CN204320292U - A kind of reactor with cyclone separator - Google Patents

A kind of reactor with cyclone separator Download PDF

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Publication number
CN204320292U
CN204320292U CN201420735942.XU CN201420735942U CN204320292U CN 204320292 U CN204320292 U CN 204320292U CN 201420735942 U CN201420735942 U CN 201420735942U CN 204320292 U CN204320292 U CN 204320292U
Authority
CN
China
Prior art keywords
kettle
powder
cyclone separator
centrum
rise
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
CN201420735942.XU
Other languages
Chinese (zh)
Inventor
宗学清
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.)
ZIBO KUNHAN FINE CHEMICAL Co Ltd
Original Assignee
ZIBO KUNHAN FINE 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 ZIBO KUNHAN FINE CHEMICAL Co Ltd filed Critical ZIBO KUNHAN FINE CHEMICAL Co Ltd
Priority to CN201420735942.XU priority Critical patent/CN204320292U/en
Application granted granted Critical
Publication of CN204320292U publication Critical patent/CN204320292U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model provides a kind of reactor with cyclone separator, comprise kettle, the bottom of described kettle is provided with support, the lower center position of described kettle outside is provided with motor, the lower center position of described kettle inside is provided with shaft, the top of described shaft is provided with paddle, the bottom of described kettle is provided with discharging opening, the top of described kettle is provided with powder feed mouth, liquid material charge door and powder fall mouth after rise, the side of described powder feed mouth is provided with induced duct, the top of described kettle is provided with cyclone separator, described cyclone separator comprises centrum, the side of described centrum is provided with helical form inlet tube, the relative side of described centrum is provided with helical form outlet, the bottom of described centrum is provided with ash bucket, the bottom of described ash bucket is provided with powder and falls pipe after rise, described helical form outlet is provided with discharge pipe, described discharge pipe is provided with air-introduced machine.The beneficial effects of the utility model had both decreased the Dust Capacity be diffused in air, in turn ensure that raw material farthest effectively utilizes.

Description

A kind of reactor with cyclone separator
Technical field
The utility model belongs to petrochemical industry, especially relates to a kind of reactor with cyclone separator.
Background technology
Reactor is the conventional reaction unit of chemical technology field, in the reaction participated in there being granular material, need when feeding intake to throw powder from kettle dog-house, because material is merrily and lightheartedly tiny, especially easily loss evaporate in air, to environment, and can cause the waste of material, a kind of device that powder can be made to enter into reactor is completely also undiscovered, needs to be researched and developed further.
Utility model content
The purpose of this utility model is to provide the reactor with cyclone separator that a kind of structure is simple, simple to operate, production efficiency is high, is especially applicable to the reaction having powder to participate in.
The technical solution of the utility model is: a kind of reactor with cyclone separator of the present utility model, comprise kettle, the bottom of described kettle is provided with support, described support is fixedly connected with kettle, the lower center position of described kettle outside is provided with motor, the lower center position of described kettle inside is provided with shaft, shaft and motor are by electrical connection, the top of described shaft is provided with paddle, the bottom of described kettle is provided with discharging opening, the top of described kettle is provided with powder feed mouth, liquid material charge door and powder fall mouth after rise, described powder feed mouth, liquid material charge door and powder fall mouth after rise and kettle communicates, the side of described powder feed mouth is provided with induced duct, the top of described kettle is provided with cyclone separator, described cyclone separator comprises centrum, the side of described centrum is provided with helical form inlet tube, the relative side of described centrum is provided with helical form outlet, the bottom of described centrum is provided with ash bucket, the bottom of described ash bucket is provided with powder and falls pipe after rise, described ash bucket and powder fall pipe after rise and communicate, described powder falls pipe after rise and powder falling mouth communicates, described helical form inlet tube and induced duct communicate, described helical form outlet is provided with discharge pipe, described discharge pipe is provided with air-introduced machine, described air-introduced machine and discharge pipe communicate.
The material of described induced duct and discharge pipe is stainless steel.
Described paddle is provided with material feeding hole.
Described cyclone separator is between powder feed mouth and liquid material charge door.
The advantage that the utility model has and good effect are: this programme has structure advantage simple, simple to operate, due to the setting of cyclone separator, both the Dust Capacity be diffused in air had been decreased, in turn ensure that raw material farthest effectively utilizes, both do not pollute the environment, the waste of material can not be caused again, the stirring resistance that minimizing is set of material feeding hole, economize energy, induced duct and the discharge pipe of Stainless Steel material are corrosion-resistant, increase the service life.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure:
1, liquid material charge door 2, induced duct 3, kettle
4, shaft 5, support 6, motor
7, discharging opening 8, powder feed mouth 9, induced duct
10, helical form inlet tube 11, cyclone separator 12, helical form outlet
13, discharge pipe 14, air-introduced machine 15, centrum
16, ash bucket 17, powder fall pipe 18, powder falling mouth after rise
19, material feeding hole
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is elaborated.
As Fig. 1, shown in structural representation of the present utility model, a kind of reactor with cyclone separator of the present utility model, comprise kettle 3, the bottom of described kettle 3 is provided with support 5, described support 5 is fixedly connected with kettle 3, the lower center position of described kettle 3 outside is provided with motor 6, the lower center position of described kettle 3 inside is provided with shaft 4, shaft 4 and motor 6 are by electrical connection, the top of described shaft 4 is provided with paddle 2, the bottom of described kettle 3 is provided with discharging opening 7, the top of described kettle 3 is provided with powder feed mouth 8, liquid material charge door 1 and powder fall mouth 18 after rise, described powder feed mouth 8, liquid material charge door 1 and powder fall mouth 18 after rise and kettle 3 communicates, the side of described powder feed mouth 8 is provided with induced duct 9, the top of described kettle 3 is provided with cyclone separator 11, described cyclone separator 11 comprises centrum 15, the side of described centrum 15 is provided with helical form inlet tube 10, the relative side of described centrum 15 is provided with helical form outlet 12, the bottom of described centrum 15 is provided with ash bucket 16, the bottom of described ash bucket 16 is provided with powder and falls pipe 17 after rise, described ash bucket 16 and powder fall pipe 17 after rise and communicate, described powder falls pipe 17 after rise and powder falling mouth 18 communicates, described helical form inlet tube 10 and induced duct 9 communicate, described helical form outlet 12 is provided with discharge pipe 13, described discharge pipe 13 is provided with air-introduced machine 14, described air-introduced machine 14 and discharge pipe 13 communicate.
The material of described induced duct 9 and discharge pipe 13 is stainless steel.
Described paddle 2 is provided with material feeding hole 19.
Described cyclone separator 11 is between powder feed mouth 8 and liquid material charge door 1.
The course of work of this example: before feeding intake, first start air-introduced machine 14, powder adds in kettle 3 by powder feed mouth 8, solid material and liquid material add in kettle 3 by liquid material charge door 1, start motor 6 simultaneously, paddle 3 is under the effect of shaft 4, reaction mass is stirred, throw in powder process, powder moves up along induced duct 9 under air-introduced machine 14 acts on, tangentially enter cyclone separator 11 from helical form inlet tube 10, start to move in a circle in centrum 15, then fall back to gradually in ash bucket 16, fall mouth 18 after rise by powder falling pipe 17 and powder and again enter into kettle 3, continue to participate in reaction, both the Dust Capacity be diffused in air had been decreased, in turn ensure that raw material farthest effectively utilizes, both free from environmental pollution, also the waste of material can not be caused, pure air enters air-introduced machine 14 from helical form outlet 12 and discharges, after the addition was finished, close air-introduced machine 14 and cyclone separator 11, after the completion of reaction, open discharging opening 7, release material.
Above an embodiment of the present utility model has been described in detail, but described content being only preferred embodiment of the present utility model, can not being considered to for limiting practical range of the present utility model.All equalizations done according to the utility model application range change and improve, and all should still belong within patent covering scope of the present utility model.

