CN1511627A - Gas-solid cyclone combination fast separation device for lifting pipe - Google Patents
Gas-solid cyclone combination fast separation device for lifting pipe Download PDFInfo
- Publication number
- CN1511627A CN1511627A CNA021594074A CN02159407A CN1511627A CN 1511627 A CN1511627 A CN 1511627A CN A021594074 A CNA021594074 A CN A021594074A CN 02159407 A CN02159407 A CN 02159407A CN 1511627 A CN1511627 A CN 1511627A
- Authority
- CN
- China
- Prior art keywords
- riser
- seal bootr
- gas
- tube
- shunting
- Prior art date
- 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.)
- Granted
Links
Images
Landscapes
- Cyclones (AREA)
Abstract
The present invention relates to combined cyclonic gas-solid separation riser tube apparatus and relates to the fast and efficient separation between the catalyst and oil gas in catalytically cracking riser tube reaction system. The apparatus includes riser tube, conic gas stripping baffle, separating tube, fast cyclonic separating head, separating baffle, auxiliary cyclone, gas stripping tube and closing hood. The fast cyclonic separating head consists of 3-5 downward tangential bending tubes. The auxiliary cyclone has closed top and side wall with several tangential slots. After the mixture of catalyst and oil gas is sprayed along bending tubes, most of the catalyst rotates and descends along the inner wall of the closed hood owing to the centrifugal force, while oil gas and small amount of catalyst ascend along the separating tube and are further separated in the auxiliary cyclone, so as to realize the fast and efficient separation between gas and solid.
Description
The invention belongs to the petrochemical technology field, the gas-solid eddy flow that relates to fluid catalytic cracking (FCC) riser reactor, particularly catalytic cracking riser reactor makes up fast subset.In the riser exit of oil plant fluid catalytic cracking reaction system, fast gas-solid separator all is housed to realize separating of catalyst and oil gas, stop unnecessary overreaction.This separator has two big classes at present, the first kind is that inertia divides device soon, it is to rely on the oil gas that contains a large amount of catalyst granules sharply to change the gas-solid two-phase inertia difference that is produced when flowing to realize gas solid separation, the typical fast packing of inertia is equipped with structures such as inverted L shape, T type, Multiblade, their characteristics are that pressure drop is very little, generally be no more than 1kPa, but the solid particle efficient that first separation is come out from gas has only about 70～80%.The oil gas that separates behind most of catalyst rises at a slow speed in the bigger settler of diameter, in about cyclone separator that was just entered settler top in 20 seconds, the catalyst of carrying secretly is further separated, and catalyst enters settler bottom bed along cyclone dip-leg.The catalyst that separates is all being carried a certain amount of oil gas secretly, needs in the bed of settler bottom to blow with steam to put forward, and this part oil gas rises to the inlet of settler top cyclone separator again through the time more than 30 seconds.Like this, the mean residence time of the oil gas behind the catalytic cracking reaction in settler may reach 20～30 seconds, the back-mixing rate height of oil gas, be easy to take place the elevated temperature heat cracking like this, yield of light oil is reduced, and can cause serious coking in the settler, influence the device long-term operation.
Second class is a centrifugal separator, and the strong centrifugal force field that it relies on gas-solid two-phase mixture to rotate formation rapidly realizes that gas-solid separates fast.Typical example is the one group of cyclone separator of outlet direct connection (be called for short and slightly revolve) at riser reactor, and its gas solid separation efficient can be up to more than 98%.The oil gas that separates most of catalyst is discharged from slightly revolving riser, enter settler space, rise with slower speed, through just being entered more than 10 seconds in the cyclone separator on settler top, oil gas further separates the catalyst of carrying secretly by this cyclone separator.Thick spin material leg is to discharge catalyst under positive differential pressure, when so a large amount of catalyst drops to settler bottom bed stripping section, not only the catalyst particles intergranular has been carried part oil gas secretly, flows downward, and also have a part of oil gas that sprays downwards under positive differential pressure from dipleg.These oil gas mix with stripping gas, and then rise at a slow speed along settler and to enter the cyclone separator on settler top.Make the mean residence time of reacted oil gas in settler still up to 10～20 seconds like this, at high temperature still have the overcracking phenomenon, influence the safe long-term operation of yield of light oil and device.
