[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

CN202501743U - Tank type calciner - Google Patents

Tank type calciner Download PDF

Info

Publication number
CN202501743U
CN202501743U CN2012200786928U CN201220078692U CN202501743U CN 202501743 U CN202501743 U CN 202501743U CN 2012200786928 U CN2012200786928 U CN 2012200786928U CN 201220078692 U CN201220078692 U CN 201220078692U CN 202501743 U CN202501743 U CN 202501743U
Authority
CN
China
Prior art keywords
volatilization
furnace
calcining
heating flame
type calcine
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
CN2012200786928U
Other languages
Chinese (zh)
Inventor
许继忠
田雪风
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN2012200786928U priority Critical patent/CN202501743U/en
Application granted granted Critical
Publication of CN202501743U publication Critical patent/CN202501743U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Landscapes

  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Abstract

The utility model discloses a tank type calciner consisting of calcination tanks, a combustion chamber, heating flame paths, air channels, volatilization lanes, smoke flues, a material feeding system and a material discharging system. The tank type calciner comprises two calcination tanks which are arranged in a left-and-right direction and vertically disposed, the heating flame paths are arranged on the front side and the rear side of the calcination tanks, the inlets of the heating flame paths are connected with the combustion chamber, the outlets of the heating flame paths are communicated with the smoke flues, the volatilization lanes are arranged on the outer periphery of the heating flame paths, the inlets of the volatilization lanes are connected and arranged on volatile component discharge outlets on the upper portion of the calcination tanks, the outlets of the volatilization lanes are communicated with the heating flame paths, and the air channels are arranged under the heating flame paths and communicated with the volatilization lanes. According to the tank type calciner of the utility model, the advantage of simple structure is realized, volatile components decomposed from raw materials are mixed with the air after being discharged from the upper discharge outlets of the calcination tanks, and enter the heating flame paths after being subjected to preheating through the heating flame paths for full combustion and utilization, so the whole calciner has advantages of high thermal efficiency, good production continuity and high production efficiency.

Description

A kind of can-type calcine furnace
Technical field
The utility model relates to a kind of calcining furnace, particularly relates to a kind of can-type calcine furnace that is used for carbon and the calcining of graphite product production raw material.
Background technology
In the commercial production of carbon and graphite product, the capital equipment that the raw material calcining will be used is a can-type calcine furnace.In the prior art; The body of heater of can-type calcine furnace is made up of the calcining jar of several same structures that are built into refractory brick and arranged perpendicular; Per four calcining jars are one group, and every calcining furnace is formed by three to six groups mostly, promptly include 12 to 24 calcining jars.The major defect of above-mentioned can-type calcine furnace is: 1, need a fairly large number of steel during capital construction, and various special-shaped silica brick and the refractory fireclay block of specification, the institute's can-type calcine furnace of building investment is huge; 2, the calcining furnace of traditional structure is when the big delay coke of calcining volatile content, not normal phenomenon such as be prone to take place coking, stifled stove in the stove or blow out.The limitation that above shortcoming has objectively caused calcining furnace to use has also influenced the development of its industry simultaneously.
Summary of the invention
The purpose of the utility model provides a kind of can-type calcine furnace, and solving traditional calcining furnace complex structure, cost is high, heat energy utilization rate low and easy generation coking, stifled stove or the deficiency of not normal phenomenon such as blow out.
In order to solve above technical deficiency, the utility model adopts following technical scheme:
A kind of can-type calcine furnace is made up of calcining jar, combustion chamber, heating quirk, air channel, volatilization shunting, flue, feeding system and discharge system, and feeding system is arranged on the top of calcining jar; Bottom at the calcining jar is provided with discharge system; Described can-type calcine furnace includes about two to be arranged and the calcining jar of arranged perpendicular, is provided with the heating quirk in the both sides, front and back of said calcining jar, and the import of heating quirk connects the combustion chamber; Outlet is communicated with flue; Outer periphery at the heating quirk is equipped with the volatilization shunting, and the inlet in volatilization shunting connects the volatile matter outlet that is located at calcining jar top, and outlet is communicated with the heating quirk; Air channel is arranged on the below of heating quirk, is communicated with the volatilization shunting.
Wherein, heating quirk has five layers, and along calcining jar arrangement in a zigzag up and down, air channel has two layers, is arranged above and below along the calcining jar.
Described feeding system comprises hopper and the screw(-type) feeder that is arranged on the calcining jar charging aperture, and discharge system comprises the furnace charge door and is installed in furnace charge cooling jacket and multiple tooth rotation discharge machine outdoors.
The utility model also furnace wall of can-type calcine furnace is provided with and sees fire and thermometer hole.
The can-type calcine furnace of the utility model is not to be the simple cutting to existing four pot types or multipot type calcining furnace body structure, compared with prior art, the utlity model has following advantage:
1, the can-type calcine furnace of the utility model employing combustion chamber simple in structure is a thermal source, and the thermal source of four pot types or multipot type calcining furnace adopts the numerous and diverse regenerator of gas piping and jet for gas and structure to form;
2, the can-type calcine furnace of the utility model only is provided with five layers of heating quirk, and the heat energy utilization rate is higher, and four pot types or multipot type calcining furnace heating quirk are general many in six to eight roads or more than eight roads, and structure is numerous and diverse, and manufacturing cost is very expensive;
3, the can-type calcine furnace fugitive constituent of the utility model is directly through after the preheating of heating quirk periphery secondary; Converge with the air of air channel, get into the heating quirk and heat, simple in structure; The heat energy utilization rate is high; And four pot types of the prior art or multipot type calcining furnace, its preheated air road structure is very complicated, and cost is also very expensive;
4, the can-type calcine furnace design science of the utility model, structure is unique, and cheap, easy to use, the calcining furnace of prior art can't be compared with it.
The can-type calcine furnace of the utility model is simple in structure, and construction cost is low, and burning quality is good; After discharging from a calcining jar top outlet by the volatile matter that decomposites in the raw material; Mix with air, after the preheating of heating quirk, get into the heating quirk, fully burning utilizes; Full furnace thermal efficiency is higher, and the production continuity is strong.Maintenance is less in the utility model production process, and maintenance cost is low, and production efficiency is high.
Description of drawings
Fig. 1 is the structural representation of the utility model can-type calcine furnace.
Fig. 2 is that the B of Fig. 1 is to cutaway view.
Fig. 3 is that the C of Fig. 1 is to cutaway view.
The specific embodiment
Below in conjunction with accompanying drawing and specific embodiment the utility model is done explanation further.
The structure of can-type calcine furnace such as Fig. 1, Fig. 2, shown in Figure 3, Fig. 1 wherein be along A-A among Fig. 3 to cutaway view.
Can-type calcine furnace is made up of calcining jar 1, combustion chamber 4, heating quirk 2, air channel 3, volatilization shunting 6, flue 5, feeding system 7 and discharge system 8.The agent structure of can-type calcine furnace is to arrange about two and the calcining jar 1 of arranged perpendicular, specification of each calcining jar for long 1520 millimeters * wide 470 millimeters * high 3500 millimeters.The five layers of specification that have been arranged above and below in the both sides, front and back of calcining jar 1 are long 3270 millimeters * wide 240 millimeters * high 411 millimeters heating quirks 2, and the import of heating quirk 2 connects combustion chamber 4, be switchback turn after, outlet is communicated with flue 5.Below orlop heating quirk 2, be provided with two-layer air channel 3, the specification of air channel 3 for long 3270 millimeters * wide 240 millimeters * high 180 millimeters, be communicated with volatilization shunting 6.Also be provided with volatilization shunting 6 in the periphery of heating quirk 2, the inlet in volatilization shunting 6 connects the volatile matter outlet 10 that is located at calcining jar 1 top, and outlet is communicated with heating quirk 2.
Be provided with the feeding system 7 that is used for charging at the top of can-type calcine furnace, said feeding system 7 comprises hopper and screw(-type) feeder.Be provided with the discharge system 8 that is used for discharge in the bottom of can-type calcine furnace sidewall, said discharge system 8 comprises furnace charge door, cooling jacket and multiple tooth rotation discharge machine.
Simultaneously, for ease temperature in the stove is carried out management and control, on body of heater, be provided with and see fire and thermometer hole 9.
The body of heater of can-type calcine furnace is built moulding by laying bricks or stones with refractory brick, outside builds into the outline of can-type calcine furnace by laying bricks or stones with machine-processed common brick, and the cavity between outline and the body of heater is filled with insulation material 11, plays heat preservation effect.
The calcining heat of the utility model can-type calcine furnace is at 1250~1350 ℃, and the maximum temperature of both sides heating quirk 2 can reach 1300~1380 ℃, can be with about the air preheat to 400 in the air channel 3~600 ℃.The production capacity of can-type calcine furnace is 60~100 kilograms/jar hours.

