CN1239681A - Magnetic separator for catalytic cracking waste catalyst, process flow and matched device - Google Patents
Magnetic separator for catalytic cracking waste catalyst, process flow and matched device Download PDFInfo
- Publication number
- CN1239681A CN1239681A CN 98110319 CN98110319A CN1239681A CN 1239681 A CN1239681 A CN 1239681A CN 98110319 CN98110319 CN 98110319 CN 98110319 A CN98110319 A CN 98110319A CN 1239681 A CN1239681 A CN 1239681A
- Authority
- CN
- China
- Prior art keywords
- magnetic
- ring
- catalytic cracking
- magnet
- separation
- 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
- 239000003054 catalyst Substances 0.000 title claims abstract description 35
- 239000006148 magnetic separator Substances 0.000 title claims abstract description 18
- 238000000034 method Methods 0.000 title claims abstract description 18
- 238000004523 catalytic cracking Methods 0.000 title claims description 12
- 239000002699 waste material Substances 0.000 title abstract description 15
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 27
- 238000007885 magnetic separation Methods 0.000 claims abstract description 19
- 238000000926 separation method Methods 0.000 claims description 25
- 239000006249 magnetic particle Substances 0.000 claims description 20
- 230000005284 excitation Effects 0.000 claims description 15
- 239000007787 solid Substances 0.000 claims description 9
- 239000002245 particle Substances 0.000 claims description 8
- 229910052751 metal Inorganic materials 0.000 claims description 5
- 239000002184 metal Substances 0.000 claims description 5
- 230000005540 biological transmission Effects 0.000 claims description 4
- 230000008878 coupling Effects 0.000 claims description 4
- 238000010168 coupling process Methods 0.000 claims description 4
- 238000005859 coupling reaction Methods 0.000 claims description 4
- 239000012298 atmosphere Substances 0.000 claims description 3
- 238000001816 cooling 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
- 239000004744 fabric Substances 0.000 claims 2
- 239000000463 material Substances 0.000 claims 2
- 230000000694 effects Effects 0.000 abstract description 7
- 238000005516 engineering process Methods 0.000 abstract description 6
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 5
- 238000011084 recovery Methods 0.000 abstract description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- 239000003921 oil Substances 0.000 description 6
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 230000003197 catalytic effect Effects 0.000 description 3
- 239000003638 chemical reducing agent Substances 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 230000005672 electromagnetic field Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000000265 homogenisation Methods 0.000 description 2
- 230000005389 magnetism Effects 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 239000002994 raw material Substances 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
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 230000006315 carbonylation Effects 0.000 description 1
- 238000005810 carbonylation reaction Methods 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000010586 diagram Methods 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
- 230000005307 ferromagnetism Effects 0.000 description 1
- 239000000295 fuel oil Substances 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
- 230000007774 longterm Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005486 sulfidation Methods 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Images
Landscapes
- Catalysts (AREA)
Abstract
Description
本发明涉及对炼油厂催化裂化废催化剂的回收利用。The invention relates to the recovery and utilization of catalytic cracking spent catalysts in oil refineries.