Divide device gas solid separation efficient not high problem soon for solving first kind inertia-type, U.S. Pat 4,495, ejection type quickly separating method and device have been developed in 063 (1985), its gas-solid first separation efficient reaches 80～90%, and the gas backmixing rate is reduced to about 20%, but pressure drop is up to thousands of handkerchiefs, operating flexibility is less, and industrial application has certain difficulty.U.S. Pat 4,364,905 (nineteen eighty-twos), US 5,294,331 (1994), US 5,364,515 (1994), US 5,393,414 (nineteen ninety-fives) improved again the fast branch of ejection type, mainly were in order further to shorten the mean residence time of oil gas in settler.But ejection type divides separative efficiency also not too high soon, and operating flexibility is again little, and industrial failing applied.
For solving the problem of second class device existence in centrifugal fast minute, U.S. Pat 4,502,947 (1985), US 4,579,716 (1986), US 4,624, enclosed direct connection cyclone separation system has been developed in 772 (1986) etc., to slightly revolve riser and directly link to each other, shorten the time of staying of oil gas in settler greatly, and make the back-mixing rate of gas further drop to 6～10% with settler top cyclone inlet, but the poor-performing of its compressive resistance fluctuation is wanted SC when going into operation.U.S. Pat 5 subsequently, 158,669 (1992), US 5,314,611 (1994), European patent EP 0593827A1, Chinese patent CN 92112441 (1992) etc. have directly connected a stripping section in the portion of screwing off slightly again, change part reaction back oil gas rough sledding of ejection downwards from thick spin material leg, further shortened the mean residence time of reaction back oil gas in settler, oil gas back-mixing rate is further dropped to below 2% again.
The circular arc bend pipe that U.S. Pat 4,482,451 (1984) have then adopted several downward-sloping certain angles at the riser end is as the gas-solid quick disconnector, and adds a seal bootr outside to realize drawing fast of oil gas.And in U.S. Pat 4,572,780 (1986) and US4 in 689,206 (1987), are provided with air deflector at the port of export of riser, and air deflector has two downward-sloping steering tubes.
In recent years, domestic petroleum university (Beijing) has developed FSC (Chinese patent ZL96103419.X), VQS (Chinese patent ZL96103478.5, ZL 96103420.3, ZL 01228805.5) and CSC (Chinese patent ZL 98102166.2, ZL 98204681.2) system.The FSC system has adopted just revolves the riser export structure that combines with the pre-stripper that adds ring baffle.Because added annular plate washer in pre-stripper, Srteam Stripping effect has bigger improvement than the VDS system of UOP.The CSC system has adopted just revolves or riser export structure that vortex quick separation combines with the pre-stripper that adds close-phase circulation.Because adopted the pre-gas stripping process of close-phase circulation, Srteam Stripping effect has had further raising again than FSC system, and structure is also very simple.The main distinction of the VSS system of VQS system and UOP is the improvement at eddy flow header structure and lower annular baffle arrangement.Yet, the fast subset of these spiral-flow types of VSS and VQS, its gas solid separation efficient generally is no more than 98～99%.
Through domestic and foreign literature and patent retrieval, do not find document and patent report that the major technique feature is identical with major technique feature of the present invention.
The purpose of this invention is to provide and to realize that the riser gas-solid eddy flow that gas-solid separates fast, separative efficiency is high makes up fast subset.
Riser gas-solid eddy flow of the present invention makes up fast subset, comprise riser, stripping tube, vortex flow quick separately, distributing damper, auxiliary cyclone, circulation pipe and seal bootr, it is characterized in that seal bootr (9) is cylindrical shape, seal bootr (9) inside comprises riser (1), taper stripping plate washer (2), shunting tube (3), vortex flow quick is (4) separately, shunting plate washer (5), auxiliary cyclone (6), circulation pipe (8) and stripping tube (10), the port of export of riser (1) is connected with vortex flow quick parted hair (4), shunting tube (3) be positioned at riser (1) the outlet position and with riser (1) coaxial line, between the outer wall of riser (1) outlet and shunting tube (3) inwall a circular passage is arranged, vortex flow quick a plurality of bend pipes (7) of (4) separately passes the wall of shunting tube (3) respectively, the port of export of bend pipe (7) is positioned at by seal bootr (9), in the space that shunting tube (3) and shunting plate washer (5) constitute, distributing damper (5) place vortex flow quick separately (4) top and be welded on the inwall of seal bootr (9) and the outer wall of shunting tube (3) on, auxiliary cyclone (6) is connected with the upper end of shunting tube (3), circulation pipe (8) places the outside of seal bootr (9), circulation pipe (8) upper end is positioned at the outside left of the above seal bootr (9) of shunting plate washer (5), the lower end is positioned at the stripping section position of seal bootr (9) bottom, and stripping tube (10) is positioned at the bottom of enclosed hood.
