CN202376995U - Wood powdered activated carbon reproduction line - Google Patents

Wood powdered activated carbon reproduction line Download PDF

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Publication number
CN202376995U
CN202376995U CN2011205726632U CN201120572663U CN202376995U CN 202376995 U CN202376995 U CN 202376995U CN 2011205726632 U CN2011205726632 U CN 2011205726632U CN 201120572663 U CN201120572663 U CN 201120572663U CN 202376995 U CN202376995 U CN 202376995U
Authority
CN
China
Prior art keywords
peat
high temperature
drying
shaft kiln
temperature shaft
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
CN2011205726632U
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Chinese (zh)
Inventor
魏安国
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.)
CHINA FUJIAN ZHIXING ACTIVATED CARBON CO., LTD.
Original Assignee
FUJIAN JIANOU ZHIXING ACTIVATED CARBON 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 FUJIAN JIANOU ZHIXING ACTIVATED CARBON Co Ltd filed Critical FUJIAN JIANOU ZHIXING ACTIVATED CARBON Co Ltd
Priority to CN2011205726632U priority Critical patent/CN202376995U/en
Application granted granted Critical
Publication of CN202376995U publication Critical patent/CN202376995U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

Disclosed is a wood powdered activated carbon reproduction line, which comprises a crushing and drying device, a cyclone separating device, a high-temperature vertical kiln activating furnace and a cooling bag filtering device, wherein peat is heated for drying and crushed mechanically by the crushing and drying device, peat particles are separated by the cyclone separating device and reactivated by the high-temperature vertical kiln activating furnace, the reactivated peat is cooled down by the cooling bag filtering device, and material discharging is performed by a bag filter, so that activated carbon reproduction is achieved completely, the ignition loss rate is low, the reproduction cost is low, the reproduction quality is good, and large-scale automatic control production is achieved.

