Termination device of a reactor of a fluid catalytic cracking unit
10099190 ยท 2018-10-16
Assignee
Inventors
Cpc classification
B01D45/16
PERFORMING OPERATIONS; TRANSPORTING
C04B2235/5228
CHEMISTRY; METALLURGY
C04B2235/48
CHEMISTRY; METALLURGY
B01J8/0065
PERFORMING OPERATIONS; TRANSPORTING
C04B2235/6028
CHEMISTRY; METALLURGY
C04B2235/5232
CHEMISTRY; METALLURGY
B01J2208/06
PERFORMING OPERATIONS; TRANSPORTING
C04B35/80
CHEMISTRY; METALLURGY
C04B2235/614
CHEMISTRY; METALLURGY
C04B35/62218
CHEMISTRY; METALLURGY
B01J19/02
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01J8/00
PERFORMING OPERATIONS; TRANSPORTING
B01J19/02
PERFORMING OPERATIONS; TRANSPORTING
C04B35/80
CHEMISTRY; METALLURGY
B01D45/16
PERFORMING OPERATIONS; TRANSPORTING
C04B35/628
CHEMISTRY; METALLURGY
Abstract
The invention relates to a termination device of a tubular reactor comprising at least one separation element adapted for the separation of solid particles and gaseous effluents and at least one coupling element that is part of an end of said tubular reactor, said separation element being connected to said coupling element, characterized in that each element of the termination device is made of ceramic material. The invention also relates to a tubular reactor, having a vertical or substantially vertical axis, of a fluid catalytic cracking unit equipped with a termination device according to the invention and to a corresponding fluid catalytic cracking unit.
Claims
1. A termination device of a tubular reactor comprising: at least one separation element adapted for the separation of solid particles and gaseous effluents and at least one coupling element that is part of an end of the tubular reactor, the separation element being connected to the coupling element, characterized in that each element of the termination device is made of ceramic material and the ceramic material comprises a ceramic matrix selected from silicon carbide SiC, boron carbide B.sub.4C, silicon nitride Si.sub.3N.sub.4, aluminium nitride AlN, boron nitride BN, alumina Al.sub.2O.sub.3, or mixtures thereof, incorporated in which ceramic matrix are carbon fibres or ceramic fibres.
2. The termination device according to claim 1, characterized in that the ceramic fibres are selected from the group consisting of crystalline alumina fibres, mullite fibres, crystalline or amorphous silicon carbide fibres, zirconia fibres, silica-alumina fibres, and mixtures thereof.
3. The termination device according to claim 1, characterized in that the ceramic material is a sintered ceramic material.
4. The termination device according to claim 1, characterized in that the ceramic material is a Ceramic Matrix Composite (CMC).
5. The termination device according to claim 1, characterized in that the elements form one and the same part made of ceramic material.
6. The termination device according to claim 1, characterized in that the elements are separate elements made of ceramic material that are assembled together, an element being made of one part or of several portions assembled together.
7. The termination device according to claim 6, characterized in that the elements and/or the portions are assembled by welding or brazing or in that elements to be assembled and/or portions to be assembled have ends shaped in order to be assembled by interlocking or screwing.
8. The termination device according to claim 1, characterized in that the coupling element comprises a bent pipe, in particular a rounded bent pipe, or a straight pipe.
9. The termination device according to claim 1, characterized in that the separation element is selected from the group consisting of a cyclone, a circulation separation element and a ballistic separation element.
10. A tubular reactor having a vertical or substantially vertical axis, of a fluid catalytic cracking unit equipped with at least one termination device according to claim 1.
11. The tubular reactor according to claim 10 made of metal, characterized in that the reactor is connected to the termination device by fastening means suitable for absorbing a difference in expansion between the metal of the reactor and the ceramic material of the termination device.
12. The tubular reactor according to claim 10, characterized in that the tubular reactor is made of ceramic material and is connected to the termination device by welding, brazing, screwing or interlocking.
