CN206624829U - Catalytic reaction settler with afterburning function - Google Patents
Catalytic reaction settler with afterburning function Download PDFInfo
- Publication number
- CN206624829U CN206624829U CN201720390001.0U CN201720390001U CN206624829U CN 206624829 U CN206624829 U CN 206624829U CN 201720390001 U CN201720390001 U CN 201720390001U CN 206624829 U CN206624829 U CN 206624829U
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- China
- Prior art keywords
- settler
- afterburning
- stage casing
- catalyst
- pairs
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- 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.)
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Abstract
The utility model belongs to petrochemical equipment technical field, a kind of more particularly to catalytic reaction settler with afterburning function, including settler body, the lower end of settler body hypomere is provided with catalyst inlet and feed(raw material)inlet, settler body stage casing is internally provided with two kinds of baffle plates, the quantity of two kinds of baffle plates is identical and is arranged in pairs, at least two pairs of baffle plate, each pair of baffle plate vertically arranges, the bottom in settler body stage casing is provided with catalyst outlet, and settler body epimere is internally provided with primary cyclone and two-stage cyclone separator.The utility model has installed afterburning nozzle additional on the basis of existing technology, slurry oil caused by catalytic cracking unit can be made full use of, slurry oil is adsorbed in the catalyst by the flowing of settler stripping section catalyst, part slurry oil vaporization, big portion, which is streamed to regenerator and burnt, becomes heat, the steam exhaling amount of device is improved, positive effect is served to the trans-utilization of slurry oil.
Description
Technical field
The utility model belongs to petrochemical equipment technical field, more particularly to a kind of catalytic reaction with afterburning function
Settler.
Background technology
During petrochemical iy produced, settler is a kind of production equipment indispensable in catalytic cracking production process, in production
Commonly use it and carry out the separation of catalyst sedimentation and oil and gas.The catalyst of appropriate height is filled with settler.Existing settler
Inside generally it is arranged on by the various stripper plants of stripping section in device, oil and gas sedimentation separation in settler, catalyst two-phase transportation
To regenerator.Without installation afterburning nozzle, this sedimentation has 2 points of deficiencies:Slurry oil caused by one side catalytic unit only has
By getting rid of outside and without good utilization means;On the other hand the quantity of steam deficiency that existing catalytic unit needs will also pass through device
Guarantee plant running is attracted outside, adds the energy consumption of device.
The content of the invention
The utility model provides a kind of catalytic reaction settler with afterburning function, to solve to carry in above-mentioned background technology
The problem of going out.
The technical problem that the utility model solves is realized using following technical scheme:The utility model provides a kind of tool
There are the catalytic reaction settler of afterburning function, including settler body, the lower end of settler body hypomere is provided with catalyst and entered
Mouthful and feed(raw material)inlet, settler body stage casing be internally provided with ring baffle and conical baffled two kinds of baffle plates, two kinds of baffle plates
Quantity is identical and is arranged in pairs, and at least two pairs of baffle plate, each pair of baffle plate vertically arranges, the bottom in settler body stage casing
It is provided with catalyst outlet, settler body epimere is internally provided with primary cyclone and two-stage cyclone separator, and one
Level cyclone separator and two-stage cyclone separator are connected, and oil and gas outlet is provided with the top of settler body epimere, and described is heavy
Afterburning nozzle is provided with the side wall in drop device body stage casing, slurry oil is injected the inside in settler body stage casing, institute by afterburning nozzle
A stripped vapor distributor is provided with below the baffle plate stated, steam enters settler body stage casing by stripped vapor distributor
Inside.
Described baffle plate shares three pairs, and the port of export of described afterburning nozzle is located at the space between two pairs of baffle plates of downside
Place.At least two, described afterburning nozzle, each afterburning nozzle are evenly distributed on around settler this body sidewall.
The beneficial effects of the utility model are:The utility model has installed afterburning nozzle, energy additional on the basis of existing technology
It is enough that slurry oil caused by catalytic cracking unit is made full use of, slurry oil is adsorbed by the flowing of settler stripping section catalyst
In the catalyst, part slurry oil vaporizes, and big portion, which is streamed to regenerator and burnt, becomes heat, the steam exhaling amount of device is improved, to oil
The trans-utilization of slurry serves positive effect.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
In figure:1- oil and gas exports, 2- ring baffles, 3- afterburning nozzles, 4- stripped vapor distributors, 5- raw material nozzles, 6-
Primary cyclone, 7- catalyst inlets, 8- catalyst outlets, 9- is conical baffled, 10- two-stage cyclone separators.
Embodiment
The utility model is described further below in conjunction with accompanying drawing:
The present embodiment includes settler body, and the lower end of settler body hypomere is provided with catalyst inlet 7 and raw material enters
Mouth 5, catalyst and raw material enter in settler body by catalyst inlet 7 and feed(raw material)inlet 5 respectively, and under stripping effect
It is delivered up into primary cyclone 6.