为了充分利用石油资源,石油的深加工如重油的催化裂化工艺是重要工艺环节。在催化裂化过程中,原料油所含的钒、镍、铁等重金属杂质会逐渐沉积到催化剂表面,降低催化剂的活性和选择性,从而降低了催化产物的收率和性能。为了使催化裂化装置中催化剂的性能保持在较高的水平,目前国内外普遍的作法是,定期从装置中卸出部分平衡剂,再向装置内补充部分新鲜催化剂。这种办法被长期实践证明是有效的,但是从装置卸出的废催化剂中实际上还含有一部分加入装置内运行不久的催化剂,其使用性能还较高,此部分随废剂一同弃置是对昂贵资源的浪费。废剂具有一定的放射性需深埋地下处理,大量废剂的处理,既污染环境又增大处理费用。因此,如何从废催化剂中分离出有用成份,一直是炼油厂急需解决的重大课题。In order to make full use of petroleum resources, the deep processing of petroleum, such as the catalytic cracking process of heavy oil, is an important process link. During the catalytic cracking process, heavy metal impurities such as vanadium, nickel, and iron contained in raw oil will gradually deposit on the surface of the catalyst, reducing the activity and selectivity of the catalyst, thereby reducing the yield and performance of the catalytic product. In order to keep the performance of the catalyst in the catalytic cracking unit at a high level, the current common practice at home and abroad is to regularly discharge part of the balancer from the unit, and then replenish part of the fresh catalyst into the unit. This method has been proved to be effective by long-term practice, but the spent catalyst discharged from the device actually contains a part of the catalyst that has been added to the device for a short time, and its performance is still relatively high. It is expensive to discard this part together with the spent catalyst. Waste of resources. The waste agent has a certain radioactivity and needs to be buried deep underground for disposal. The treatment of a large amount of waste agent not only pollutes the environment but also increases the treatment cost. Therefore, how to separate useful components from spent catalysts has always been a major issue that refineries urgently need to solve.
由硅、铝、沸石构成的催化剂是没有磁性的,但污染了铁、镍、钒等重金属以后,在磁场下会显示一定的磁性。重金属污染程度越高,催化剂在磁场中的磁性就越明显,因此就可以应用磁分离技术,将废剂按磁性不同分成两部分,一部分是在装置内运行时间较长、金属污染程度较严重、催化活性和选择性较低的磁性剂,另一部分是在装置内运行时间较短、金属污染程度较轻、催化活性和选择性较高的低磁性剂或非磁性剂,后者可再返回装置中使用。Catalysts composed of silicon, aluminum, and zeolite are non-magnetic, but after being contaminated with heavy metals such as iron, nickel, and vanadium, they will show certain magnetism under a magnetic field. The higher the degree of heavy metal pollution, the more obvious the magnetism of the catalyst in the magnetic field. Therefore, magnetic separation technology can be used to divide the waste agent into two parts according to their magnetic properties. The magnetic agent with lower catalytic activity and selectivity, and the other part is the low magnetic agent or non-magnetic agent with shorter running time in the device, less metal pollution, higher catalytic activity and selectivity, and the latter can be returned to the device used in .
专利US4359379公布了日本石油公司的高梯度磁分离技术,该技术应用于加工蒸馏渣油溶剂脱沥青油或加氢脱硫油的流化催化裂化装置,载体可选用空气、氢气、水蒸汽及其混合物,磁场强度为2000~20000高斯,磁场梯度为(2000~20000)×103高斯/厘米,介绍了分离的磁性物可通过离子交换、氯化、硫化、羰化、氧化还原等方法来脱除沉积的金属;专利US5190635阐述了铁磁性和超顺磁性对磁分离效果的影响;专利WO9219698中介绍,将废催化剂研磨、粒度分选,来增强磁分离效果,上述专利都没有涉及磁分离工艺及装备的型式结构。Patent US4359379 announced the high-gradient magnetic separation technology of Nippon Oil Corporation, which is applied to the fluidized catalytic cracking unit for processing distillation residual oil solvent deasphalted oil or hydrodesulfurized oil. Air, hydrogen, water vapor and their mixtures can be used as carriers , the magnetic field strength is 2000-20000 Gauss, and the magnetic field gradient is (2000-20000)×10 3 Gauss/cm. It is introduced that the separated magnetic substances can be removed by ion exchange, chlorination, sulfidation, carbonylation, redox and other methods. Deposited metal; Patent US5190635 describes the influence of ferromagnetism and superparamagnetism on the effect of magnetic separation; patent WO9219698 introduces that the waste catalyst is ground and particle size sorted to enhance the magnetic separation effect. The above patents do not involve magnetic separation technology and The type structure of the equipment.