13. A catalytic cracking unit comprising at least one tubular reactor according to claim 10.
14. A method of preparation of a termination device of a tubular reactor, wherein each element of the termination device is made of Ceramic Matrix Composite (CMC), the method comprising: 1) shaping a fibrous ceramic material over a supporting material that could be removed without excessive effort, in order to obtain a fibrous shape that can be assimilated to the backbone of the final element to be obtained, in the presence of a first resin, 2) coating the shape obtained at step (1) with finely divided ceramic powder and at least a second resin, in the presence of finely divided carbon powder, to obtain a coated shape, 3) repeat steps (1) and (2), 4) heating the coated shape of step (2) or (3) under vacuum and/or under inert atmosphere in order to transform the resins of step (1), (2) and (3) into a carbon-rich structure, essentially deprived of other elements to obtain a carbon-rich coated shape, 5) introducing a gas within the carbon-rich coated shape of step (4) under conditions efficient to transform the carbon-rich structure into carbide containing carbon-rich structure, 6) removing the supporting material of step (1), when present, wherein carbon fibers are present at least at step (1), (2) and/or (3) within the fibrous ceramic material, within the finely divided ceramic powder, within the finely divided carbon powder, and/or within the first and/or second resin.
Description
(1) The invention is now described with reference to the appended, non-limiting drawings, in which:
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(10) The termination device according to the invention is made of ceramic material, preferably silicon carbide SiC. It is for example formed by injection moulding or extrusion. Injection moulding or extrusion are conventionally carried out using ceramic powders or precursors of ceramics with a binder. According to another manufacturing method, the ceramic termination device is formed by compression and heating of a ceramic powder, it being possible for the compression to be maintained during the heating step, the heating step being a step of sintering the ceramic powder. This technique is particularly well suited to the manufacture of solid elements made of silicon carbide according to the invention. The ceramic powder used optionally comprises ceramic fibres in order to increase the mechanical strength of the parts produced. The ceramic fibres, when they are present, generally represent from 0.1% to 10% by weight of the part produced.
(11) This termination device may be arranged according to any one of the termination devices known in the prior art.
(12) Some of these termination devices are described with reference to
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(14) Other reactor termination devices exist that have in particular more complex configurations but that provide a better separation efficiency.
(15) In the same way as in the preceding example, the reactor 1 may be made of metal or equally made of ceramic material.
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(18) The lower end of smaller diameter of this conical lower portion 101b is connected to the particle outlet duct 104, which is in the form of a tube extending in the axis of symmetry X of the separation chamber 101. This tube is often referred to as a dip-leg or else leg.
(19) The inlet duct 102 receiving the gas/particle mixture, sometimes also referred to as suction eye or bell mouth, is formed of a tube positioned so as to impart a circular movement to the incoming mixture. Thus, the inlet duct 102 may either be tangential with respect to the separation chamber 101, as represented schematically in
(20) Under the effect of this movement, the catalyst particles fall into the conical lower portion 101b of the separation chamber 101 before being discharged through the particle outlet duct 104. The gas itself exits at the upper end of the cyclone via the gas outlet duct 103, also referred to as a stack. A dust catcher 105 may be positioned between the conical lower portion 101b of the separation chamber 101 and the particle outlet duct 104.
(21) The circulation of the gas inside the cyclone is represented by the arrows visible in
(22) The separation element 41 may be made from one or more parts made of ceramic material.
(23) For example, the separation chamber 101 and the particle outlet duct 104 may be separate parts, it being possible for the inlet duct 102 and the gas outlet duct 103 to be made from one part with the separation chamber 101.
(24) The elements 101 and 104 may then be interlocked, as represented schematically in
(25) Assembly operations similar to those described with reference to
(26) The coupling element 12 of the termination device 40 is connected directly to the tubular reactor 1, as represented schematically in
(27) According to one embodiment that is not represented, the invention is also wholly applicable to a termination device of RS2 type as disclosed in EP 1 017 762 or U.S. Pat. No. 6,296,812, the content of which is incorporated here by way of reference.