Riser gas-solid eddy flow of the present invention makes up fast subset, it is characterized in that auxiliary cyclone (6) top seal, have many tangential seams on the side walls, the direction of tangential seam is the rotation direction of favorable current, and total circulation area of tangential seam is 0.03～0.15 of seal bootr (a 9) cross-sectional area.
Riser gas-solid eddy flow of the present invention makes up fast subset, it is characterized in that vortex flow quick parted hair (4) is provided with 3～5 bend pipes (7), downward-sloping separately 0～45 degree, and make arranged tangential along seal bootr (9) inwall, the ejiction opening cross section of bend pipe (7) end is a rectangle, also can be circle or other shape.
Riser gas-solid eddy flow of the present invention makes up fast subset, and the circulation area that it is characterized in that circular passage between the outer wall of riser (1) outlet and shunting (3) inwall is 0.04～0.36 times of seal bootr sectional area.
Riser gas-solid eddy flow of the present invention makes up fast subset, it is characterized in that being positioned at the eddy flow piece and have a plurality of sieve apertures on the taper stripping baffles (2) of the bottom of (4) separately, aperture φ 3～φ 15mm, with seal bootr (9) is that the percent opening of benchmark is 1～15%, the positive pitch of taper stripping baffles (2) is 30 °～60 °, with vortex flow quick separately the vertical range of bend pipe (7) ejiction opening be (0.6～3) D3, D3 is the seal bootr internal diameter, also can arrange a plurality of taper stripping baffles below the taper stripping baffles (2).
Riser gas-solid eddy flow of the present invention makes up fast subset, it is characterized in that the bottom of circulation pipe (8) is provided with a loosening airduct (11).
Technical scheme of the present invention is, cylindrical shape seal bootr inside comprises riser, taper stripping plate washer, the shunting tube, vortex flow quick separately, the shunting plate washer, auxiliary cyclone, circulation pipe and stripping tube, the port of export of riser is connected separately with vortex flow quick, shunting tube be positioned at riser the outlet position and with the riser coaxial line, between the outer wall of riser outlet and the shunting tube inwall circular passage is arranged, vortex flow quick a plurality of bend pipes separately pass the wall of shunting tube respectively, the port of export of bend pipe is positioned at by seal bootr, in the space that shunting tube and shunting plate washer constitute, distributing damper place vortex flow quick separately top and be welded on the seal bootr inwall and the outer wall of shunting tube on, auxiliary cyclone is connected with the upper end of shunting tube, the catalyst circulation pipe places the outside of seal bootr, the circulation pipe upper end is positioned at the outside left of the above seal bootr of shunting plate washer, the lower end is positioned at the stripping section position of seal bootr bottom, and stripping tube is positioned at the bottom of enclosed hood.
Auxiliary cyclone top seal of the present invention has many tangential seams on the side walls, the direction of tangential seam is the rotation direction of favorable current.
Technical solution of the present invention is, on the upper end tube wall of shutting on the riser top, evenly have 3～5 rectangular openings or circular port, at each tapping, pick out a downward downward-sloping gradually hollow bent pipe, the end of each bend pipe is rectangle or circular opening, and the inwall of seal bootr is close in its outside, and makes arranged tangential along the seal bootr inwall.Reaction back oil gas and the outlet of mixture of catalysts process riser enter vortex flow quick parted hair and bend pipe, and the mixture of catalyst and oil gas is along the tangential ejection of bend pipe, and catalyst is because centrifugal action is downward along the rotation of seal bootr inwall.The catalyst granules rotation that the overwhelming majority is separated downwards, drop on the taper stripping plate washer, catalyst granules seldom rises on the circular passage between isolated oil gas edge shunting tube and riser, enter auxiliary cyclone, along many that have on the auxiliary cyclone side walls tangential seams, the rotation direction ejection of favorable current, gas-solid further separates, and isolated catalyst granules follows the stripping section that endless tube enters the seal bootr bottom.