Description

Wooden powdered active carbon regenerating production line
Technical field
The utility model relates to the automatic assembly line technical field, specifically is meant wooden powdered active carbon regenerating production line.
Background technology
According to incompletely statistics, after charcoal absorption was saturated, the particle charcoal of reproducible utilization accounted for 70 percent, carries out Regeneration Treatment, has both satisfied the resource circulation utilization, has reduced resource loss, had also practiced thrift a large amount of costs for enterprise.
At present; The renovation process of active carbon has a variety of; For example: thermal regeneration method, wet oxidation process, bio-regeneration method or the like, problem that prior art exists and shortcoming are incomplete for regeneration, burning mistake rate is high, regeneration cost is high, regeneration is of poor quality, can't form extensive and automation control production.
The utility model content
The utility model provides a kind of wooden powdered active carbon regenerating production line, and its main purpose is to solve the continuous enclosed automated production of wood powder shaped activated carbon and cuts down the consumption of energy, improves output and quality and yield.
The utility model adopts following technical scheme:
Wooden powdered active carbon regenerating production line; Comprise drying equipment, Cyclonic separating apparatus, high temperature shaft kiln activation furnace, the cooling bag filter equipment pulverized; Peat gets into the pulverizing drying equipment of this production line after the sheet frame dehydration; The output of pulverizing drying equipment is connected to Cyclonic separating apparatus through drying tube, and the Cyclonic separating apparatus output is connected to high temperature shaft kiln activation furnace through pipeline, and high temperature shaft kiln activation furnace is connected to cooling bag filter equipment through pipeline.
Described pulverizing drying equipment comprises conveying worm, pulverizer, combustion furnace and drying tube; Conveying worm continuously, be transported to pulverizer with peat quantitatively; Combustion furnace is sent into combustion gas through pipeline to pulverizer, and pulverizer is dispersity with the peat that suspends and enters into Cyclonic separating apparatus through drying tube.
Described Cyclonic separating apparatus comprises cyclone separator, peat conveyance conduit, drying tube, air-introduced machine and air damper; Cyclone separator is sent into high temperature shaft kiln activation furnace with the peat particle of drying through the peat conveyance conduit, and air-introduced machine connects cyclone separator, its output connection gas conditioner through drying tube.
Described high temperature shaft kiln activation furnace comprises high temperature shaft kiln, burner, cartridge, air hose, and the high temperature shaft kiln provides heat energy through burner, joins through pipeline and cooling bag filter equipment, and burner is connected with cartridge, air hose.
Described cooling bag filter equipment comprises cooling tube, sparge pipe, bag hose, discharger, air-introduced machine, and cooling tube is connected with sparge pipe, bag hose, and bag hose links to each other, exports dry charcoal with discharger.
The utility model adopts above technical scheme; Through pulverizing drying equipment peat is carried out heat drying and mechanical disintegration; Isolate the peat particle through Cyclonic separating apparatus, the peat particle is carried out activation again, cool through the peat of cooling bag filter equipment after to activation through high temperature shaft kiln activation furnace; And carry out discharging behind the process bag hose, thereby make that regeneration of activated carbon is complete, burning mistake rate is low, regeneration cost is low, the regeneration quality is good, realized extensive and production is controlled in automation.
Description of drawings
Fig. 1 the utility model general structure block diagram.
The specific embodiment
Wooden powdered active carbon regenerating production line; Comprise drying equipment 1, Cyclonic separating apparatus 2, high temperature shaft kiln activation furnace 3, the cooling bag filter equipment 4 pulverized; Peat gets into the pulverizing drying equipment 1 of this production line after the sheet frame dehydration; The output of pulverizing drying equipment 1 is connected to Cyclonic separating apparatus 2 through drying tube, and Cyclonic separating apparatus 2 outputs are connected to high temperature shaft kiln activation furnace 3 through pipeline, and high temperature shaft kiln activation furnace 3 is connected to cooling bag filter equipment 4 through pipeline.
Peat gets into through the sheet frame dehydration and pulverizes drying equipment, and the peat of moisture content 70% is dry under the condition of high temperature, and moisture content drops to about 20%, gets into activation stage subsequently, and the peat particle is suspended in and is transfused to the high temperature shaft kiln in the air.Idiographic flow is: be delivered to pulverizer 12 continuously, quantitatively by conveying worm 11, send into combustion gas through pipeline to pulverizer 12 from combustion furnace 13 again simultaneously, separate under the broken effect at heat drying and machinery; Peat is suspended in the waste gas of pulverizer 12 discharges; Be dispersity and get into drying tube 14, the drying capacity of pulverizer 12 is very big, and peat has evaporated most of moisture (moisture content≤20%) in pulverizer; At 21 li in drying tube 14 and cyclone separator, the moisture of evaporation of residual.In cyclone separator 21, air-flow divides upwards outflow and flows out two parts downwards.Most of dry peat particle all is captured in the air-flow of downward outflow, gets into high temperature shaft kiln 31 through peat conveyance conduit 22.After dividing the peat particle of leaving away, the effluent stream that makes progress, most of being drawn by air-introduced machine 23 sent, through drying tube 24 and 25 emptyings of waste gas adjuster; The fraction air-flow mixes with combustion gas through air damper 26 and drying tube 27, and the temperature of adjustments of gas (500-650 ℃) is to meet the requirement of pulverizer 12.The dry needed heat of peat is to be provided by the burning of the fuel of combustion tube 16 supply burners 15 with the fuel gas of (is main with carbon monoxide and hydrogen) in the high-temperature gas of drying tube 44 entering combustion furnaces.Combustion air is all supplied with, or is supplied with combustion furnace to a part as auxiliary air through air hose 17, burner 15.
In the high temperature shaft kiln 31 of certain volume, peat particle and high-temperature gas (850 ℃-900 ℃) time of staying in stove is according to deciding through the gas of high temperature shaft kiln 31 and the flow of peat mist.In high temperature shaft kiln 31, the tangential velocity of gas will be higher than the speed of passing through of peat particle.General peat is with the speed more than 0.5 meter per second, or is advisable with the speed more than 1 meter per second.
Powdered activated carbon after high temperature shaft kiln 31 carries out activation gets into cooling tube 41, temperature of charge is reduced to≤100 ℃ of entering bag hoses 42 from 850 ℃-900 ℃, and through the dry charcoal of discharger 43 outputs.