Settler body stage casing is internally provided with ring baffle 2 and conical baffled 9 two kinds of baffle plates, the quantity of two kinds of baffle plates
Identical and be arranged in pairs, at least two pairs of baffle plate, each pair of baffle plate vertically arranges.The effect of baffle plate is to stop catalyst,
It is up under stripping effect farthest to limit it.
The bottom in settler body stage casing is provided with catalyst outlet 8.The catalysis reacted the coke of generation and isolated
Agent powder is discharged by catalyst outlet 8.
Settler body epimere is internally provided with primary cyclone 6 and two-stage cyclone separator 10, one-level eddy flow
Separator 6 and two-stage cyclone separator 10 are connected, and oil and gas outlet 1 is provided with the top of settler body epimere.
Afterburning nozzle 3 is provided with the side wall in described settler body stage casing, slurry oil injects settler by afterburning nozzle 3
The inside in body stage casing.Afterburning nozzle 3, slurry oil caused by catalytic cracking unit can be made full use of, pass through settler
The flowing of stripping section catalyst adsorbs slurry oil in the catalyst, and the vaporization of part slurry oil, big portion, which is streamed to regenerator and burnt, to be become
Heat, the steam exhaling amount of device is improved, positive effect is served to the trans-utilization of slurry oil.
A stripped vapor distributor 4 is provided with below described baffle plate, it is heavy that steam is entered by stripped vapor distributor 4
The inside in device body stage casing drops.Steam is introduced back into settler body by stripped vapor distributor 4, a promotion can be entered
The generation of coke.
Described baffle plate shares three pairs, and the port of export of described afterburning nozzle 3 is located at the sky between two pairs of baffle plates of downside
At gap.At least two, described afterburning nozzle 3, each afterburning nozzle 3 are evenly distributed on around settler this body sidewall.
Claims (3)
1. a kind of catalytic reaction settler with afterburning function, including settler body, the lower end of settler body hypomere are set
Catalyst inlet (7) and feed(raw material)inlet (5) are equipped with, settler body stage casing is internally provided with ring baffle (2) and taper gear
(9) two kinds of baffle plates of plate, the quantity of two kinds of baffle plates is identical and is arranged in pairs, and at least two pairs of baffle plate, each pair of baffle plate is vertically
Arrangement, the bottom in settler body stage casing are provided with catalyst outlet (8), and settler body epimere is internally provided with one-level rotation
Stream separator (6) and two-stage cyclone separator (10), primary cyclone (6) and two-stage cyclone separator (10) series connection, sink
Oil and gas outlet (1) is provided with the top of drop device body epimere, it is characterised in that:Set in the side wall in described settler body stage casing
Afterburning nozzle (3) is equipped with, slurry oil is injected the inside in settler body stage casing by afterburning nozzle (3), set below described baffle plate
A stripped vapor distributor (4) is equipped with, steam is entered the inside in settler body stage casing by stripped vapor distributor (4).
A kind of 2. catalytic reaction settler with afterburning function according to claim 1, it is characterised in that:Described gear
Plate shares three pairs, and the port of export of described afterburning nozzle (3) is located at the gap between two pairs of baffle plates of downside.
A kind of 3. catalytic reaction settler with afterburning function according to claim 1, it is characterised in that:Described benefit
Fire nozzle (3) at least two, each afterburning nozzle (3) is evenly distributed on around settler this body sidewall.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720390001.0U CN206624829U (en) | 2017-04-13 | 2017-04-13 | Catalytic reaction settler with afterburning function |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720390001.0U CN206624829U (en) | 2017-04-13 | 2017-04-13 | Catalytic reaction settler with afterburning function |
Publications (1)
Publication Number | Publication Date |
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CN206624829U true CN206624829U (en) | 2017-11-10 |
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Family Applications (1)
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CN201720390001.0U Expired - Fee Related CN206624829U (en) | 2017-04-13 | 2017-04-13 | Catalytic reaction settler with afterburning function |
Country Status (1)
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CN (1) | CN206624829U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110614072A (en) * | 2018-06-20 | 2019-12-27 | 中国石化工程建设有限公司 | Catalytic cracking reactor and catalytic cracking method |
CN116212971A (en) * | 2021-12-03 | 2023-06-06 | 中国石油化工股份有限公司 | Catalyst regeneration equipment and regeneration method |
-
2017
- 2017-04-13 CN CN201720390001.0U patent/CN206624829U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110614072A (en) * | 2018-06-20 | 2019-12-27 | 中国石化工程建设有限公司 | Catalytic cracking reactor and catalytic cracking method |
CN116212971A (en) * | 2021-12-03 | 2023-06-06 | 中国石油化工股份有限公司 | Catalyst regeneration equipment and regeneration method |
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Legal Events
Date | Code | Title | Description |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171110 |
|
CF01 | Termination of patent right due to non-payment of annual fee |