CN1089642C - Magnetic separation method and device for catalytic cracking waste catalyst - Google Patents
Magnetic separation method and device for catalytic cracking waste catalyst Download PDFInfo
- Publication number
- CN1089642C CN1089642C CN98110319A CN98110319A CN1089642C CN 1089642 C CN1089642 C CN 1089642C CN 98110319 A CN98110319 A CN 98110319A CN 98110319 A CN98110319 A CN 98110319A CN 1089642 C CN1089642 C CN 1089642C
- Authority
- CN
- China
- Prior art keywords
- magnetic
- ring
- separator
- main shaft
- compressed air
- 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.)
- Expired - Fee Related
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 28
- 238000000034 method Methods 0.000 title claims abstract description 17
- 238000004523 catalytic cracking Methods 0.000 title claims abstract description 14
- 238000007885 magnetic separation Methods 0.000 title claims abstract description 9
- 239000002699 waste material Substances 0.000 title claims abstract description 7
- 239000006148 magnetic separator Substances 0.000 claims abstract description 16
- 238000000926 separation method Methods 0.000 claims description 23
- 239000003795 chemical substances by application Substances 0.000 claims description 22
- 239000006249 magnetic particle Substances 0.000 claims description 12
- 239000007787 solid Substances 0.000 claims description 10
- 230000005284 excitation Effects 0.000 claims description 8
- 229910052751 metal Inorganic materials 0.000 claims description 6
- 239000002184 metal Substances 0.000 claims description 6
- 239000002245 particle Substances 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 3
- 230000008878 coupling Effects 0.000 claims description 3
- 238000010168 coupling process Methods 0.000 claims description 3
- 238000005859 coupling reaction Methods 0.000 claims description 3
- 230000007935 neutral effect Effects 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 239000002994 raw material Substances 0.000 claims 2
- 239000003638 chemical reducing agent Substances 0.000 claims 1
- 230000006835 compression Effects 0.000 claims 1
- 238000007906 compression Methods 0.000 claims 1
- 238000000265 homogenisation Methods 0.000 claims 1
- 238000002156 mixing Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 9
- 230000007246 mechanism Effects 0.000 abstract description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 239000000203 mixture Substances 0.000 description 5
- 239000003921 oil Substances 0.000 description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- 230000005540 biological transmission Effects 0.000 description 4
- 239000004744 fabric Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 230000003197 catalytic effect Effects 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 229910001385 heavy metal Inorganic materials 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 230000005389 magnetism Effects 0.000 description 3
- 230000033228 biological regulation Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 229910052720 vanadium Inorganic materials 0.000 description 2
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000027455 binding Effects 0.000 description 1
- 238000009739 binding Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000006315 carbonylation Effects 0.000 description 1
- 238000005810 carbonylation reaction Methods 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000005672 electromagnetic field Effects 0.000 description 1
- 230000005307 ferromagnetism Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 238000005987 sulfurization reaction Methods 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Images
Landscapes
- Catalysts (AREA)
Abstract
The invention relates to a method and a device for magnetically separating and recovering catalytic cracking waste catalyst. The magnetic separator consists of vertical separating ring and two main working units, the working surface of the separating ring is perpendicular to the plane of the exciting coil inside the magnet, the separating ring is divided into several magnetic separating chambers with magnetic conducting wire net, the waste catalyst is carried by compressed air to realize continuous magnetic separation, and the separating ring also adopts radial vibration mechanism to strengthen magnetic separation effect.
Description
The present invention relates to recycling to the refinery catalytic cracking spent catalyst.
In order to make full use of petroleum resources, the deep processing of oil such as the catalytic cracking process of heavy oil are the important process links.In catalytic cracking process, beavy metal impurities such as the contained vanadium of stock oil, nickel, iron can deposit to catalyst surface gradually, reduce activity of such catalysts and selectivity, thereby have reduced the yield and the performance of catalysate.For the property retention that makes catalyzer in the catalytic cracking unit in higher level, the general practice is both at home and abroad at present, regularly draws off the partial equilibrium agent from device, more additional part live catalyst in device.This way is proved effectively by long-term practice, but in fact also contains in some adding apparatus operation catalyzer soon from the spent catalyst that device draws off, and its use properties is also higher, and it is waste to expensive resource that this part is together thrown aside with useless agent.Useless agent has certain radioactivity needs buried underground disposal, the processing of useless agent in a large number, not only contaminate environment but also increase processing costs.Therefore, how to isolate useful composition from spent catalyst, be the key subjects that refinery is badly in need of solution always.
