CN2611040Y - On-line equipment for magnetic separation and recovery of catalyst - Google Patents

On-line equipment for magnetic separation and recovery of catalyst Download PDF

Info

Publication number
CN2611040Y
CN2611040Y CN 03241341 CN03241341U CN2611040Y CN 2611040 Y CN2611040 Y CN 2611040Y CN 03241341 CN03241341 CN 03241341 CN 03241341 U CN03241341 U CN 03241341U CN 2611040 Y CN2611040 Y CN 2611040Y
Authority
CN
China
Prior art keywords
catalyst
connects
outlet
automatic feeder
recovering
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
Application number
CN 03241341
Other languages
Chinese (zh)
Inventor
樊福生
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN 03241341 priority Critical patent/CN2611040Y/en
Application granted granted Critical
Publication of CN2611040Y publication Critical patent/CN2611040Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

The utility model discloses an accelerant online magnetic recycling separator including a magnetic separator, the feeding end of the magnetic separator is connected with a cooling device, the inlet of the cooling device is connected with a feeding pipe, a recycling accelerant discharging end of the magnetic separator is connected with an automatic feeder, the outlet of the automatic feeder is connected with a circulating pipe, a fouled accelerant outlet of the magnetic separator is connected with the automatic feeder, the outlet of the automatic feeder is connected with the fouled accelerant container. The accelerant recycling efficiency is high. The utility model applies to accelerant separating and recycling of all popular catalytic cracker of different processing capacity. The utility model online automatically separates and recycles equilibrium catalyst, optimizes catalytic cracker performance, improves and increases equilibrium catalyst integral activity and selectivity of catalytic cracker, increases conversion rate and light oil absorption rate, saves fresh accelerant amount and improves economic benefit of catalytic cracker.