Claims (5)

1. wooden powdered active carbon regenerating production line, it is characterized in that: it comprises:
Pulverize drying equipment, peat is carried out heat drying and mechanical disintegration;
Cyclonic separating apparatus is isolated the peat particle through cyclone separator;
High temperature shaft kiln activation furnace carries out activation again through the high temperature shaft kiln to the peat particle;
Cooling bag filter equipment cools to the peat after the activation, and carries out discharging through behind the bag hose;
Peat gets into the pulverizing drying equipment of this production line after the sheet frame dehydration; The output of pulverizing drying equipment is connected to Cyclonic separating apparatus through drying tube; The Cyclonic separating apparatus output is connected to high temperature shaft kiln activation furnace through pipeline, and high temperature shaft kiln activation furnace is connected to cooling bag filter equipment through pipeline.
2. wooden powdered active carbon regenerating production line according to claim 1; It is characterized in that: described pulverizing drying equipment comprises conveying worm, pulverizer, combustion furnace and drying tube; Conveying worm continuously, be transported to pulverizer with peat quantitatively; Combustion furnace is sent into combustion gas through pipeline to pulverizer, and pulverizer is dispersity with the peat that suspends and enters into Cyclonic separating apparatus through drying tube.
3. wooden powdered active carbon regenerating production line according to claim 1; It is characterized in that: described Cyclonic separating apparatus comprises cyclone separator, peat conveyance conduit, drying tube, air-introduced machine and air damper; Cyclone separator is sent into high temperature shaft kiln activation furnace with the peat particle of drying through the peat conveyance conduit, and air-introduced machine connects cyclone separator, its output connection gas conditioner through drying tube.
4. wooden powdered active carbon regenerating production line according to claim 1; It is characterized in that: described high temperature shaft kiln activation furnace comprises high temperature shaft kiln, burner, cartridge, air hose; The high temperature shaft kiln provides heat energy through burner; Join through pipeline and cooling bag filter equipment, burner is connected with cartridge, air hose.
5. wooden powdered active carbon regenerating production line according to claim 1; It is characterized in that: described cooling bag filter equipment comprises cooling tube, sparge pipe, bag hose, discharger, air-introduced machine; Cooling tube is connected with sparge pipe, bag hose, and bag hose links to each other, exports dry charcoal with discharger.
CN2011205726632U 2011-12-31 2011-12-31 Wood powdered activated carbon reproduction line Expired - Fee Related CN202376995U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011205726632U CN202376995U (en) 2011-12-31 2011-12-31 Wood powdered activated carbon reproduction line

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011205726632U CN202376995U (en) 2011-12-31 2011-12-31 Wood powdered activated carbon reproduction line

Publications (1)

Publication Number Publication Date
CN202376995U true CN202376995U (en) 2012-08-15

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011205726632U Expired - Fee Related CN202376995U (en) 2011-12-31 2011-12-31 Wood powdered activated carbon reproduction line

Country Status (1)

Country Link
CN (1) CN202376995U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102553554A (en) * 2011-12-31 2012-07-11 福建省建瓯市芝星活性炭有限公司 Production line for regenerating wood based powdered activated carbon
CN107913689A (en) * 2017-11-16 2018-04-17 于伟军 A kind of dangerous waste solid waste method for regenerating activated carbon
CN108993458A (en) * 2018-07-04 2018-12-14 浙江荣兴活性炭有限公司 A kind of novel environment friendly regenerated carbon production line

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102553554A (en) * 2011-12-31 2012-07-11 福建省建瓯市芝星活性炭有限公司 Production line for regenerating wood based powdered activated carbon
CN102553554B (en) * 2011-12-31 2013-11-27 福建省芝星炭业股份有限公司 Production line for regenerating wood based powdered activated carbon
CN107913689A (en) * 2017-11-16 2018-04-17 于伟军 A kind of dangerous waste solid waste method for regenerating activated carbon
CN108993458A (en) * 2018-07-04 2018-12-14 浙江荣兴活性炭有限公司 A kind of novel environment friendly regenerated carbon production line

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee

Owner name: FUJIAN ZHIXING ACTICATED CARBON CO., LTD.

Free format text: FORMER NAME: FUJIAN JIANOU ZHIXING ACTIVATED CARBON CO., LTD.

CP01 Change in the name or title of a patent holder

Address after: 353100 Nanping City, Fujian province Jianou City Xilin wood

Patentee after: CHINA FUJIAN ZHIXING ACTIVATED CARBON CO., LTD.

Address before: 353100 Nanping City, Fujian province Jianou City Xilin wood

Patentee before: Fujian Jianou Zhixing Activated Carbon Co., Ltd.

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

Granted publication date: 20120815

Termination date: 20141231

EXPY Termination of patent right or utility model