CN112057929B - Method for automatically separating and recycling solid catalyst in liquid reaction - Google Patents

Method for automatically separating and recycling solid catalyst in liquid reaction Download PDF

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Publication number
CN112057929B
CN112057929B CN202010929955.0A CN202010929955A CN112057929B CN 112057929 B CN112057929 B CN 112057929B CN 202010929955 A CN202010929955 A CN 202010929955A CN 112057929 B CN112057929 B CN 112057929B
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Prior art keywords
liquid
filter cloth
reaction
solid
reaction kettle
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CN112057929A (en
Inventor
康登海
李珣珣
周新基
陆铮铮
夏俊维
朱德均
林明明
周云霞
沈鑫鑫
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Jiangsu Jiujiujiu Technology Co ltd
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Jiangsu Jiujiujiu Technology Co ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/11Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
    • B01D29/13Supported filter elements
    • B01D29/23Supported filter elements arranged for outward flow filtration
    • B01D29/27Filter bags
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/584Recycling of catalysts

Abstract

The invention discloses a method for automatically separating and recycling a solid catalyst in liquid reaction.A cylindrical steel wire mesh is distributed and fixed on the inner wall of a reaction kettle, cylindrical filter cloth tightly attached to the inner wall of the cylindrical steel wire mesh is arranged in the reaction kettle, and the filter cloth is fixed with the steel wire mesh; the cloth filtering ports in the reaction kettle are distributed along the anticlockwise direction, and the stirring in the kettle is carried out along the anticlockwise direction in the system reaction process; after the reaction is finished, changing the stirring direction into clockwise rotation; the separated liquid is discharged from the reaction kettle and keeps rotating clockwise; when new unreacted liquid is replenished into the reaction kettle, the stirring is adjusted to be anticlockwise rotated, the catalyst solid in the filter cloth bag is washed by the flowing of the liquid to be mixed into the liquid, and the anticlockwise rotation is kept until the reaction is finished. The invention can effectively separate the solid and the liquid of the system in the reaction kettle, and can ensure that the operation of recycling the solid catalyst becomes simpler and more convenient.

Description

Method for automatically separating and recycling solid catalyst in liquid reaction
Technical Field
The invention relates to a method for automatically separating and recycling a solid catalyst in liquid reaction.
Background
In the liquid reaction system, the operation of recycling the solid substance as a catalyst after the completion of the reaction is very complicated, and the effect is not satisfactory.
Disclosure of Invention
The invention aims to provide a method for automatically separating and recycling a solid catalyst in a liquid reaction, which can effectively separate the solid from the liquid in a reaction kettle and can simplify and facilitate the recycling operation of the solid catalyst.
The technical solution of the invention is as follows:
a method for automatically separating and recycling a solid catalyst in liquid reaction is characterized in that: the inner wall of the reaction kettle is uniformly distributed and fixed with a cylindrical steel wire mesh, cylindrical filter cloth tightly attached to the inner wall of the cylindrical steel wire mesh is arranged in the cylindrical steel wire mesh, and the filter cloth is fixed with the steel wire mesh and is prevented from deforming along with the flow of liquid in the reaction kettle;
the cloth filtering ports in the reaction kettle are distributed along the anticlockwise direction, in the reaction process of the system, the stirring in the kettle is stirred along the anticlockwise direction, and the solid catalyst is dispersed in the system and cannot enter the cloth filtering bag; after the reaction is finished, the stirring direction is changed into clockwise rotation, the solid catalyst enters the filter bag from the filter cloth opening along with the liquid, the liquid flows out of the filter cloth by using the driving force of stirring, and the solid is blocked by the filter cloth and is left in the filter cloth bag; the liquid flows along one direction and has a driving force provided by stirring, and the solid in the filter cloth bag cannot reversely flow out, so that the liquid continuously containing the catalyst solid enters, is separated by the filter cloth, the solid is left, and the liquid flows out until the liquid does not contain the catalyst solid; when the separated liquid is discharged from the reaction kettle, the clockwise rotation is also kept, so that the catalyst in the filter cloth bag is prevented from flowing out;
when new unreacted liquid is replenished in the reaction kettle, the stirring is adjusted to be anticlockwise rotated, the catalyst solid in the filter cloth bag is flushed by utilizing the flow of the liquid to be mixed into the liquid, and the anticlockwise rotation is kept until the reaction is finished.
The method does not need additional filtering equipment, can effectively separate the solid and the liquid of the system in the reaction kettle, and can ensure that the operation of recycling the solid catalyst becomes simpler and more convenient.
Drawings
The invention is further illustrated by the following figures and examples.
FIG. 1 is a schematic view of the structure of a reaction vessel. Wherein 1, a filter cloth bag; 2. steel wire mesh; 3. the inner wall of the reaction kettle;
fig. 2 is a schematic side view of a filter cloth bag.
Fig. 3 is a schematic cross-sectional view of a filter cloth bag.
Fig. 4, 5 and 6 are schematic diagrams of the working states at different stages.
In fig. 5: 4. the liquid flows out through the filter cloth bag; 5. the bag mouth direction of the filter cloth; 6, remaining the solid catalyst in the filter cloth bag; 7. the direction of stirring.
In fig. 6: 8. the direction of the mouth of the filter cloth bag; 9. liquid enters the direction of the filter cloth bag; 10. the solid catalyst flows out of the filter bag along with the liquid; 11. the direction of stirring.
Detailed Description
A method for automatically separating and recycling a solid catalyst in a liquid reaction comprises the steps that a cylindrical steel wire mesh 2 is uniformly distributed and fixed on the inner wall of a reaction kettle 3, cylindrical filter cloth 1 attached to the inner wall of the cylindrical steel wire mesh is arranged in the cylindrical steel wire mesh, and the filter cloth is fixed with the steel wire mesh and is prevented from deforming along with the flowing of liquid in the reaction kettle (as shown in figures 1, 2 and 3);
the cloth filtering ports in the reaction kettle are distributed along the counterclockwise direction, in the reaction process of the system, the stirring in the kettle is stirred along the counterclockwise direction, and the solid catalyst is dispersed in the system and cannot enter the cloth filtering bag (as shown in figure 4).
After the reaction is finished, the stirring direction is changed into clockwise rotation, the solid catalyst enters the filter bag from the filter cloth opening along with the liquid, the liquid flows out of the filter cloth by using the driving force of stirring, and the solid is blocked by the filter cloth and is left in the filter cloth bag; the liquid flows along one direction and has a driving force provided by stirring, and the solid in the filter cloth bag cannot reversely flow out, so that the liquid continuously containing the catalyst solid enters, is separated by the filter cloth, the solid is left, and the liquid flows out until the liquid does not contain the catalyst solid; the separated liquid is discharged from the reaction kettle while being kept rotating clockwise to prevent the catalyst in the filter cloth bag from flowing out (as shown in fig. 5).
When new unreacted liquid is replenished into the reaction kettle, the stirring is adjusted to be anticlockwise rotated, the catalyst solid in the filter cloth bag is washed by the flowing of the liquid to be mixed into the liquid, and the anticlockwise rotation is kept until the reaction is finished (as shown in figure 6).