Steam from stripping tube makes progress by the sieve aperture of taper stripping plate washer, contact with catalyst, remaining oil gas stripping in the catalyst is come out, and the oil gas that stripping comes out enters the upper space of seal bootr by the circular passage between riser outer wall and the shunting tube inwall.Like this, the present invention has just realized that the efficient of gas-solid separates fast.
The present invention can arrange a plurality of taper stripping plate washers that have sieve aperture in the bottom of seal bootr, depends on the needs.
The present invention has following good effect: can realize that efficient gas-solid separates fast, gas can be drawn fast, both realized gas-solid 99.9% above separative efficiency, simultaneously the mean residence time of oil gas in settler reduced to below 4 seconds, thereby avoided the cracking reaction of crossing that excessive contact owing to catalyst and product causes, avoided the coking in the settler, the distribution of product is improved.
Fig. 1 makes up the front view of fast subset for riser gas-solid eddy flow of the present invention.
Fig. 2 is to be the vertical view of eddy flow head.
Among Fig. 1 and Fig. 2,1 is riser, and 2 are the taper stripping baffles, and 3 are the shunting tube, and 4 is the vortex flow quick parted hair, and 5 is distributing damper, and 6 are auxiliary cyclone, and 7 is vortex flow quick bend pipe separately, and 8 is circulation pipe, and 9 is seal bootr, and 10 is stripping tube, and 11 for becoming flexible airduct.
Referring to Fig. 1, seal bootr (9) is columnar structured, seal bootr (9) inside comprises riser (1), taper stripping plate washer (2), shunting tube (3), vortex flow quick is (4) separately, shunting plate washer (5), auxiliary cyclone (6), circulation pipe (8) and stripping tube (10), the port of export of riser (1) is connected with vortex flow quick parted hair (4), shunting tube (3) be positioned at riser (1) the outlet position and with riser (1) coaxial line, between the outer wall of riser (1) outlet and shunting tube (3) inwall a circular passage is arranged, vortex flow quick a plurality of bend pipes (7) of (4) separately passes the wall of shunting tube (3) respectively, the port of export of bend pipe (7) is positioned at by seal bootr (9), in the space that shunting tube (3) and shunting plate washer (5) constitute, distributing damper (5) place vortex flow quick separately (4) top and be welded on the inwall of seal bootr (9) and the outer wall of shunting tube (3) on, auxiliary cyclone (6) is connected with the upper end of shunting tube (3), circulation pipe (8) places the outside of seal bootr (9), circulation pipe (8) upper end is positioned at the outside left of the above seal bootr (9) of shunting plate washer (5), the lower end is positioned at the stripping section position of seal bootr (9) bottom, and stripping tube (10) is positioned at the bottom of enclosed hood.
Auxiliary cyclone (6) top seal has many tangential seams on the side walls, the direction of tangential seam is the rotation direction of favorable current, and total circulation area of tangential seam is 0.03～0.15 of seal bootr (a 9) cross-sectional area.
Vortex flow quick separately (4) is provided with 3～5 bend pipes (7), downward-sloping separately 0～45 degree, and make arranged tangential along seal bootr (9) inwall, the ejiction opening cross section of bend pipe end is a rectangle, also can be circle or other shape.The circulation area of circular passage is 0.04～0.36 times of seal bootr sectional area between the outer wall of riser (1) outlet and shunting (3) inwall.
Be positioned at the eddy flow piece and separately have a plurality of sieve apertures on the taper stripping baffles (2) of the bottom of (4), aperture φ 3～φ 15mm, with seal bootr (9) is that the percent opening of benchmark is 1～15%, the positive pitch of taper stripping baffles (2) is 30 °～60 °, with vortex flow quick separately the vertical range of bend pipe (7) ejiction opening be (0.6～3) D3, D3 is the seal bootr diameter, also can arrange a plurality of taper stripping baffles below the taper stripping baffles (2).The bottom of circulation pipe (8) is provided with a loosening airduct (11).