Claims (4)

1. the reactor with cyclone separator, comprise kettle, the bottom of described kettle is provided with support, described support is fixedly connected with kettle, the lower center position of described kettle outside is provided with motor, the lower center position of described kettle inside is provided with shaft, shaft and motor are by electrical connection, the top of described shaft is provided with paddle, the bottom of described kettle is provided with discharging opening, it is characterized in that: the top of described kettle is provided with powder feed mouth, liquid material charge door and powder fall mouth after rise, described powder feed mouth, liquid material charge door and powder fall mouth after rise and kettle communicates, the side of described powder feed mouth is provided with induced duct, the top of described kettle is provided with cyclone separator, described cyclone separator comprises centrum, the side of described centrum is provided with helical form inlet tube, the relative side of described centrum is provided with helical form outlet, the bottom of described centrum is provided with ash bucket, the bottom of described ash bucket is provided with powder and falls pipe after rise, described ash bucket and powder fall pipe after rise and communicate, described powder falls pipe after rise and powder falling mouth communicates, described helical form inlet tube and induced duct communicate, described helical form outlet is provided with discharge pipe, described discharge pipe is provided with air-introduced machine, described air-introduced machine and discharge pipe communicate.
2. a kind of reactor with cyclone separator according to claim 1, is characterized in that: the material of described induced duct and discharge pipe is stainless steel.
3. a kind of reactor with cyclone separator according to claim 1, is characterized in that: described paddle is provided with material feeding hole.
4. a kind of reactor with cyclone separator according to claim 1, is characterized in that: described cyclone separator is between powder feed mouth and liquid material charge door.
CN201420735942.XU 2014-11-27 2014-11-27 A kind of reactor with cyclone separator Expired - Fee Related CN204320292U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420735942.XU CN204320292U (en) 2014-11-27 2014-11-27 A kind of reactor with cyclone separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420735942.XU CN204320292U (en) 2014-11-27 2014-11-27 A kind of reactor with cyclone separator

Publications (1)

Publication Number Publication Date
CN204320292U true CN204320292U (en) 2015-05-13

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420735942.XU Expired - Fee Related CN204320292U (en) 2014-11-27 2014-11-27 A kind of reactor with cyclone separator

Country Status (1)

Country Link
CN (1) CN204320292U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105997515A (en) * 2016-06-29 2016-10-12 胡海潮 Automatic granulator for pharmaceutical production

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105997515A (en) * 2016-06-29 2016-10-12 胡海潮 Automatic granulator for pharmaceutical production

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Date Code Title Description
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: 20150513

Termination date: 20161127

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