CN203316132U - Reaction kettle for producing catalysts - Google Patents

Reaction kettle for producing catalysts Download PDF

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Publication number
CN203316132U
CN203316132U CN2013202875297U CN201320287529U CN203316132U CN 203316132 U CN203316132 U CN 203316132U CN 2013202875297 U CN2013202875297 U CN 2013202875297U CN 201320287529 U CN201320287529 U CN 201320287529U CN 203316132 U CN203316132 U CN 203316132U
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CN
China
Prior art keywords
kettle
rotating shaft
main body
frequency motor
kettle body
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
CN2013202875297U
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Chinese (zh)
Inventor
王震宇
王立君
刘雁
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.)
TIANJIN SHENNENG SCIENCE AND TECHNOLOGY Co Ltd
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TIANJIN SHENNENG SCIENCE AND TECHNOLOGY 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.)
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Publication date
Application filed by TIANJIN SHENNENG SCIENCE AND TECHNOLOGY Co Ltd filed Critical TIANJIN SHENNENG SCIENCE AND TECHNOLOGY Co Ltd
Priority to CN2013202875297U priority Critical patent/CN203316132U/en
Application granted granted Critical
Publication of CN203316132U publication Critical patent/CN203316132U/en
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Expired - Fee Related legal-status Critical Current

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    • 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
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

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  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

The utility model provides a reaction kettle for producing catalysts. The reaction kettle comprises a kettle body and a kettle cover, wherein the kettle body is movably connected with the kettle cover; the kettle cover is provided with an exhaust port; a rotating shaft is arranged at the center of the inside bottom surface of the kettle body; a reaction cabin is arranged at the top of the rotating shaft; the bottom of the reaction cabin is hemispherical; a two-way variable frequency motor is arranged at the bottom of the outer wall of the kettle body and is connected with the rotating shaft by a driving belt; a control panel is arranged on the outer wall of the kettle body; heating devices are arranged on the inner walls on two sides of the kettle body; the heating devices and the two-way variable frequency motor are controlled by the control panel; the heating devices are infrared heating devices. The reaction kettle has the beneficial effects that the equipment has a simple structure, is simple and convenient to use and can mix the raw materials of the catalysts uniformly, improve the product quality and reduce processes, thus improving the production efficiency.

Description

A kind of reactor for Catalyst Production
(1) technical field
The utility model relates to a kind of chemical production equipment, particularly relates to a kind of reactor for Catalyst Production.
(2) background technology
At present, in the production process of catalyst, the mechanical mixing controlling catalyst is a kind of making catalyst method that range of application is the widest.When making catalyst by this method, the uppity reason of rotary speed due to used reaction kettle for reaction storehouse, be easy to cause the spheroid situation generation not uniformly of making, the catalyst of producing can be because inhomogeneous its product quality that makes of mixing can not be up to standard, simultaneously, owing to using the mechanical mixing controlling catalyst to need mixed-forming, drying, the several steps of calcining, each procedure all needs different equipment, comparatively loaded down with trivial details, production efficiency is low.Thereby now can make on the market the reactor for Catalyst Production of the evenly mixing of catalyst raw material, Improving The Quality of Products, minimizing operation improving production efficiency also not be found, have to be developed.
(3) utility model content
In order to overcome the weak point of existing chemical production equipment, the utility model provides a kind of reactor for Catalyst Production.
The technical solution of the utility model is to realize like this.
A kind of reactor for Catalyst Production of this programme, comprise still body main body and kettle cover, and described still body main body and kettle cover are flexibly connected; Be provided with exhaust outlet on described kettle cover; Described still body body interior bottom center is provided with rotating shaft, and this rotating shaft top is provided with reaction warehouse, and this reaction warehouse bottom is hemispherical; Described still body main body outer wall bottom is provided with two-way variable-frequency motor, and this two-way variable-frequency motor is connected by driving-belt with rotating shaft; Described still body main body outer wall is provided with control panel; Described still body main body both sides inwall is provided with heater; Described heater, two-way variable-frequency motor are controlled by control panel.
Described heater is infrared heating device.
Usefulness of the present utility model is: this device structure is simple, easy to use, can make the catalyst raw material evenly mix, Improving The Quality of Products, thus reduce the operation improving production efficiency.
(4) accompanying drawing explanation
Fig. 1 is institutional framework schematic diagram of the present utility model.
(5) specific embodiment
Below in conjunction with accompanying drawing, the specific embodiment of the present utility model is made to brief description.
A kind of reactor for Catalyst Production as shown in Figure 1, comprise still body main body 1 and kettle cover 2, and described still body main body 1 and kettle cover 2 are flexibly connected; Be provided with exhaust outlet 8 on described kettle cover 2; Described still body main body 1 inner bottom surface center is provided with rotating shaft 3, and these rotating shaft 3 tops are provided with reaction warehouse 5, and these reaction warehouse 5 bottoms are hemispherical; Described still body main body 1 outer wall bottom is provided with two-way variable-frequency motor 4, and this two-way variable-frequency motor 4 is connected by driving-belt with rotating shaft 3; Described still body main body 1 outer wall is provided with control panel 6; Described still body main body 1 both sides inwall is provided with heater 7; Described heater 7, two-way variable-frequency motor 4 are controlled by control panel 6.
Described heater 7 is infrared heating device.
The course of work of this example: while using this equipment to carry out Catalyst Production, first raw material is poured in the reaction warehouse 5 in still body main body 1, cover kettle cover 2, open exhaust outlet 8, control the rotating speed of variable-frequency motor 4 and turn to by control panel 6, variable-frequency motor break-in is at set intervals rotated, it is more accurate that this method is controlled rotating speed, by covert rotation, also make the raw material in reaction warehouse 5 mix more abundant simultaneously, thereby Improving The Quality of Products, after mixing, the catalyst spheroid started in 7 pairs of reaction warehouses of heater 5 by control panel 6 carries out drying, saved the catalyst spheroid has been taken out to dry separately operation in reactor, simultaneously because heater 7 is infrared heating device, temperature control is more accurate, heat more even, improving production efficiency.
Above an embodiment of the present utility model is had been described in detail, but described content is only preferred embodiment of the present utility model, can not be considered to for limiting practical range of the present utility model.All equalization variations of doing according to the utility model application range and improvement etc., within all should still belonging to patent covering scope of the present utility model.