Description

The online magnetic separating and recovering of catalyst device
Technical field
The utility model belongs to the device in the petroleum catalytic cracking production process, is specifically related to the device of the continuous magnetic separating and recovering of catalyst.
Background technology
The quality of oil catalytic cracking unit operating condition depends on to a great extent whether it can optimize various operating parameters highly automated, continuously.At present, the magnetism separate method of catalyst is: the catalyst in the regenerator by manually being transported to magnetic separator place, separates after cooling off naturally again, uses by manually the catalyst of regeneration being transported back after the separation again.This method efficient is low, and the cycle is long, the cost height.
Summary of the invention
The purpose of this utility model is to provide a kind of device, and this device can be realized the on-line continuous of catalyst, carry out that magnetic separates and reuse automatically.
The utility model is achieved in that the online magnetic separating and recovering of catalyst device comprises magnetic separator, the feed end of magnetic separator connects cooling device, the import of cooling device connects feed pipe, the reuse of catalyst discharge end of magnetic separator connects automatic feeder, the outlet of this automatic feeder connects circulation pipe, the dead catalyst outlet of magnetic separator connects automatic feeder, and the outlet of this automatic feeder connects the dead catalyst storage tank.
This device has been realized serialization, the automation that catalyst magnetic separates, can with former catalytic cracking unit synchronous operation.Catalyst separation reuse efficient height, cost is low.Be applicable to the catalyst separation reuse of all fluidized catalytic crackers that disposal ability varies in size.The feed pipe of this device can be connected use with regenerator, settler, poising agent jar etc.After using this device to realize linearize again, can finish the separation and the reuse of poising agent automatically, optimize the technology of catalytic cracking unit, improve the overall activity and the selectivity of operation poising agent in the catalytic cracking unit, improve conversion ratio and yield of light oil, save the consumption of fresh catalyst, improve the economic benefit of catalytic cracking unit
Description of drawings
The online magnetic separating and recovering of Fig. 1 catalyst apparatus structure I schematic diagram
The online magnetic separating and recovering of Fig. 2 catalyst apparatus structure II schematic diagram
Fig. 3 poising agent cooler construction schematic diagram
Fig. 4 poising agent tank structure schematic diagram
The online magnetic separating and recovering of Fig. 5 catalyst device application example 1 schematic diagram
The online magnetic separating and recovering of Fig. 6 catalyst device application example 2 schematic diagrames
The online magnetic separating and recovering of Fig. 7 catalyst device application example 3 schematic diagrames
The online magnetic separating and recovering of Fig. 8 catalyst device application example 4 schematic diagrames
The online magnetic separating and recovering of Fig. 9 catalyst device application example 5 schematic diagrames
The online magnetic separating and recovering of Figure 10 catalyst device application example 6 schematic diagrames
The specific embodiment
As shown in Figure 1, the feed end of magnetic separator 4 connects equilibrium catalyst storage tank 3, and the outlet of equilibrium catalyst cooler 2 connects equilibrium catalyst storage tank 3 by pipeline 20.The reuse of catalyst discharge end of magnetic separator 4 connects automatic feeder 5.1, the outlet of automatic feeder 5.1 connects circulation pipe 21, the dead catalyst outlet of magnetic separator 4 connects automatic feeder 5.2, and the outlet of automatic feeder 5.2 connects dead catalyst storage tank 6 by pipeline 22.Connect control valve 7 on the feed pipe 23, control valve is a guiding valve.
As shown in Figure 2, the feed end of magnetic separator 4 connects equilibrium catalyst storage tank 3, and the outlet of automatic charging equipment 5.3 connects equilibrium catalyst storage tank 3 by pipeline 24.The reuse of catalyst discharge end of magnetic separator 4 connects automatic feeder 5.1, the outlet of automatic feeder 5.1 connects circulation pipe 21, the dead catalyst outlet of magnetic separator 4 connects automatic feeder 5.2, and the outlet of automatic feeder 5.2 connects dead catalyst storage tank 6 by pipeline 22.
As shown in Figure 3, poising agent cooler 2 can adopt various types of bundled tube coolings.The tube bank cooler of present embodiment comprises horizontal tank body 2.1, offers poising agent charging aperture 2.4 on the tank skin on the horizontal tank body 2.1, air outlet 2.5; Offer air inlet 2.6 on 2.1 times tank skins of horizontal tank body, poising agent outlet 2.7.Horizontal tank body 2.1 1 ends connect bobbin carriage 2.3, establish dividing plate 2.8 in the bobbin carriage 2.3, and dividing plate 2.8 is divided into two chambeies up and down with bobbin carriage.2.3 times tank walls of bobbin carriage are offered cooling water inlet 2.9, and tank wall sets out the mouth of a river 2.10 on the bobbin carriage 2.3.Cooler bundle 2.2 1 ends that are provided with in the horizontal tank body 2.1 communicate with bobbin carriage 2.3 cavity of resorptions, and cooler bundle 2.2 other ends and bobbin carriage 2.3 epicoele casees are logical.
As shown in Figure 4, equilibrium catalyst storage tank 3 comprises tank body 3.1, the air-distribution device of establishing in the tank body 3.1, the air-distribution device can be the structure of annular or branch shape, the air-distribution device of present embodiment is included in the annular air pipe 3.2 that tank body 3.1 bottoms are provided with, the Lower Half of annular air pipe 3.2 is opened distribution venthole 3.3, and (shown in Fig. 4 b) annular air pipe 3.2 taps into tracheae 3.4.Tank body 3.1 tops connect cyclone separator 3.5, and the discharging opening 3.6 of cyclone separator 3.5 communicates with tank body 3.1.
Magnetic separator 4 can be adopted electromagnetic separator or the rare earth permanent magnet seperator of selling on the existing market.Automatic feeder 5.1,5.2 can adopt the small-sized automatic feeder of the catalyst of selling on the existing market.
This device can be used in multiple petroleum catalytic cracking production system.As shown in Figure 5, the device of Fig. 1 is used for not being provided with the regeneration catalyzing cracking unit of external warmer.Feed pipe 23 is connected with regenerator 1.Circulation pipe 21 is connected with regenerator 1.
As shown in Figure 6, the device of Fig. 1 is used for being provided with the regeneration catalyzing cracking unit of external warmer.Feed pipe 23 is connected with the outlet of regenerator 1 and external warmer 10.Circulation pipe 21 is connected with regenerator 1.Boiler water is adopted in the water inlet of balancing machine cooler, and water outlet is used for external warmer.
Shown in 7, the device of Fig. 1 is used for two-stage regeneration and do not have the catalytic cracking unit of external warmer.Feed pipe 23 is connected with regenerator 1, and circulation pipe 21 is connected with regenerator 11.
As shown in Figure 8, the device of Fig. 1 is used for two-stage regeneration and the catalytic cracking unit of external warmer is arranged.Feed pipe 23 is connected with the outlet of regenerator 1 and external warmer 10.Circulation pipe 21 is connected with regenerator 11.Boiler water is adopted in the water inlet of poising agent cooler, and water outlet is used for external warmer.
As shown in Figure 9, the device with Fig. 1 is used for one section or two-stage regeneration catalytic cracking unit.Feed pipe 23 is connected with settler 14, and circulation pipe 21 is connected with regenerator 11.
As shown in figure 10, the device with Fig. 2 is used for the little small-sized catalytic cracking unit of disposal ability.Feed pipe 24 is connected with poising agent jar 15, and circulation pipe 21 is connected with regenerator 11.