The catalyzer that is made of silicon, aluminium, zeolite does not have magnetic, but has polluted after the heavy metals such as iron, nickel, vanadium, can show certain magnetic under magnetic field.The heavy metal contamination degree is high more, the magnetic of catalyzer in magnetic field is just obvious more, therefore just can use magnetic separation technique, to give up agent by the different separated into two parts of magnetic, a part be in device working time long, metallic pollution degree seriously, catalytic activity and the lower magnetic agent of selectivity, another part be in device working time short, metallic pollution degree gently, the higher low magnetic agent of catalytic activity and selectivity or non magnetic dose, the latter uses in the return mechanism again.
Patent US43S9379 has announced the High-gradient Magnetic isolation technique of Japan National Oil Corporation, this technology is applied to process the fluidized catalytic cracker of distillation residue solvent-deasphalted oils or hydrogenating desulfurization oil, carrier can be selected air, hydrogen, water vapor and composition thereof for use, magneticstrength is 2000~20000 Gausses, and field gradient is (2000-20000) * 10
3Gauss/cm
3, introduced isolating magnetic thing and can remove sedimentary metal by methods such as ion-exchange, chlorination, sulfuration, carbonylation, redox; Patent US519063S has set forth the influence to the magnetic separating effect of ferromegnetism and superparamagnetism; Introduce among the patent WO9219698, with spent catalyst grinding, size sorting, strengthen the magnetic separating effect, above-mentioned patent does not all relate to the type structure of magnetic separating technology and equipment.
The objective of the invention is to, propose a kind of catalytic cracking spent catalyst magnetism separate method and device, realize the recycling of useful part in the spent catalyst.
The catalytic cracking spent catalyst magnetism separate method that the present invention proposes is: adopt pressurized air as used catalyst support, the useless agent that draws off from catalytic cracking unit, through magnetic coarse strainer charging feedstock jar, through the feed controller regulation and control, constantly mix with pressurized air, send into the material feeder homogenizing in the magnetic separator, arrive the separation ring separate chamber in the magnetic field, isolate non magnetic dose; The pressurized air wind scoop is isolated neutral agent with weak magnetic-particle in the separate chamber in the magnetic field; The pressurized air wind scoop will break away from that magnetic-particle blows off in the separate chamber in magnetic field; The backwash wind scoop is removed residual particles in the separate chamber, dredges clear wire cloth; Carry the magnetic agent, non magnetic dose pressurized air enters gas-solid separator respectively and isolates solid particulate; The tail gas that produces is after the cleaner dedusting, and row is to atmosphere.
Device of the present invention mainly comprises magnetic separator and corollary apparatus; Corollary apparatus mainly include compressed air source, spent catalyst head tank, gas-solid separator, cleaner and holding tank and; Magnetic separator mainly includes separation ring and two groundwork unit of magnet and rectifier, water cooling plant, and separation ring is operated in the vertical plane, and the separation ring ring body is isolated into the plurality of separate chamber, overlaps in the separate chamber to place magnetic conduction and magnetic conductive metal silk screen not; Magnet by magnetic field and therein the magnetizing coil of horizontal positioned form, the circular channel that the inner formation of yoke is rotated for the sorting ring body, separation ring radially working face are completed a business transaction with the magnetizing coil plane is vertical, be provided with in the upper and lower yoke body of circular channel mutual isolated slide hopper and, magnet top is provided with spent catalyst material feeder and pressurized air wind scoop; The elastic support that the separation ring main shaft is made up of rubber spring is supported on the magnet, main shaft by buncher, belt transmission pay, speed reduction unit, shaft coupling drive, and make the speed of mainshaft adjustable; The other end of main shaft is equipped with excitation wheel.
Use magnetic separation technique of the present invention and equipment, the non magnetic dose of rate of recovery reaches more than 60%, in magneticstrength is under the 9000-11000 Gauss condition, the non magnetic dose of heavy metal content that reclaims is starkly lower than spent catalyst, its micro-activity improves 3 more than the unit, turn back in the catalyst-assembly consumption that can save live catalyst after using with non magnetic dose, reduced useless agent processing costs again simultaneously, have very remarkable economic efficiency and social benefit.
Provide embodiments of the invention below:
Accompanying drawing 1 is the magnetic separator structural front view.
Accompanying drawing 2 is magnetic separator structure side view.