Claims (2)

1. the reactor for Catalyst Production, comprise still body main body (1) and kettle cover (2), it is characterized in that: described still body main body (1) and kettle cover (2) are flexibly connected; Be provided with exhaust outlet (8) on described kettle cover (2); Described still body main body (1) inner bottom surface center is provided with rotating shaft (3), and this rotating shaft (3) top is provided with reaction warehouse (5), and this reaction warehouse (5) bottom is hemispherical; Described still body main body (1) outer wall bottom is provided with two-way variable-frequency motor (4), and this two-way variable-frequency motor (4) is connected by driving-belt with rotating shaft (3); Described still body main body (1) outer wall is provided with control panel (6); Described still body main body (1) both sides inwall is provided with heater (7); Described heater (7), two-way variable-frequency motor (4) are controlled by control panel (6).
2. a kind of reactor for Catalyst Production according to claim 1, it is characterized in that: described heater (7) is infrared heating device.
CN2013202875297U 2013-05-24 2013-05-24 Reaction kettle for producing catalysts Expired - Fee Related CN203316132U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2013202875297U CN203316132U (en) 2013-05-24 2013-05-24 Reaction kettle for producing catalysts

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2013202875297U CN203316132U (en) 2013-05-24 2013-05-24 Reaction kettle for producing catalysts

Publications (1)

Publication Number Publication Date
CN203316132U true CN203316132U (en) 2013-12-04

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2013202875297U Expired - Fee Related CN203316132U (en) 2013-05-24 2013-05-24 Reaction kettle for producing catalysts

Country Status (1)

Country Link
CN (1) CN203316132U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105268390A (en) * 2014-06-26 2016-01-27 东至天孚化工有限公司 Sealed reaction kettle
CN106179056A (en) * 2016-08-31 2016-12-07 无锡东恒新能源科技有限公司 A kind of high viscosity carbon nano tube paste preparation system
CN106179058A (en) * 2016-08-31 2016-12-07 无锡东恒新能源科技有限公司 A kind of carbon nano tube paste preparation system
CN106345354A (en) * 2016-12-03 2017-01-25 百奥森(江苏)食品安全科技有限公司 Vortex mixer

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105268390A (en) * 2014-06-26 2016-01-27 东至天孚化工有限公司 Sealed reaction kettle
CN106179056A (en) * 2016-08-31 2016-12-07 无锡东恒新能源科技有限公司 A kind of high viscosity carbon nano tube paste preparation system
CN106179058A (en) * 2016-08-31 2016-12-07 无锡东恒新能源科技有限公司 A kind of carbon nano tube paste preparation system
CN106345354A (en) * 2016-12-03 2017-01-25 百奥森(江苏)食品安全科技有限公司 Vortex mixer

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20131204

Termination date: 20160524

CF01 Termination of patent right due to non-payment of annual fee