CN202638410U - Catalyst recycling recovery system - Google Patents

Catalyst recycling recovery system Download PDF

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Publication number
CN202638410U
CN202638410U CN 201220236209 CN201220236209U CN202638410U CN 202638410 U CN202638410 U CN 202638410U CN 201220236209 CN201220236209 CN 201220236209 CN 201220236209 U CN201220236209 U CN 201220236209U CN 202638410 U CN202638410 U CN 202638410U
Authority
CN
China
Prior art keywords
pressure reactor
catalyst
surge tank
storage tank
recovery system
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 - Lifetime
Application number
CN 201220236209
Other languages
Chinese (zh)
Inventor
邱志刚
雍成松
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.)
Jiangsu Kangheng Chemical Co Ltd
Original Assignee
Jiangsu Kangheng Chemical Co Ltd
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 Jiangsu Kangheng Chemical Co Ltd filed Critical Jiangsu Kangheng Chemical Co Ltd
Priority to CN 201220236209 priority Critical patent/CN202638410U/en
Application granted granted Critical
Publication of CN202638410U publication Critical patent/CN202638410U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model relates to a catalyst recycling recovery system which comprises a pressure reactor and a storage tank. The storage tank is communicated with the pressure reactor through a material discharging pipe, and an inlet of the material discharging pipe is inserted to the lower portion of the pressure reactor. The catalyst is characterized by further comprising a buffer tank which is connected on the material discharging pipe in series, a material feeding back pipe is arranged at the bottom of the buffer tank, and the material feeding back pipe is communicated with a material pipe of the pressure reactor. The buffer tank is arranged on the material discharging pipe to be used to precipitate catalysts, and the catalysts are prevented from entering into a next working process after entering into the storage tank. After the catalysts are precipitated by the buffer tank, a valve can be used to cut off the connection between the buffer tank and the storage tank, the material feeding back pipe and the material pipe are communicated, so that materials which contain the catalysts enter into the pressure reactor again, and then the catalysts are recycled.

Description

A kind of catalyst recycling recovery system
Technical field
The utility model relates to a kind of catalyst recycling recovery system, particularly a kind of catalyst recycling recovery system of avoiding line clogging, improving catalyst utilization.
Background technology
In Chemical Manufacture, usually use the stress reaction that catalyst carries out material, for example the reaction of ortho-nitrochlorobenzene, ortho-nitraniline.In reaction, material and catalyst place pressure reacting container, and pressure reacting container is communicated with storage tank by drainage conduit.When utilizing pressure to discharge material, need to staticly settle catalyst, open again the valve of drainage conduit and discharge material.Usually because precipitation is not thorough, cause the catalyst of suspension to enter next procedure, thus blocking pipe, material pump and condenser, and not only impact is normal produces, and also has certain potential safety hazard.
Summary of the invention
The technical problems to be solved in the utility model provides a kind of catalyst recycling recovery system of avoiding line clogging, improving catalyst utilization.
For solving the problems of the technologies described above, the technical solution of the utility model is: a kind of catalyst recycling recovery system, comprise pressure reactor, storage tank, described storage tank is communicated with by drainage conduit with pressure reactor, the bottom of pressure reactor is stretched in the import of described drainage conduit, and its innovative point is: also comprise a surge tank, described surge tank is serially connected on the drainage conduit, the bottom of described surge tank is provided with the feed back pipe, and described feed back pipe is communicated with the materail tube of pressure reactor.
Further, the bottom of described surge tank is back taper.
Further, in the described surge tank paddle is set.
The utility model has the advantage of: in drainage conduit one surge tank is set, is used for precipitated catalyst, enter next procedure after avoiding catalyst to enter storage tank.After the surge tank precipitated catalyst, can cut off being connected of surge tank and storage tank by valve, connect feed back pipe and materail tube, again enter in the pressure reactor so that contain the material of catalyst, thereby recycle catalyst.
Description of drawings
Fig. 1 is the utility model catalyst recycling recovery system structural representation.
The specific embodiment
As shown in Figure 1, comprise pressure reactor 1, storage tank 2, drainage conduit 3, surge tank 4, feed back pipe 5.
Above-mentioned storage tank 2 is communicated with by drainage conduit 3 with pressure reactor 1, and the bottom of pressure reactor 1 is stretched in the import of drainage conduit 3.
Surge tank 4 is arranged between pressure reactor 1 and the storage tank 2, it is serially connected on the drainage conduit 3, and surge tank 4 bottoms are back taper, and paddle 7 is set in the tank body of surge tank 4, surge tank 4 bottoms are provided with feed back pipe 5, and feed back pipe 5 is communicated with the materail tube 6 of pressure reactor 1.
Operation principle: during discharge, the material in the pressure reactor 1 enters surge tank 4 and storage tank 2 by drainage conduit 3 under pressure, and when entering surge tank 4, most of catalyst can accumulate in the surge tank 4, and few the continuation enters storage tank 2 with material.When surge tank 4 inner catalysts gather more after, cut off being communicated with of surge tank 4 and storage tank 2 by valve, connect feed back pipe 5 and materail tube 6, so that material and catalyst in the surge tank 4 enter pressure reactor 1 again with feed back pipe 5, so that catalyst is fully used.

Claims (3)

1. catalyst recycling recovery system, comprise pressure reactor, storage tank, described storage tank is communicated with by drainage conduit with pressure reactor, the bottom of pressure reactor is stretched in the import of described drainage conduit, it is characterized in that: also comprise a surge tank, described surge tank is serially connected on the drainage conduit, and the bottom of described surge tank is provided with the feed back pipe, and described feed back pipe is communicated with the materail tube of pressure reactor.
2. catalyst recycling recovery system according to claim 1, it is characterized in that: the bottom of described surge tank is back taper.
3. catalyst recycling recovery system according to claim 1 is characterized in that: in the described surge tank paddle is set.
CN 201220236209 2012-05-24 2012-05-24 Catalyst recycling recovery system Expired - Lifetime CN202638410U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220236209 CN202638410U (en) 2012-05-24 2012-05-24 Catalyst recycling recovery system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220236209 CN202638410U (en) 2012-05-24 2012-05-24 Catalyst recycling recovery system

Publications (1)

Publication Number Publication Date
CN202638410U true CN202638410U (en) 2013-01-02

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201220236209 Expired - Lifetime CN202638410U (en) 2012-05-24 2012-05-24 Catalyst recycling recovery system

Country Status (1)

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CN (1) CN202638410U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103521142A (en) * 2013-11-05 2014-01-22 浙江华亿工程设计有限公司 Equipment and method for applying catalyst circularly and downwards

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103521142A (en) * 2013-11-05 2014-01-22 浙江华亿工程设计有限公司 Equipment and method for applying catalyst circularly and downwards
CN103521142B (en) * 2013-11-05 2015-05-27 浙江华亿工程设计有限公司 Equipment and method for applying catalyst circularly and downwards

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C14 Grant of patent or utility model
GR01 Patent grant
CX01 Expiry of patent term

Granted publication date: 20130102

CX01 Expiry of patent term