Accompanying drawing 3 is the separation ring structural front view.
Accompanying drawing 4 is a separation ring structure side view.
Accompanying drawing 5 is the magnet perspective view.
Accompanying drawing 6 is a magnetic separation process scheme sketch.
Magnetic separator is made of separation ring 1,2 two groundwork unit of magnet.Separation ring is operated in the vertical plane, the elastic support 12 that its main shaft 3 is made up of spring rubber is supported on the magnet 2, separation ring main shaft 3 by motor 4, belt transmission pay 5, speed reduction unit and shaft coupling 7 drive, and make the speed of mainshaft adjustable, adopt buncher or change the transmitting ratio that belt transmission is paid as motor.The other end of main shaft 3 is equipped with excitation wheel 8 by bearing, and the eccentric block 9 of adjustable position is set on the excitation wheel; Pay in buncher 10 and belt transmission under 11 the driving, the excitation wheel rotation, make the sorting ring body produce radial vibration and change rotating speed and the vibrational frequency that the buncher rotating speed can be controlled separation ring, change the quality or the displacement of eccentric block, can control radially amplitude of sorting ring body.
Separation ring is a supporting plate with middle ring flat-plate 13, its both sides ring body 14 arranged side by side, if dividing plate 15 is separated into ring body in the separate chamber, interfolded magnetic conduction and magnetic conductive metal silk screen 16 not each separate chamber in, hold in the palm excellent 17 and pressure bar 18 wire cloth is fixed and clamped.The separate chamber is the isolating main place of magnetic, middle ring flat-plate center and main shaft 3 bindings.
Fig. 6 has provided magnetic separation process scheme sketch.Compressed air source 30 is carried used catalyst support wind and technology wind by under meter 31 and the magnetic separator of blast tube alignment, the useless agent that draws off from catalytic cracking unit is earlier through the magnetic coarse strainer, charging feedstock jar 32 behind filtering ferromagnetism particle and the large size impurity, via valve 33, feed controller 34 regulation and control, constantly mix with pressurized air, send into material feeder 35 homogenizing in the magnetic separator, arrive the separation ring separate chamber in the magnetic field, magnetic-particle be adsorbed in magnetic wire cloth 16, non-magnetic particle separates through slipping hopper 2S; Simultaneously, weak magnetic-particle separates through slide hopper 26 as neutral agent under 36 effects of pressurized air wind scoop; Wind scoop 37 will break away from the indoor magnetic-particle of magnetic field separation and blow off; The pressurized air of backwash wind scoop 38 oppositely is blown into the separate chamber, removes residual particles mediation wire cloth, is in clean state when guaranteeing to accept spent catalyst next time.Carrying isolating magnetic-particle or non-magnetic particle from the pressurized air of magnetic separator output enters gas-solid separator 39 respectively and isolates solid formulation; and take in magnetic agent holding tank 41 and non magnetic dose of holding tank 40 respectively; intermediate agent can be incorporated in non magnetic dose or the magnetic agent according to arts demand or service requirements; carry a little solid particulate secretly from the gas-solid separator tail gas discharged, row is to atmosphere after cleaner 42 is further removed.
At catalyzer for different metal content, its separating effect and non magnetic dose of yield and processing parameters such as magneticstrength, separation ring rotating speed, vibrational frequency, compressed air require and useless agent treatment capacity are in close relations, the present invention has adopted the measure of can regulating in above-mentioned link, so that test obtains best effect.