本发明的目的在于,通过开发磁分离装备及相应的磁分离工艺流程,实现废催化剂中有用部分的回收利用。The purpose of the present invention is to realize the recovery and utilization of useful parts in spent catalysts by developing magnetic separation equipment and corresponding magnetic separation process flow.
本发明的技术方案是,设计一套做为核心装置的磁分离机,以及以压缩空气为废剂输送载体的磁分离工艺配套装置。The technical scheme of the present invention is to design a set of magnetic separator as the core device, and a magnetic separation process supporting device using compressed air as the waste agent delivery carrier.
磁分离机由分选环和磁体两个最重要的工作单元构成,分选环主轴由调速电机、减速器联轴节驱动,分选环工作在垂直平面内,分选环环体被隔离成若干分离室,每个分离室内交叠放置导磁和不导磁金属网丝,在强磁场背景下形成高梯度磁场空间,成为废催化剂的磁分离场所。磁体由以工程纯铁为材料的磁轭和在其内水平放置的激磁线圈组成,是产生电磁场的单元。磁轭内部形成供分选环体转动的环形通道,分选环径向平面与激磁线圈平面垂直交割,使转动部分的分选环体在转动周期依次进入磁场、脱离磁场。环形通道的上、下方的磁轭体内设有相互隔离的两组溜料槽,磁体上方设置废剂给料器和压缩空气风斗。磁分离机还包括向激磁线圈提供强大直流电的整流器和对激磁线圈、整流器降温的循环冷却系统。The magnetic separator is composed of the two most important working units, the sorting ring and the magnet. The main shaft of the sorting ring is driven by a speed-regulating motor and a reducer coupling. The sorting ring works in a vertical plane, and the body of the sorting ring is isolated It is divided into several separation chambers, and each separation chamber is overlapped with magnetically conductive and nonmagnetic metal mesh wires to form a high-gradient magnetic field space under the background of a strong magnetic field and become a magnetic separation place for spent catalysts. The magnet is composed of a yoke made of engineering pure iron and an excitation coil placed horizontally inside it, which is the unit that generates the electromagnetic field. The inside of the yoke forms an annular channel for the rotation of the sorting ring. The radial plane of the sorting ring is perpendicular to the plane of the excitation coil, so that the sorting ring in the rotating part enters and leaves the magnetic field in turn during the rotation cycle. The upper and lower yoke bodies of the annular channel are provided with two groups of chutees isolated from each other, and a waste agent feeder and a compressed air wind bucket are arranged above the magnet. The magnetic separator also includes a rectifier that supplies powerful direct current to the excitation coil and a circulating cooling system that cools the excitation coil and the rectifier.
为了增加分离室的数量空间,提高分选环的结构强度,分选环采用以中环板为支承筋板、两侧并列设置环体的结构形式。In order to increase the number and space of the separation chamber and improve the structural strength of the sorting ring, the sorting ring adopts a structural form in which the middle ring plate is used as a supporting rib and the rings are arranged side by side on both sides.
在分离室内,尚有一少部分非磁性颗粒裹胁在磁性颗粒中而被吸附于导磁网丝上。本发明的分选环主轴通过轴承装有激振轮,激振轮上设置可调节位置的偏心块,分选环主轴由橡胶弹簧组成的弹性支承支持在磁体上,并由电机、皮带传动付、减速器和联轴节驱动,使主轴转速可调,如电机采用调速电机,或改变皮带传动付的传动比。调速电机、皮带传动付和驱动激振轮振动单元组成,使分选环体产生径向振动,从而释放出被磁性剂裹胁的非磁性颗粒,以提高非磁性剂的回收率。In the separation chamber, there are still a small number of non-magnetic particles trapped in the magnetic particles and adsorbed on the magnetic mesh. The main shaft of the sorting ring of the present invention is equipped with an exciting wheel through a bearing, and an eccentric block with an adjustable position is arranged on the exciting wheel. , reducer and coupling drive, so that the spindle speed can be adjusted, such as using a speed-adjusting motor for the motor, or changing the transmission ratio of the belt drive. The speed-regulating motor, the belt drive pair and the vibration unit of the driving excitation wheel make the sorting ring generate radial vibration, thereby releasing the non-magnetic particles trapped by the magnetic agent, so as to improve the recovery rate of the non-magnetic agent.
本发明以压缩空气为废催化剂载体,工艺配套流程为:废催化剂经磁性粗滤网滤除强磁性颗粒和大尺寸杂质后,进入原料罐,由进料控制器调控,不断地与风源输出的压缩空气混合,送入磁分离机内的给料器均匀化,然后进入在磁场内的分选环分离室进行磁分离,磁性颗粒吸附在得磁金属丝网上,非磁性颗粒通过一组溜料槽分离;同时,压缩空气风斗吹出磁场内滞留在分离室中的弱磁性颗粒,沿另一组溜料槽将中性颗粒分离;随着分选环转动,分离室脱离磁场,导磁性金属丝网失磁,机内放置的压缩空气风斗将磁性颗粒吹离;分选环上方设置有反洗风斗,压缩空气反向吹入,清除分离室内残留颗粒,疏清金属丝网;携带磁性、弱磁性、非磁性颗粒的压缩空气,分别通过管道进入相应的气固分离器,将固体颗粒分离收集,其尾气经净化器进一步除尘后排向大气。In the present invention, compressed air is used as the waste catalyst carrier, and the supporting process of the process is as follows: after the waste catalyst is filtered by a magnetic coarse filter to remove strong magnetic particles and large-sized impurities, it enters the raw material tank, is regulated by the feed controller, and is continuously output with the wind source The compressed air is mixed, sent to the feeder in the magnetic separator for homogenization, and then enters the sorting ring separation chamber in the magnetic field for magnetic separation. The magnetic particles are adsorbed on the magnetic wire mesh, and the non-magnetic particles pass through a set of slides. The trough is separated; at the same time, the compressed air fan blows out the weak magnetic particles trapped in the separation chamber in the magnetic field, and separates the neutral particles along another set of chute; as the separation ring rotates, the separation chamber is separated from the magnetic field, and the magnetic field The wire mesh is demagnetized, and the compressed air wind bucket placed in the machine blows away the magnetic particles; there is a backwash wind bucket above the separation ring, and the compressed air is blown in reverse to remove the residual particles in the separation chamber and clear the wire mesh; Compressed air carrying magnetic, weakly magnetic, and non-magnetic particles enters the corresponding gas-solid separator through the pipeline to separate and collect the solid particles, and the exhaust gas is further dedusted by the purifier and then discharged to the atmosphere.
应用本发明磁分离技术及装备,非磁性剂回收率达到60%以上,在磁场强度为9000—11000高斯条件下,回收的非磁性剂重金属含量明显低于废催化剂,其微反活性提高3个单位以上,将非磁性剂返回到催化剂装置中使用后可节约新鲜催化剂的用量,同时又减少了废剂处理费用,具有十分显著的经济效益和社会效益。With the application of the magnetic separation technology and equipment of the present invention, the recovery rate of the non-magnetic agent reaches over 60%. Under the condition of a magnetic field strength of 9000-11000 gauss, the heavy metal content of the recovered non-magnetic agent is significantly lower than that of the spent catalyst, and its micro-reaction activity is increased by 3 More than one unit, returning the non-magnetic agent to the catalyst device for use can save the amount of fresh catalyst, and at the same time reduce the cost of waste agent treatment, which has very significant economic and social benefits.
下面给出本发明的实施例:Provide the embodiment of the present invention below:
附图1为磁分离机结构主视图。Accompanying drawing 1 is the front view of magnetic separator structure.
附图2为磁分离机结构侧视图。Accompanying
附图3为分选环结构主视图。Accompanying drawing 3 is the front view of the sorting ring structure.