Catalyst and gas mixture upwards enter vortex flow quick (4) separately through riser (1), through the vortex flow quick tangential ejection downwards of bend pipe (7) of (4) separately, form rotatablely moving of gas-solid mixture at the inwall of seal bootr (9), the most catalyst in the mixture are separated under effect of centrifugal force to drop to stripping section down and along the inwall of seal bootr (9).In stripping section, catalyst is wandered downwards along many group taper stripping baffles (2) successively, and by the stripping gas of stripping tube (10) ejection of stripping baffles (2) bottom the air-blowing of catalyst particles intergranular entrained oil is put forward.And rise on the circular passage of the oil gas after the catalyst separation through constituting between shunting tube (3) and the riser (1) and enter auxiliary cyclone (6), many the tangential seam ejections of opening on auxiliary cyclone (6) side walls again, further cutting out partial does not have the separated catalyst that gets off in (4) separately at vortex flow quick.This part catalyst that the auxiliary cyclone (6) of warp further separates is in circulation pipe (8) returns the stripping section of seal bootr (9) bottom.Oil gas after the separation continues to rise along seal bootr (9), thereby realizes that the efficient of catalyst and oil gas separates fast.
Claims (6)
1. riser gas-solid eddy flow makes up fast subset, comprise riser, stripping tube, vortex flow quick separately, distributing damper, auxiliary cyclone, circulation pipe and seal bootr, it is characterized in that seal bootr (9) is cylindrical shape, seal bootr (9) inside comprises riser (1), taper stripping plate washer (2), shunting tube (3), vortex flow quick is (4) separately, shunting plate washer (5), auxiliary cyclone (6), circulation pipe (8) and stripping tube (10), the port of export of riser (1) is connected with vortex flow quick parted hair (4), shunting tube (3) be positioned at riser (1) the outlet position and with riser (1) coaxial line, between the outer wall of riser (1) outlet and shunting tube (3) inwall a circular passage is arranged, vortex flow quick a plurality of bend pipes (7) of (4) separately passes the wall of shunting tube (3) respectively, the port of export of bend pipe (7) is positioned at by seal bootr (9), in the space that shunting tube (3) and shunting plate washer (5) constitute, distributing damper (5) place vortex flow quick separately (4) top and be welded on seal bootr (9) inwall and the outer wall of shunting tube (3) on, auxiliary cyclone (6) is connected with the upper end of shunting tube (3), circulation pipe (8) places the outside of seal bootr (9), circulation pipe (8) upper end is positioned at the outside left of the above seal bootr (9) of shunting plate washer (5), the lower end is positioned at the stripping section position of seal bootr (9) bottom, and stripping tube (10) is positioned at the bottom of seal bootr.
2. riser gas-solid eddy flow according to claim 1 makes up fast subset, it is characterized in that auxiliary cyclone (6) top seal, have many tangential seams on the side walls, the direction of tangential seam is the rotation direction of favorable current, and total circulation area of tangential seam is 0.03～0.15 of seal bootr (a 9) cross-sectional area.
3. riser gas-solid eddy flow according to claim 1 makes up fast subset, it is characterized in that vortex flow quick parted hair (4) is provided with 3～5 bend pipes (7), downward-sloping separately 0～45 degree, the ejiction opening cross section of bend pipe end is a rectangle, also can be circle or other shape.
4. riser gas-solid eddy flow according to claim 1 makes up fast subset, and the circulation area that it is characterized in that circular passage between the outer wall of riser (1) outlet and shunting (3) inwall is 0.04～0.36 times of seal bootr sectional area.
5. riser gas-solid eddy flow according to claim 1 makes up fast subset, it is characterized in that being positioned at the eddy flow piece and have a plurality of sieve apertures on the taper stripping baffles (2) of the bottom of (4) separately, aperture φ 3～φ 15mm, with seal bootr (9) is that the percent opening of benchmark is 1～15%, the positive pitch of taper stripping baffles (2) is 30 °～60 °, with vortex flow quick separately the vertical range of bend pipe (7) ejiction opening be (0.6～3) D3, D3 is the seal bootr internal diameter, also can arrange a plurality of taper stripping baffles below the taper stripping baffles (2).