Claims (7)

1, the online magnetic separating and recovering of a kind of catalyst device, it comprises magnetic separator, the feed end that it is characterized in that magnetic separator connects cooling device, the import of cooling device connects feed pipe, the reuse of catalyst discharge end of magnetic separator connects automatic feeder, the outlet of this automatic feeder connects circulation pipe, and the dead catalyst outlet of magnetic separator connects automatic feeder, and the outlet of this automatic feeder connects the dead catalyst storage tank.
2, the online magnetic separating and recovering of catalyst device according to claim 1, it is characterized in that cooling device comprises flat Chang catalyst cooler, the outlet of flat Chang catalyst cooler connects the equilibrium catalyst storage tank by pipeline, and the outlet of equilibrium catalyst storage tank connects magnetic separator.
3, as the online magnetic separating and recovering of catalyst device as described in the claim 2, it is characterized in that the equilibrium catalyst storage tank comprises tank body, the air-distribution device of establishing in the tank body, the tank body top connects cyclone separator, and the discharging opening of cyclone separator communicates with tank body.
4, as the online magnetic separating and recovering of catalyst device as described in the claim 3, it is characterized in that the air-distribution device in the tank body comprises the air-distribution pipe that is located at the tank body bottom, the Lower Half of air-distribution pipe is opened the distribution venthole, and the air-distribution pipe connects air inlet pipe.
5. as the online magnetic separating and recovering of catalyst device as described in the claim 4, it is characterized in that the air-distribution pipe is annular or dendroid.
6, the online magnetic separating and recovering of catalyst device according to claim 1 is characterized in that connecting on the feed pipe feeding device, and the discharging opening of feeding device connects the equilibrium catalyst storage tank.
7, the online magnetic separating and recovering of catalyst device according to claim 1 is characterized in that connecting on the feed pipe control valve.
CN 03241341 2003-04-22 2003-04-22 On-line equipment for magnetic separation and recovery of catalyst Expired - Fee Related CN2611040Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 03241341 CN2611040Y (en) 2003-04-22 2003-04-22 On-line equipment for magnetic separation and recovery of catalyst

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 03241341 CN2611040Y (en) 2003-04-22 2003-04-22 On-line equipment for magnetic separation and recovery of catalyst

Publications (1)

Publication Number Publication Date
CN2611040Y true CN2611040Y (en) 2004-04-14

Family

ID=34168403

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 03241341 Expired - Fee Related CN2611040Y (en) 2003-04-22 2003-04-22 On-line equipment for magnetic separation and recovery of catalyst

Country Status (1)

Country Link
CN (1) CN2611040Y (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105861307A (en) * 2016-05-13 2016-08-17 山东师范大学 Production device of magnetically-recyclable biological enzymes suitable for industrialized application

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105861307A (en) * 2016-05-13 2016-08-17 山东师范大学 Production device of magnetically-recyclable biological enzymes suitable for industrialized application
CN105861307B (en) * 2016-05-13 2018-08-28 山东师范大学 Suitable for industrial applications can magnetic recovery biological enzyme process units

Similar Documents

Publication Publication Date Title
CN108949508B (en) Fermentation tank waste heat recovery system and waste heat recovery process
CN2611040Y (en) On-line equipment for magnetic separation and recovery of catalyst
CN203728569U (en) Hydrogen generating reactor employing aluminum water
CN203061162U (en) Heterogeneous catalysis reaction separating-coupling device
CN104098424A (en) Continuous reaction process utilizing methanol conversion to prepare hydrocarbon mixture and reactor
CN2652503Y (en) Iron remover from slurry
CN202898283U (en) Major catalyst recycling device for preparing polyolefin
CN101168137A (en) System and method for regenerating reactivating and recovering FCC balance catalyst
CN2303853Y (en) Gas cleaning and recovering apparatus
CN2331418Y (en) Stepped resin separating unit
CN218608699U (en) Tail gas recovery processing system in chemical product preparation process
CN211665132U (en) Cooling circulation mechanism of steel wire quenching liquid for overhead transmission line
CN218944689U (en) Device for recovering yellow phosphorus from yellow phosphorus furnace gas
CN109232878A (en) A kind of purification process of polyglycol ether
CN204211486U (en) The extracting and purifying system of hydrogen peroxide
CN202246045U (en) Hydrogen-nitrogen replacement device with vacuum pump of high-purity hydrogen purification device
CN202961989U (en) Sedimentation device
CN217041932U (en) Exhaust treatment device for oil depot
CN218454004U (en) Alumina evaporation secondary backwater processing apparatus
CN213958728U (en) Automatic oil filtering circulation station for transformer oil
CN1433839A (en) Large scale vortex magnetic separation integrating separator for catalyzing dehydrogen desulfurization device
CN213609838U (en) Device for recycling industrial hydraulic waste oil
CN212237328U (en) Fluidized resin bed
CN218539307U (en) Container type ethanol hydrogen production device
CN110003960B (en) Natural gas preparation system and integrated skid-mounted natural gas preparation system

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20040414

Termination date: 20120422