Claims (1)

1. A method for automatically separating and recycling a solid catalyst in liquid reaction is characterized in that: the inner wall of the reaction kettle is uniformly distributed and fixed with a cylindrical steel wire mesh, cylindrical filter cloth tightly attached to the inner wall of the cylindrical steel wire mesh is arranged in the cylindrical steel wire mesh, and the filter cloth is fixed with the steel wire mesh and is prevented from deforming along with the flow of liquid in the reaction kettle;
the cloth filtering ports in the reaction kettle are distributed along the anticlockwise direction, in the reaction process of the system, the stirring in the kettle is stirred along the anticlockwise direction, and the solid catalyst is dispersed in the system and cannot enter the cloth filtering bag; after the reaction is finished, the stirring direction is changed into clockwise rotation, the solid catalyst enters the filter bag from the filter cloth opening along with the liquid, the liquid flows out of the filter cloth by using the driving force of stirring, and the solid is blocked by the filter cloth and is left in the filter cloth bag; the liquid flows along one direction and has a driving force provided by stirring, and the solid in the filter cloth bag cannot flow out reversely, so that the liquid containing the catalyst solid enters, and is separated by the filter cloth, the solid is left, and the liquid flows out; when the separated liquid is discharged from the reaction kettle, the clockwise rotation is also kept, so that the catalyst in the filter cloth bag is prevented from flowing out;
when new unreacted liquid is replenished into the reaction kettle, the stirring is adjusted to be anticlockwise rotated, the catalyst solid in the filter cloth bag is washed by the flowing of the liquid to be mixed into the liquid, and the anticlockwise rotation is kept until the reaction is finished.
CN202010929955.0A 2020-09-07 2020-09-07 Method for automatically separating and recycling solid catalyst in liquid reaction Active CN112057929B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010929955.0A CN112057929B (en) 2020-09-07 2020-09-07 Method for automatically separating and recycling solid catalyst in liquid reaction

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Application Number Priority Date Filing Date Title
CN202010929955.0A CN112057929B (en) 2020-09-07 2020-09-07 Method for automatically separating and recycling solid catalyst in liquid reaction

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CN112057929A CN112057929A (en) 2020-12-11
CN112057929B true CN112057929B (en) 2022-05-31

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101711965A (en) * 2008-10-06 2010-05-26 大成生化科技集团有限公司 Systems and methods for continuous multiphase reaction and separation
CN203764270U (en) * 2014-03-12 2014-08-13 江苏恒安化工有限公司 Device capable of preventing solvent volatilization and fast recovering palladium and carbon
CN105218299A (en) * 2015-09-30 2016-01-06 巨化集团技术中心 A kind of continuous production method for tetracol phenixin and olefin production hydrochloric ether
CN207153705U (en) * 2017-08-28 2018-03-30 新能能源有限公司 A kind of reactor with solid-liquid separation function
CN110252229A (en) * 2019-05-31 2019-09-20 陈小勇 A kind of chemical production equipment reaction kettle
CN210874847U (en) * 2019-08-26 2020-06-30 龙净科杰环保技术(上海)有限公司 Useless SCR catalyst recovery processing device

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101711965A (en) * 2008-10-06 2010-05-26 大成生化科技集团有限公司 Systems and methods for continuous multiphase reaction and separation
CN203764270U (en) * 2014-03-12 2014-08-13 江苏恒安化工有限公司 Device capable of preventing solvent volatilization and fast recovering palladium and carbon
CN105218299A (en) * 2015-09-30 2016-01-06 巨化集团技术中心 A kind of continuous production method for tetracol phenixin and olefin production hydrochloric ether
CN207153705U (en) * 2017-08-28 2018-03-30 新能能源有限公司 A kind of reactor with solid-liquid separation function
CN110252229A (en) * 2019-05-31 2019-09-20 陈小勇 A kind of chemical production equipment reaction kettle
CN210874847U (en) * 2019-08-26 2020-06-30 龙净科杰环保技术(上海)有限公司 Useless SCR catalyst recovery processing device

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