6. riser gas-solid eddy flow according to claim 1 makes up fast subset, it is characterized in that the bottom of circulation pipe (8) is provided with a loosening airduct (11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02159407 CN1228137C (en) | 2002-12-31 | 2002-12-31 | Gas-solid cyclone combination fast separation device for lifting pipe |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02159407 CN1228137C (en) | 2002-12-31 | 2002-12-31 | Gas-solid cyclone combination fast separation device for lifting pipe |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1511627A true CN1511627A (en) | 2004-07-14 |
| CN1228137C CN1228137C (en) | 2005-11-23 |
Family
ID=34237451
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 02159407 Expired - Lifetime CN1228137C (en) | 2002-12-31 | 2002-12-31 | Gas-solid cyclone combination fast separation device for lifting pipe |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1228137C (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102925207A (en) * | 2011-08-12 | 2013-02-13 | 中国石油天然气股份有限公司 | Catalytic cracking method and device for processing heavy oil |
| CN109550318A (en) * | 2018-12-03 | 2019-04-02 | 中国石油大学(北京) | A kind of gas-liquid separator and its separation method |
| CN113117905A (en) * | 2021-03-04 | 2021-07-16 | 中国石油大学(华东) | Decoking device and method of cyclone separator for decoking of top gas of coking tower |
-
2002
- 2002-12-31 CN CN 02159407 patent/CN1228137C/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102925207A (en) * | 2011-08-12 | 2013-02-13 | 中国石油天然气股份有限公司 | Catalytic cracking method and device for processing heavy oil |
| CN102925207B (en) * | 2011-08-12 | 2014-11-19 | 中国石油天然气股份有限公司 | Catalytic cracking method and device for processing heavy oil |
| CN109550318A (en) * | 2018-12-03 | 2019-04-02 | 中国石油大学(北京) | A kind of gas-liquid separator and its separation method |
| CN109550318B (en) * | 2018-12-03 | 2023-11-17 | 中国石油大学(北京) | Gas-liquid separator and separation method thereof |
| CN113117905A (en) * | 2021-03-04 | 2021-07-16 | 中国石油大学(华东) | Decoking device and method of cyclone separator for decoking of top gas of coking tower |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1228137C (en) | 2005-11-23 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1051032C (en) | Apparatus for separation of solids from mixture of solids and fluid | |
| US4187089A (en) | Horizontal vapor-liquid separator | |
| EA003446B1 (en) | Process and apparatus for separating solid substances from gases | |
| CN100487081C (en) | Catalytic cracker without settler | |
| CA1295556C (en) | Apparatus and process for solids-fluid separation | |
| EP1054725B1 (en) | Method and assembly for separating solids from a gaseous phase | |
| WO2020143140A1 (en) | Separation system for slurry bed reactor | |
| CN1175916C (en) | Serial multi-stage process and its compact equipment for fast gas-solid separation and settling | |
| JPS62102849A (en) | Apparatus and method for separating solid and fluid | |
| US7799286B2 (en) | Stripping apparatus | |
| CN1228137C (en) | Gas-solid cyclone combination fast separation device for lifting pipe | |
| CN1229175C (en) | Gas-solid cyclone fast separation device for lifting pipe | |
| CN101524610B (en) | Vortex flow quick separation equipment at outlet of high-efficiency riser with conical flow isolating cylinder | |
| CN1055492C (en) | Fast gas-solid separation and gas lead-out method and equipment for hoisting-pipe catalytic-cracking reaction system | |
| US20090107884A1 (en) | Stripping apparatus and process | |
| CN2489874Y (en) | Open direct-coupling multi-arm cyclone separator with pre-stripping segment | |
| CN100497533C (en) | Catalytic cracker of coarse cyclone internal tubular settler | |
| CN2330404Y (en) | Melamine-urea washing and gas-liquid separation combined equipment | |
| US7914610B2 (en) | Stripping process | |
| CN1082392C (en) | Fast swirl gas-solid separator | |
| CN100487082C (en) | Catalytic cracker without settler | |
| CN113117633B (en) | High-speed spin flow gas-liquid mass transfer system | |
| CN110283631A (en) | A kind of device and method of fine coal pressurization continuous gasification furnace crude synthesis gas gas, liquid, solid three phase separation | |
| RU219177U1 (en) | MULTIVORTEX DEVICE WITH SEPARATION INCLINED PLATES | |
| CN114433001B (en) | Tandem type high-speed spin flow gas-liquid mass transfer system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20051123 |
|
| CX01 | Expiry of patent term |