Claims (4)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN98110319A CN1089642C (en) | 1998-06-24 | 1998-06-24 | Magnetic separation method and device for catalytic cracking waste catalyst |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN98110319A CN1089642C (en) | 1998-06-24 | 1998-06-24 | Magnetic separation method and device for catalytic cracking waste catalyst |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1239681A CN1239681A (en) | 1999-12-29 |
| CN1089642C true CN1089642C (en) | 2002-08-28 |
Family
ID=5220380
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN98110319A Expired - Fee Related CN1089642C (en) | 1998-06-24 | 1998-06-24 | Magnetic separation method and device for catalytic cracking waste catalyst |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1089642C (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101250173B1 (en) * | 2004-12-10 | 2013-04-04 | 자이단호진 세키유산교캇세이카센터 | Magnetic separation method of fluidized catalytic cracking catalyst |
| CN108774687B (en) * | 2018-08-07 | 2019-12-13 | 陈子清 | method for recovering noble metal in catalyst by magnetic separation |
| CN111153473B (en) * | 2020-02-10 | 2024-11-08 | 华电水务科技股份有限公司 | A continuous high gradient magnetic separation device |
| CN115213001A (en) * | 2021-04-21 | 2022-10-21 | 国家能源投资集团有限责任公司 | Separation device |
| CN116371596B (en) * | 2023-05-26 | 2023-08-18 | 北京华科泰生物技术股份有限公司 | Integrated magnetic separation device |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4359379A (en) * | 1979-12-21 | 1982-11-16 | Nippon Oil Company, Ltd. | Process for fluid catalytic cracking of distillation residual oils |
| CN86206395U (en) * | 1986-09-01 | 1987-12-16 | 西安交通大学 | Ac separator for iron and magnetism |
| CN2109256U (en) * | 1991-12-16 | 1992-07-08 | 开封磁性材料厂 | Permanent-magnet separator |
| US5190635A (en) * | 1989-04-03 | 1993-03-02 | Ashland Oil, Inc. | Superparamagnetic formation of FCC catalyst provides means of separation of old equilibrium fluid cracking catalyst |
| US5393412A (en) * | 1991-05-03 | 1995-02-28 | Ashland Oil, Inc. | Combination magnetic separation, classification and attrition process for renewing and recovering particulates |
-
1998
- 1998-06-24 CN CN98110319A patent/CN1089642C/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4359379A (en) * | 1979-12-21 | 1982-11-16 | Nippon Oil Company, Ltd. | Process for fluid catalytic cracking of distillation residual oils |
| CN86206395U (en) * | 1986-09-01 | 1987-12-16 | 西安交通大学 | Ac separator for iron and magnetism |
| US5190635A (en) * | 1989-04-03 | 1993-03-02 | Ashland Oil, Inc. | Superparamagnetic formation of FCC catalyst provides means of separation of old equilibrium fluid cracking catalyst |
| US5393412A (en) * | 1991-05-03 | 1995-02-28 | Ashland Oil, Inc. | Combination magnetic separation, classification and attrition process for renewing and recovering particulates |
| CN2109256U (en) * | 1991-12-16 | 1992-07-08 | 开封磁性材料厂 | Permanent-magnet separator |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1239681A (en) | 1999-12-29 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP6358520B1 (en) | Soil purification system | |
| JPH04503373A (en) | Feed oil conversion method | |
| MX2014001276A (en) | Ore beneficiation. | |
| WO2009103191A1 (en) | Devece and process for continuously separating and recoverying magnetic solid particles from solid-liquid mixtures | |
| CN109530083B (en) | A fine particle continuous dry magnetic separation device and its use method | |
| NO20141146A1 (en) | Process and system for the dry extraction of fine and superfine iron ore particles and a magnetic separation unit | |
| CN210876716U (en) | Dry-wet separation system for waste catalyst | |
| JP2020075242A (en) | Soil purification system | |
| CN2382474Y (en) | Crawler-type magnetic separator | |
| CN116984119B (en) | A flat-ring dry magnetic separation device and method for iron ore | |
| CN101554614A (en) | Anti-podal permanent magnetic high-intensity magnetic separator | |
| CN102764733B (en) | Chromium ore recovering system | |
| CN1239681A (en) | Magnetic separator for catalytic cracking waste catalyst, process flow and matched device | |
| CN113969182B (en) | Device and method for separating solid particles in catalytic cracking slurry oil | |
| CN108452943B (en) | A permanent magnet induction high gradient disk machine | |
| JP6451973B1 (en) | Soil purification system | |
| CN2133361Y (en) | Permanent-magnet three-level five-roller dry magnetic separator | |
| CN116328938B (en) | Weak-field strong high-gradient magnetic separator for recovering magnetite and configuration and beneficiation process thereof | |
| CN2345286Y (en) | Magnetic separation device for catalytic cracking waste catalyst | |
| CN210876715U (en) | Dry type sorting system for waste catalyst | |
| CN87107743A (en) | High frequency vibration spiral chute concentrator | |
| CN212418286U (en) | A magnetic beneficiation shaker for silica ore | |
| EP0072060A2 (en) | Process for the agglomeration of solids | |
| CN118663164B (en) | Apparatus and method for continuous separation of magnetically separable catalysts | |
| CN212441617U (en) | A steel fragment sorting device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C06 | Publication | ||
| PB01 | Publication | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |