CN201694848U - Equipment for producing activated charcoal through core carbonizing material - Google Patents

Equipment for producing activated charcoal through core carbonizing material Download PDF

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Publication number
CN201694848U
CN201694848U CN2009201656351U CN200920165635U CN201694848U CN 201694848 U CN201694848 U CN 201694848U CN 2009201656351 U CN2009201656351 U CN 2009201656351U CN 200920165635 U CN200920165635 U CN 200920165635U CN 201694848 U CN201694848 U CN 201694848U
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CN
China
Prior art keywords
collecting box
chamber
heating
conveying belt
harvesting
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
CN2009201656351U
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Chinese (zh)
Inventor
祁项超
凌凤军
苑晶
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.)
CHENGDE LVSHIJIE ACTIVE CARBON Co Ltd
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CHENGDE LVSHIJIE ACTIVE CARBON Co Ltd
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Priority to CN2009201656351U priority Critical patent/CN201694848U/en
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Publication of CN201694848U publication Critical patent/CN201694848U/en
Anticipated expiration legal-status Critical
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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
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency

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Abstract

The utility model discloses equipment for producing activated charcoal through core carbonizing material. The equipment comprises a furnace body, a raw material conveying mechanism, a feed port, a heating section, a vapor supply and gas protection system and a collecting box, wherein the furnace body adopts a closed cavity with the feed port at one end and the collecting box at the other end; the raw material conveying mechanism and the heating section are arranged between the feed port and the collecting box; the conveying mechanism adopts chain drive and the conveying chain plate thereof is made of high-temperature resistant material; and the heating section comprises a raw material preheating section and an activation section, and adopts a microwave heating manner, and a microwave generator is placed above the conveying chain plate. Due to the microwave heating manner, the raw material can continuously pass the heating section for activation, thereby realizing automatic and continuous production; and the equipment has the benefits of reasonable structure, energy conservation, environmental protection, high production efficiency and stable product quality.

Description

A kind of equipment of producing gac with core class charring material
Technical field
The utility model relates to a kind of Activated Carbon Production equipment, particularly relates to a kind of equipment of producing gac with core class charring material.
Background technology
Gac is the important materials of multiple industry and environmental protection industry (epi), and market demand grows with each passing day, and particularly shell class gac is more well sold and in short supply.The main process of producing shell class gac is that raw material is carried out charing and activation at a certain temperature, makes it reach the regulation physical and chemical index.At present, produce gac and adopt process furnace more, and be stove to be built into refractory materials, its structure comprises charging opening, charing section, activation section, discharge port and steam plenum system and flue system, existing problem mainly contains: (1) discharges a large amount of smog, and environmental pollution is more serious; (2) furnace binding complexity, the maintenance difficulty; (3) be difficult to realize automatic continuous production, production efficiency is low; The method of producing the used heating of gac generally has two kinds: the one, and coal, the one,, as heating material, gac per ton need consume 1.2 tons in coal with coal, and a large amount of fume emissions are arranged, the severe contamination that causes to periphery, electricity consumption is as heater means, except that current consumption greatly because furnace binding is unreasonable, fruit stone discharges a large amount of smog in combustion processes, environmental pollution is more serious.Several activation furnaces commonly used now, as the smoldering stove, Si Liepu ature of coal activation furnace and 288 type activation furnaces etc. all are high energy consumption, seriously polluted, big, high, the baroque type of furnace of product cost of investment, wherein, seriously polluted problem is the main contents that local government requires rectification.For this reason, with serious pollution problem is the main task that manufacturing enterprise faces in the solution Activated Carbon Production process.Disclosed in ZL200720102965.7 " a kind of environmental protection, energy-conservation, efficient activation oven for active fruit shell carbon " and disclosed in ZL200820076149.8 " a kind of efficient, energy-conservation absorbent charcoal activation furnace ", all be by improving the structure of charing section, activation section in the body of heater, make sufficient combustion in the gac normal productive process, reduce the discharging of flue gas, use through reality, effect is pretty good, but do not change the stove form, make the furnace binding complexity, the problem of maintenance difficulty and be difficult to realize that the problem of automatic continuous production does not obtain basic solution.
The utility model content
The utility model is at the deficiencies in the prior art; a kind of equipment of producing gac with core class charring material is provided; this equipment is raw material with the core class charring material; adopt microwave heating; realize automatic continuous production; technical problem to be solved is that raw material is continuously activated by heating region; and be provided with rationally that steam is supplied with and gas protection system; this device structure is reasonable; energy-conservation; environmental protection; the production efficiency height; constant product quality; technical solution adopted in the utility model is as follows: the utility model is by body of heater; the ingredient conveyor structure; charging opening; heating zone; steam supply and gas protection system and Material collecting box for harvesting are formed; it is characterized in that body of heater is a sealed hollow; one end is a charging opening; the other end is a Material collecting box for harvesting; the conveying belt that is provided with portless between charging opening and the Material collecting box for harvesting is used for carrying carbonized material; carbonized material is exposed in the micro-wave energy; microwave office is an airtight obturator; to prevent microwave leakage; this obturator comprises that a centre chamber is to provide microwave heating; also comprise two transfer passages that stretch out from centre chamber; carbonized material is placed on the conveying belt of first transfer passage end through opening for feed; pass centre chamber with conveying belt; enter Material collecting box for harvesting from the conveying belt of another transfer passage end; the Material collecting box for harvesting casing is a sandwich structure; it in the interlayer mobile water coolant; centre chamber is divided into a plurality of heating chambers; comprise carbonized material preheating chamber and activating chamber; each heating chamber is established independent exhaust outlet and nitrogen input aperture, and in each activating chamber vapour generator is set.
Mechanism of the present utility model:
Carbonized material adds from opening for feed; and be placed on the conveying belt that moves continuously with the form of surface bed layer; the surface bed layer can guarantee the quick and even of microwave heating; carbonized material on the conveying belt at first enters preheating chamber through transfer passage; preheating temperature is 500~800 ℃; be 2~5 minutes warm up time; make carbonized material after preheating chamber is heated to the desired temperature of charing, enter activating chamber; activation temperature is 900~1000 ℃; guarantee activation effect, the activation back enters Material collecting box for harvesting by transfer passage and is collected.
Compared with prior art, the utility model employing conveying belt mode can reduce the relative movement between carbon granule greatly, particularly in the microwave high-temperature district, there is relative movement hardly, the charcoal loss amount reduced, in addition, moving belt can be realized automatization control, realizes continuous production, enhances productivity.
Description of drawings
Fig. 1 is the utility model structural representation
Embodiment
As shown in Figure 1, the utility model is made up of body of heater, ingredient conveyor structure, charging opening, heating zone, steam supply and gas protection system and Material collecting box for harvesting, and body of heater 22 is sealed hollow, and the conveying belt 2 of portless places in this cavity; Conveying belt adopts resistant to elevated temperatures material to make, one end of body of heater is a charging opening 1, carbonized material 6 enters body of heater by charging opening and places on the conveying belt, through transfer passage 25 carbonized material on the conveying belt 7 is sent into preheating chamber, be placed with microwave heater 3 in the preheating chamber, carbonized material is heated to temperature required by electromagnetic radiation takes place, heated subsequently carbonized material is sent into activating chamber by conveying belt, also be provided with microwave heater 4 in the activating chamber, 5, carbonized material is activated after transfer passage 24 is sent in the Material collecting box for harvesting 23 of the body of heater the other end in activating chamber, preheating chamber and activating chamber all are provided with exhaust outlet 12 separately, 13,14 and nitrogen input aperture 10,11,15,16, nitrogen is delivered to respectively in preheating chamber and the activating chamber by import 17, vapour generator 8,9 are arranged in the activating chamber.