Claims (6)

1. can-type calcine furnace; Form by calcining jar (1), combustion chamber (4), heating quirk (2), air channel (3), volatilization shunting (6), flue (5), feeding system (7) and discharge system (8); Feeding system (7) is arranged on the top of calcining jar (1), in calcining jar (a 1) bottom discharge system (8) is set, and it is characterized in that described can-type calcine furnace includes to arrange about two and the calcining jar (1) of arranged perpendicular; Be provided with heating quirk (2) in the both sides, front and back of said calcining jar (1); The import of heating quirk (2) connects combustion chamber (4), and outlet is communicated with flue (5), is equipped with volatilization shunting (6) in the outer periphery that heats quirk (2); The inlet in volatilization shunting (6) connects the volatile matter outlet (10) that is located at calcining jar (1) top; Outlet is communicated with heating quirk (2), and air channel (3) is arranged on the below of heating quirk (2), is communicated with volatilization shunting (6).
2. can-type calcine furnace as claimed in claim 1 is characterized in that described heating quirk (2) has five layers, arranges in a zigzag up and down along calcining jar (1).
3. can-type calcine furnace as claimed in claim 1 is characterized in that described air channel (3) has two layers, is arranged above and below along calcining jar (1).
4. can-type calcine furnace as claimed in claim 1 is characterized in that described feeding system (7) comprises hopper and the screw(-type) feeder that is arranged on calcining jar (1) charging aperture.
5. can-type calcine furnace as claimed in claim 1 is characterized in that said discharge system (8) comprises the furnace charge door and is installed in furnace charge cooling jacket and multiple tooth rotation discharge machine outdoors.
6. can-type calcine furnace as claimed in claim 1, the furnace wall that it is characterized in that can-type calcine furnace are provided with sees fire and thermometer hole (9).
CN2012200786928U 2012-03-06 2012-03-06 Tank type calciner Expired - Fee Related CN202501743U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2012200786928U CN202501743U (en) 2012-03-06 2012-03-06 Tank type calciner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2012200786928U CN202501743U (en) 2012-03-06 2012-03-06 Tank type calciner

Publications (1)

Publication Number Publication Date
CN202501743U true CN202501743U (en) 2012-10-24

Family

ID=47038355

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2012200786928U Expired - Fee Related CN202501743U (en) 2012-03-06 2012-03-06 Tank type calciner

Country Status (1)

Country Link
CN (1) CN202501743U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102538455A (en) * 2012-03-06 2012-07-04 许继忠 Pot-type calcining furnace
CN104677098A (en) * 2013-12-02 2015-06-03 贵阳铝镁设计研究院有限公司 Spring pull-rod device of tank-type calcining furnace
CN108800922A (en) * 2018-08-14 2018-11-13 沈阳创联工业技术有限公司 A kind of simple type can-type calcine furnace

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102538455A (en) * 2012-03-06 2012-07-04 许继忠 Pot-type calcining furnace
CN104677098A (en) * 2013-12-02 2015-06-03 贵阳铝镁设计研究院有限公司 Spring pull-rod device of tank-type calcining furnace
CN104677098B (en) * 2013-12-02 2016-08-24 贵阳铝镁设计研究院有限公司 A kind of can-type calcine furnace spring pull rod device
CN108800922A (en) * 2018-08-14 2018-11-13 沈阳创联工业技术有限公司 A kind of simple type can-type calcine furnace

Similar Documents

Publication Publication Date Title
CN101585524B (en) Fugitive constituent and preheated air passage structure of tank type carbon calciner
CN201883063U (en) External-heating tank-type formed coke carbonizing furnace
CN201321381Y (en) Novel carbon tank type calciner
CN102303956B (en) Sleeve-type lime kiln
CN202152278U (en) Novel integral activation furnace
WO2013177952A1 (en) Large downstream tank type incinerator
CN201313819Y (en) Volatile matter and preheated air channel structure of calciner
CN102627976B (en) Coking chamber for pulverized coal destructive distillation
CN202754941U (en) Stamp-charging coke oven with partition-adjustable regenerative chambers
CN105905894A (en) Carbonization and activation device for active coke production
CN102627418B (en) Compound lime kiln
CN204174158U (en) A kind of external-heat low-temperature pyrolysis stove
CN201314783Y (en) Tank-type calcining furnace
CN107238295A (en) A kind of roaster and method of roasting
CN202501743U (en) Tank type calciner
CN101531906A (en) Method for electrical heating continuous coal pyrogenation coking and coking furnace thereof
CN102538455A (en) Pot-type calcining furnace
CN104593015A (en) Formcoke refining method and device thereof
CN102745671B (en) Pot-type carbon calciner
CN202322715U (en) Novel stamp-charging coke oven
CN201883062U (en) Easy-discharging tank-type formed coke carbonizing furnace
CN109485028B (en) Needle-shaped calcined petroleum coke production process and calciner for production thereof
CN202705042U (en) Tank type carbon calcining furnace
CN202214324U (en) Heat adjustable formed coke carbonization furnace
CN202193734U (en) Sleeve type lime kiln

Legal Events

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: 20121024

Termination date: 20150306

EXPY Termination of patent right or utility model