附图4为分选环结构侧视图。Accompanying drawing 4 is the side view of sorting ring structure.
附图5为磁体立体结构示意图。Accompanying drawing 5 is the schematic diagram of the three-dimensional structure of the magnet.
附图6为磁分离工艺流程简图。Accompanying drawing 6 is a schematic flow chart of the magnetic separation process.
磁分离机由分选环1、磁体2两个主要工作单元构成。分选环工作在垂直平面内,其主轴3由弹簧橡胶组成的弹性支承12支持在磁体2上,分选环主轴3由电机4、皮带传动付5、减速器6和联轴节7驱动,并使主轴转速可调,如电机采用调速电机或改变皮带传动付的传动比。主轴3的另一端通过轴承装有激振轮8,激振轮上设置可调节位置的偏心块9;在调速电机10和皮带传动付11的驱动下,激振轮旋转,使分选环体产生径向振动。改变调速电机转速可以控制分选环的转速和振动频率,改变偏心块的质量或位移,可以控制分选环体径向振幅。The magnetic separator consists of two main working units, the sorting ring 1 and the
分选环以中环板13为支持板,其两侧并列环体14,隔板15将环体分隔成若干分离室,每个分离室内交错叠放导磁和不导磁金属丝网16,托棒17和压棒18将金属丝网固定压紧。分离室是磁分离的主要场所,中环板中心套与主轴3键联。The sorting ring takes the middle ring plate 13 as the support plate, and the ring body 14 is juxtaposed on both sides. The
磁体2是产生电磁场的场所,以工程纯铁为材料,由左上磁轭19、右上磁轭20、侧磁轭21和下磁轭22组合而成。磁轭体内水平放置激磁线圈23,线圈截面为矩形或圆形,中间通孔为冷却剂提供流动通道。磁轭的作用是形成封闭磁路,并防止磁力线外泄,四块磁轭拼置为一体,结合面采用耐压密封,防止废催化剂外泄;在磁体内部,激磁线圈要与风和催化剂通道完全隔离,以保证线圈绝缘完好;磁轭内部形成供分选环体转动的环形通道24,环形通道位于激磁线圈内,且工作平面与激磁线圈平面垂直交割,环形通道24的上、下方的磁轭体内设有相互隔离的两组溜料槽,它们分别是非磁性颗粒溜料槽25和弱磁性颗粒溜料槽26。机罩27与主轴和磁体2上表面耐压密封。磁分离机还配置有向激磁线圈提供强大直流电的整流器29,和对激磁线圈、激振线圈冷却的循环水冷装置28。The
图6给出了磁分离工艺配套流程简图。压缩空气源30通过流量计31及送风管线向磁分离机输送废催化剂载体风和工艺用风,从催化裂化装置中卸出的废剂先经过磁性粗滤网,滤除强磁性颗粒和大尺寸杂质后装入原料罐32,经由阀门33、进料控制器34调控,不断与压缩空气混合,送入磁分离机内的给料器35均匀化,到达磁场中的分选环分离室,磁性颗粒吸附于得磁金属丝网16,非磁性颗粒经溜料槽25分离;同时,弱磁性颗粒在压缩空气风斗36作用下,做为中性剂经溜料槽26分离;风斗37将脱离磁场分离室内磁性颗粒吹离;反洗风斗38的压缩空气反向吹入分离室,清除残留颗粒疏通金属丝网,保证下一次接受废催化剂时处于干净状态。从磁分离机输出的压缩空气携带分离的磁性颗粒或非磁性颗粒分别进入气固分离器39分离出固体剂,并分别收入磁性剂收集罐41和非磁性剂收集罐40,中间剂根据工艺需要或使用要求可并入非磁性剂或磁性剂中,从气固分离器出来的尾气夹带少许固体颗粒,经净化器42进一步去除后排向大气。Figure 6 shows a schematic flow chart of the magnetic separation process. The
对于不同金属含量的催化剂,其分离效果和非磁性剂收率与磁场强度、分选环转速、振动频率、压缩空气流量和废剂处理量等工艺参数关系密切,本发明在上述环节都采用了可调节措施,以便于试验获得最佳效果。For catalysts with different metal contents, the separation effect and non-magnetic agent yield are closely related to process parameters such as magnetic field strength, sorting ring speed, vibration frequency, compressed air flow rate and waste agent treatment capacity. Measures can be adjusted to facilitate experimentation to obtain the best results.
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 true CN1239681A (en) | 1999-12-29 |
| CN1089642C 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) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1814711B (en) * | 2004-12-10 | 2010-08-04 | 新日本石油株式会社 | Magnetic separation method for fluid contact decomposition catalyst |
| CN108774687A (en) * | 2018-08-07 | 2018-11-09 | 陈子清 | A method of recycling noble metal in catalyst using Magneto separate |
| CN111153473A (en) * | 2020-02-10 | 2020-05-15 | 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 |
| CN116371596A (en) * | 2023-05-26 | 2023-07-04 | 北京华科泰生物技术股份有限公司 | An integrated magnetic separation device |
Family Cites Families (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 |
-
1998
- 1998-06-24 CN CN98110319A patent/CN1089642C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1814711B (en) * | 2004-12-10 | 2010-08-04 | 新日本石油株式会社 | Magnetic separation method for fluid contact decomposition catalyst |
| CN108774687A (en) * | 2018-08-07 | 2018-11-09 | 陈子清 | A method of recycling noble metal in catalyst using Magneto separate |
| CN111153473A (en) * | 2020-02-10 | 2020-05-15 | 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 |
| CN116371596A (en) * | 2023-05-26 | 2023-07-04 | 北京华科泰生物技术股份有限公司 | An integrated magnetic 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 |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1089642C (en) | 2002-08-28 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| RU2502563C1 (en) | Vertical circular magnetic separator to remove iron from coal ash and method of its application | |
| JP6358519B1 (en) | Soil purification system | |
| JP6399325B1 (en) | Soil purification system | |
| Hoffmann et al. | A novel high-gradient magnetic separator (HGMS) design for biotech applications | |
| CN100577300C (en) | Continuous Discrete Rare Earth Permanent Magnet High Gradient Magnetic Separator | |
| 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 | |
| JP2020075242A (en) | Soil remediation system | |
| CN210876716U (en) | Dry-wet separation system for waste catalyst | |
| CN1239681A (en) | Magnetic separator for catalytic cracking waste catalyst, process flow and matched device | |
| CN101554614A (en) | Anti-podal permanent magnetic high-intensity magnetic separator | |
| CN210097939U (en) | Iron remover | |
| CN108452943B (en) | A permanent magnet induction high gradient disk machine | |
| CN106216095A (en) | Concentration equipment | |
| CN2133361Y (en) | Permanent-magnet three-level five-roller dry magnetic separator | |
| CN202045006U (en) | Permanente magnet coal heavy-medium recovery equipment | |
| WO2015052368A1 (en) | A method and a device for separating weakly magnetic particles | |
| CN116328938B (en) | Weak-field strong high-gradient magnetic separator for recovering magnetite and configuration and beneficiation process thereof | |
| CN2262460Y (en) | Separator | |
| CN113969182A (en) | Device and method for separating solid particles in catalytic cracking slurry oil | |
| CN2345286Y (en) | Magnetic separation device for catalytic cracking waste catalyst | |
| CN1158279A (en) | Magnetic screening machine | |
| KR20110056654A (en) | Powder Magnetic Separation Device Using Superconducting Magnet | |
| CN101823020B (en) | Permanent magnet vibration module type magnetic separator | |
| CN210876715U (en) | Dry type sorting system for waste catalyst |
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 |