIG. 7 is a plan view of a gas rapidly cooling portion of apparatus for pyrolysis of a hydrocarbon gas shown in FIG. 6.

DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS

[0021] Modes for carrying out the invention will be described hereinafter with reference to the following examples in connection with the drawings.

[0022] First Embodiment

[0023] FIG. 1 is a diagram illustrating the concept of an apparatus for the pyrolysis of a hydrocarbon gas according to the first example of the invention. In this diagram, the reference numeral 1 indicates a decomposition reaction column comprising a diffuser 2 provided at the upper portion thereof and a reducer 3 provided at the lower portion thereof. Provided extending vertically in the decomposition reaction column 1 are a group of porous tubes. The reaction column may be cylindrical or prismatic.

[0024] The various porous tubes constituting the foregoing group of porous tubes are each made of a porous metal or a metal film material having a pore size of the order of MF (microfiltration) or UF (ultrafiltration). As the porous metal or metal film material there may be used SUS, tool steel, inconnel, titanium alloy, aluminum alloy or the like.

[0025] The various porous tubes 4 are each blocked at the upper end thereof and connected to the header 5 at the lower end thereof. The header 5 is a hollow plate. Provided protruding from the upper surface of the header 5 are non-porous tubes 7 which are connected to the foregoing porous tubes 4 with a joint 6, respectively.

[0026] Provided at the lower end of the diffuser 2 and above the group of porous tubes is a distributor 8. Provided in the gap between the outer surface of the upper portion of the various porous tubes 4 is an ignition system 9.

[0027] The diffuser 2 is provided with an inlet 2a through which a hydrocarbon gas to be decomposed such as paraffin gas, optionally mixed with water vapor, is supplied into the decomposition reaction column 1. The reducer 3 is provided with an outlet 3a through which a gas such as olefinic gas obtained by decomposition and purification is discharged out of the decomposition reaction column 1. The header 5 is provided with a nozzle 5a through which air or oxygen is supplied into the decomposition reaction column 1.

[0028] The operation of the decomposition reaction column 1 will be described hereinafter.

[0029] A hydrocarbon gas to be decomposed, optionally mixed with water vapor, is supplied into the decomposition reaction column 1 through the inlet 2a, rectified through the distributor, and then allowed to flow downward from the upper portion of the reaction column 1 uniformly through the gap between the various porous tubes 4.

[0030] Separately, air or oxygen which has been supplied into the reaction column 1 through the supply nozzle 5a is then jetted homogeneously out of the porous tubes through the pores in the porous metal material in the direction perpendicular to the stream of the hydrocarbon gas to be decomposed, optionally mixed with water vapor, due to the difference in pressure between inside and outside the porous tubes.

[0031] When the gaseous mixture is ignited by the ignition system 9 under these conditions, a diffusion flame layer B is then formed on the outer surface of the porous tubes 4 as shown in FIG. 2. With this diffusion flame layer as a heat source, the hydrocarbon gas to be decomposed, such as paraffinic gas, optionally mixed with water vapor, undergoes radical reaction (free radical reaction) to produce a gaseous olefinic organic compound having a shorter chain chemical composition or a synthetic gas containing hydrogen, methane, carbon monoxide and a gaseous olefinic organic compound having a shorter chain chemical composition.

[0032] Second Embodiment

[0033] FIG. 3 is a diagram illustrating the concept of an apparatus for the pyrolysis of a hydrocarbon gas according to the second example of the invention. Since the present example differs from the first example only in that non-porous tubes 10 are provided concentrically of the porous tubes 4 surrounding the periphery of the porous tubes 4, respectively, with a gap interposed therebetween, the description of other structures will be omitted. In some detail, as shown in FIG. 4, air is allowed to flow through the inner tube of a double tube consisting of the porous tube 4 as an inner tube and the non-porous tube 10 as an outer tube while a hydrocarbon gas to be decomposed, optionally mixed with water vapor, is allowed the flow space (double tube portion) defined by the inner tube and the outer tube, whereby the hydrocarbon gas to be decomposed undergoes radical reaction as in the first example to produce a gaseous olefinic organic compound having a shorter chain chemical composition or a synthetic gas containing hydrogen, methane, carbon monoxide and a gaseous olefinic organic compound having a shorter chain chemical composition.

[0034] In accordance with the foregoing example, air or oxygen is allowed to flow from the interior of the porous tubes 4 to the exterior of the porous tubes 4 while a hydrocarbon gas to be decomposed, optionally mixed water vapor, is allowed to flow along the exterior of the porous tubes 4. However, a hydrocarbon gas to be decomposed, optionally mixed with water vapor, is allowed to flow the interior of the porous tubes 4 while air or oxygen may be allowed to flow from the exterior of the porous tube 4 to the interior of the porous tubes 4.

[0035] Further, in accordance with the foregoing example, a hydrocarbon gas to be decomposed, optionally mixed with water vapor, is supplied into the decomposition reaction column 1. As shown in FIG. 5, however, a gas produced by a process which comprises supplying a solid starting material such as waste plastic into a gasification apparatus 11 where it is then heated by a heating device 13 to decompose to a gas and a residue, and decomposed gas may be applied into the reaction column 1 through the inlet 2a.

[0036] Moreover, in accordance with the foregoing example, the decomposition reaction column 1 is provided with the inlet 2a at the upper portion thereof and the outlet 3a at the lower portion thereof. However, the decomposition reaction column 1 may be provided with the inlet 2a at the lower portion thereof and the outlet 3a at the upper portion thereof.

[0037] Third Embodiment

[0038] FIG. 1 is a diagram illustrating the concept of an apparatus for the pyrolysis of a hydrocarbon gas according to the first example of the invention. In this embodiment, there an upper portion of reaction column is the same as the structure described in the first embodiment, and an lower portion corresponds to a gas rapidly cooling column 100 for the pyrolyzed gas produced in the upper portion. Coolant spraying tubes 14 are arranged along with an inner peripheral portion of the gas rapidly cooling column 100.

[0039] The operation of this device will be described hereinafter.

[0040] The pyrolyzed gas produced in the reaction column as shown in FIG. 1 is transferred directly from the reaction column 1 to the gas rapidly cooling column 100. A coolant sprays from a silt or a spraying hole provided on the coolant spray tubes 14 toward the gas flow path in such a manner that the coolant sprays slantly with respect to the center of a gas cooling portion to occur the spiral air flow in the gas rapidly cooling portion, The coolant spray tubes 14 are arranged in the gas rapidly cooling column 100 to rapidly cool the gas produced in the upper portion of reaction column 1.

[0041] Unlike the foregoing conventional decomposition process and apparatus, the pyrolysis process and apparatus according to the invention is characterized by a process which comprises allowing a hydrocarbon gas obtained by the evaporation of naphtha or the like, optionally mixed with water vapor, to come in direct contact with air or oxygen to form a diffusion flame layer, and then allowing the mixture to undergo radical reaction with the diffusion flame layer as a heat source. By using the process and apparatus of the invention, a desired olefin-based organic compound gas or a synthetic gas containing hydrogen, methane, carbon monoxide and an olefin-based organic compound gas having a short chain chemical composition can be produced without a high temperature and pressure process, making it possible to reduce the facility cost and avoid caulking.

[0042] Further, in use of a radical reaction, after radical reaction, the reacted gas is rapidly cooled to increase yield of the synthetic gas to be desired.

Claims

1. A process for pyrolyzing a hydrocarbon gas, comprising the steps of: coming a hydrocarbon gas in direct contact with air or oxygen to form a diffusion flame layer; and processing said hydrocarbon gas through radical reaction with said diffusion flame layer serving as a heat source to produce an olefin-based organic compound gas.

2. A process for pyrolyzing a hydrocarbon gas comprising the steps of: supplying water vapor with a hydrocarbon gas; coming the mixture of water vapor and the hydrocarbon gas in direct contact with air or oxygen to form a diffusion flame layer; and processing said hydrocarbon gas through radical reaction with said diffusion flame layer as a heat source to produce a synthetic gas containing hydrogen, methane, carbon monoxide and an olefin-based organic compound gas.

3. The process for pyrolyzing a hydrocarbon gas according to claim 1, further comprising: flowing a hydrocarbon gas, optionally mixed with water vapor, uniformly through the gap between various porous tubes including a group of porous tubes extending vertically in a pyrolysis reaction column; homogeneously jetting air or oxygen from the interior to the exterior of said porous tubes in the direction perpendicular to a stream of said hydrocarbon gas, optionally mixed with water vapor; and igniting said stream to form a diffusion flame layer on the outer surface of said porous tubes.

4. The process for pyrolyzing a hydrocarbon gas according to claim 2, further comprising: flowing a hydrocarbon gas, optionally mixed with water vapor, uniformly through the gap between various porous tubes including a group of porous tubes extending vertically in a pyrolysis reaction column; homogeneously jetting air or oxygen from the interior to the exterior of said porous tubes in the direction perpendicular to a stream of said hydrocarbon gas, optionally mixed with water vapor; and igniting said stream to form a diffusion flame layer on the outer surface of said porous tubes.

5. The process for pyrolyzing a hydrocarbon gas according to claim 1, further comprising the steps of: flowing a hydrocarbon gas to be decomposed, optionally mixed with water vapor in the porous tubes jetting air or oxygen from an exterior of the porous tubes to an interior of the porous tubes in a direction orthogonal to a flow of the hydrocarbon gas; and igniting said stream to form a diffusion flame layer on the outer surface of said porous tubes.

6. The process for pyrolyzing of a hydrocarbon gas according to claim 2, further comprising the steps of: flowing a hydrocarbon gas to be decomposed, optionally mixed with water vapor in the porous tubes jetting air or oxygen from an exterior of the porous tubes to an interior of the porous tubes in a direction orthogonal to a flow of the hydrocarbon gas; and igniting said stream to form a diffusion flame layer on the outer surface of said porous tubes.

7. The process for pyrolyzing a hydrocarbon gas according to claim 1, wherein said hydrocarbon gas is replaced by a synthetic gas obtained by the pyrolysis of waste plastic.

8. The process for pyrolyzing a hydrocarbon gas according to claim 2, wherein said hydrocarbon gas is replaced by a synthetic gas obtained by the pyrolysis of waste plastic.

9. The process for pyrolyzing a hydrocarbon gas according to claim 3, wherein said hydrocarbon gas is replaced by a synthetic gas obtained by the pyrolysis of waste plastic.

10. The process for pyrolyzing a hydrocarbon gas according to claim 4, wherein said hydrocarbon gas is replaced by a synthetic gas obtained by the pyrolysis of waste plastic.

11. The process for pyrolyzing a hydrocarbon gas according to claim 5, wherein said hydrocarbon gas is replaced by a synthetic gas obtained by the pyrolysis of waste plastic.

12. The process for pyrolyzing a hydrocarbon gas according to claim 6, wherein said hydrocarbon gas is replaced by a synthetic gas obtained by the pyrolysis of waste plastic.

13. An apparatus for pyrolyzing a hydrocarbon gas comprising: a decomposition reaction column having an inlet provided at one end thereof through which a hydrocarbon gas, optionally mixed with water vapor, is supplied thereinto; an outlet provided at the other thereof through which an olefin-based organic compound gas produced is discharged; a group of porous tubes extending vertically in said reaction column; a header connected to said porous tubes for supplying air or oxygen;

14. An apparatus for pyrolyzing a hydrocarbon gas comprising: a decomposition reaction column having an inlet provided at one end thereof through which air or oxygen is supplied thereinto; an outlet provided at the other thereof through which an olefin-based organic compound gas produced is discharged; a group of porous tubes extending vertically in said reaction column and a header connected to said porous tubes for supplying a hydrocarbon gas, optionally mixed with water vapor.

15. The apparatus for pyrolyzing a hydrocarbon gas according to claim 13, wherein a non-porous tube is provided concentrically of said porous tubes surrounding the periphery of said porous tubes.

16. The apparatus for pyrolyzing a hydrocarbon gas according to claim 14, wherein a non-porous tube is provided concentrically of said porous tubes surrounding the periphery of said porous tubes.

17. The apparatus for pyrolyzing a hydrocarbon gas according to claim 13, wherein a distributor is provided at the inlet side of said decomposition reaction column.

18. The apparatus for pyrolyzing a hydrocarbon gas according to claim 14, wherein a distributor is provided at the inlet side of said decomposition reaction column.

19. The apparatus for pyrolyzing a hydrocarbon gas according to claim 15, wherein a distributor is provided at the inlet side of said decomposition reaction column.

20. The apparatus for pyrolyzing a hydrocarbon gas according to claim 16, wherein a distributor is provided at the inlet side of said decomposition reaction column.

21. The process for pyrolyzing a hydrocarbon gas according to claim 13, wherein said hydrocarbon gas is replaced by a synthetic gas obtained by the pyrolysis of waste plastic.

22. The process for pyrolyzing a hydrocarbon gas according to claim 14, wherein said hydrocarbon gas is replaced by a synthetic gas obtained by the pyrolysis of waste plastic.

23. The process for pyrolyzing a hydrocarbon gas according to claim 15, wherein said hydrocarbon gas is replaced by a synthetic gas obtained by the pyrolysis of waste plastic.

24. The process for pyrolyzing a hydrocarbon gas according to claim 16, wherein said hydrocarbon gas is replaced by a synthetic gas obtained by the pyrolysis of waste plastic.

25. The process for pyrolyzing a hydrocarbon gas according to claim 17, wherein said hydrocarbon gas is replaced by a synthetic gas obtained by the pyrolysis of waste plastic.

26. The process for pyrolyzing a hydrocarbon gas according to claims 18, wherein said hydrocarbon gas is replaced by a synthetic gas obtained by the pyrolysis of waste plastic.

27. The process for pyrolyzing a hydrocarbon gas according to claim 19, wherein said hydrocarbon gas is replaced by a synthetic gas obtained by the pyrolysis of waste plastic.

28. The process for pyrolyzing a hydrocarbon gas according to any one of claim 20, wherein said hydrocarbon gas is replaced by a synthetic gas obtained by the pyrolysis of waste plastic.

29. The apparatus for pyrolyzing a hydrocarbon gas according to claim 13 further comprising: gas cooling portion for rapidly cooling the pyrolyzed gas, said gas cooling portion directly connected to said decomposition reaction column.

30. The apparatus for pyrolyzing a hydrocarbon gas according to claim 14 further comprising: gas cooling portion for rapidly cooling the pyrolyzed gas, said gas cooling portion directly connected to said decomposition reaction column.

31. The apparatus for pyrolyzing a hydrocarbon gas according to claim 15 further comprising: gas cooling portion for rapidly cooling the pyrolyzed gas, said gas cooling portion directly connected to said decomposition reaction column.

32. The apparatus for pyrolyzing a hydrocarbon gas according to claim 16 further comprising: gas cooling portion for rapidly cooling the pyrolyzed gas, said gas cooling portion directly connected to said decomposition reaction column.

33. The apparatus for pyrolyzing a hydrocarbon gas according to claim 17 further comprising: gas cooling portion for rapidly cooling the pyrolyzed gas, said gas cooling portion directly connected to said decomposition reaction column.

34. The apparatus for pyrolyzing a hydrocarbon gas according to claim 18 further comprising: gas cooling portion for rapidly cooling the pyrolyzed gas, said gas cooling portion directly connected to said decomposition reaction column.

35. The apparatus for pyrolyzing a hydrocarbon gas according to claim 19 further comprising: gas cooling portion for rapidly cooling the pyrolyzed gas, said gas cooling portion directly connected to said decomposition reaction column.

36. The apparatus for pyrolyzing a hydrocarbon gas according to claim 20 further comprising: gas cooling portion for rapidly cooling the pyrolyzed gas, said gas cooling portion directly connected to said decomposition reaction column.