Claims (1)

1. equipment of producing gac with core class charring material; by body of heater; the ingredient conveyor structure; charging opening; heating zone; steam supply and gas protection system and Material collecting box for harvesting are formed; it is characterized in that body of heater is a sealed hollow; one end is a charging opening; the other end is a discharge port; the conveying belt that is provided with portless between charging opening and the Material collecting box for harvesting is used for carrying carbonized material; carbonized material is exposed in the micro-wave energy; microwave office is an airtight obturator; this obturator comprises that a centre chamber is to provide microwave heating; also comprise two transfer passages that stretch out from centre chamber; carbonized material is placed on the conveying belt of first transfer passage end through opening for feed; pass centre chamber with conveying belt; enter Material collecting box for harvesting from the conveying belt of another transfer passage end; the Material collecting box for harvesting casing is a sandwich structure; it in the interlayer mobile water coolant; centre chamber is divided into a plurality of heating chambers; comprise carbonized material preheating chamber and activating chamber; each heating chamber is established independent exhaust outlet and nitrogen input aperture, and in each activating chamber vapour generator is set.
CN2009201656351U 2009-07-13 2009-07-13 Equipment for producing activated charcoal through core carbonizing material Expired - Fee Related CN201694848U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2009201656351U CN201694848U (en) 2009-07-13 2009-07-13 Equipment for producing activated charcoal through core carbonizing material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2009201656351U CN201694848U (en) 2009-07-13 2009-07-13 Equipment for producing activated charcoal through core carbonizing material

Publications (1)

Publication Number Publication Date
CN201694848U true CN201694848U (en) 2011-01-05

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2009201656351U Expired - Fee Related CN201694848U (en) 2009-07-13 2009-07-13 Equipment for producing activated charcoal through core carbonizing material

Country Status (1)

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CN (1) CN201694848U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102806175A (en) * 2011-06-02 2012-12-05 张家港市佳龙真空浸漆设备制造厂 Vacuum pressure paint dipping cluster equipment with improved preheating system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102806175A (en) * 2011-06-02 2012-12-05 张家港市佳龙真空浸漆设备制造厂 Vacuum pressure paint dipping cluster equipment with improved preheating system

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of utility model: Equipment for producing active carbon by core class charring material

Effective date of registration: 20111230

Granted publication date: 20110105

Pledgee: Pingquan County Rural Credit Cooperative Association

Pledgor: Chengde Lvshijie Active Carbon Co., Ltd.

Registration number: 2011990000526

C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20110105

Termination date: 20130713