CN201321381Y - Novel carbon tank type calciner - Google Patents

Novel carbon tank type calciner Download PDF

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Publication number
CN201321381Y
CN201321381Y CNU2008202189639U CN200820218963U CN201321381Y CN 201321381 Y CN201321381 Y CN 201321381Y CN U2008202189639 U CNU2008202189639 U CN U2008202189639U CN 200820218963 U CN200820218963 U CN 200820218963U CN 201321381 Y CN201321381 Y CN 201321381Y
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China
Prior art keywords
fugitive constituent
millimeters
road
furnace
utility
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Expired - Fee Related
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CNU2008202189639U
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Chinese (zh)
Inventor
刘敬穆
马绍先
李振国
杨青辰
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Northeast University Design and Research Institute Co Ltd
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Northeast University Design and Research Institute Co Ltd
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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
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Abstract

The utility model relates to a novel carbon tank type calciner, which comprises a feeding storage bucket, a material chamber, flame passages, a flue passage, a fugitive constituent passage, preheating air passages and a support frame. The utility model is characterized in that the special fugitive constituent passage and a regulating control valve are additionally arranged on the novel carbon tank type calciner; the number of the flame passages is reduced by a half, and the width of the flame passages is increased; the preheating air passages at the bottom of the novel carbon tank type calciner have four layers; the uppermost layer is communicated with the fugitive constituent passage; the rest three layers are the preheating air passages; a fuel burner of the front wall is removed; and a baker burner is arranged on the back wall. Compared with the existing tank type calciner, the utility model improves the yield, saves the energy, and improves the working conditions of workers, so the utility model has high popularized application value.

Description

The plain can-type calcine furnace of a kind of novel charcoal
Technical field
The utility model belongs to the technical field of carbon product, is specifically related to a kind of raw petroleum coke calcining main equipment---the technology reforming scheme of the plain pot furnace of charcoal.
Background technology
At present, main pot furnace and two kinds of equipment of rotary kiln of adopting of carbon product enterprise raw petroleum coke calcining.Pot furnace is compared with rotary kiln, and its major advantage is: quality product is high and stable; The carbonaceous scaling loss is few: do not add or few refuel: converter life long (in general eight to ten years can not overhaul) etc.Yet it also exists output on the low side; Heat-energy losses is excessive; Shortcomings such as operational condition difference.
In the last few years, pot furnace some improvement had been made.As: material chamber height and quirk height strengthen simultaneously, and the quirk number of plies is increased to eight layers by six layers; Cancellation lattice formula special-purpose air primary heater unit; High-temp waste gas is drawn body of heater and is added to utilize; Bottom of furnace body is newly established the preheated air road; Strengthen the watercooling jacket size and strengthen material cooling performance etc.Through after the above-mentioned improvement, pot furnace is by the still formula refinery coke of original production volatile content 6~7%, and output is 50~60kg/h jar; Can produce the retard petroleum coke of volatile content 10~15% till now, output can reach 85kg/h jar (contain 15~20% and return batching).But still there are many shortcomings in the pot furnace after improving, mainly contains: (1) material transverse section, chamber and quirk cross-sectional dimension and structure do not become, and output is on the low side, can not adapt to the needs of the plain enterprise of large-scale charcoal; (2) furnace bottom preheating of air efficient is not high little to material chamber cooling performance; (3) design of fugitive constituent road is unreasonable, makes unnecessary fugitive constituent also in the body of heater internal combustion, has caused the long dump temperature of calcining zone too high, and wasted heat energy: (4) furnace insulation poor performance causes stove table temperature too high; (5) the original design burner structure that remains with because of not needing extra fuel, does not have actual use value.
The utility model content
Domestic and international aluminium industrial equipments maximizes and the requirement of energy-saving and environmental protection in order to satisfy, at the existing problem of the plain can-type calcine furnace of above-mentioned charcoal, the design people is summing up on the basis of production experience for many years, and use for reference the technology of metallurgical coke oven and ring type carbon roasting furnace, the plain can-type calcine furnace of a kind of novel charcoal has been proposed.
The utility model proposes the plain can-type calcine furnace of a kind of novel charcoal, comprise reinforced hopper, material chamber, quirk, flue, fugitive constituent road, preheated air road and support frame, it is characterized in that:
(1) set up special-purpose fugitive constituent road, and added and be equipped with adjusting control valve;
(2) the quirk number is reduced half, and increased the width and the height of quirk;
(3) furnace bottom preheated air road is divided into four layers, last layer is communicated with special-purpose fugitive constituent road, below three layers be the preheated air road;
(4) removed the fuel nozzle of front wall, and the baker burner has been set at the back wall.
The plain can-type calcine furnace of existing charcoal all inserts the heating quirk with fugitive constituent, makes fugitive constituent all in the quirk internal combustion.And from heat calculation as can be known, the raw petroleum coke volatile content only needs 5~6%, and the heat energy that it produced can satisfy the needs of can-type calcine furnace ordinary production; And at present the volatile content of carbon element enterprise calcined petroleum coke allows fugitive constituent perfect combustion in quirk all about 10~15%, and being actually has wasted 30~50% fugitive constituent (calorific value 3300kcal/Nm 3).So in present design, other has designed the special-purpose fugitive constituent road with valve control, adjusting, and unnecessary fugitive constituent is directed to the body of heater main flue, make the residue fugitive constituent in the proper site burning of setting, heat energy obtains fully, reasonable use thereby make.Simultaneously, because the design's residue fugitive constituent does not burn, just prevented that also material chamber calcining zone from moving down with dump temperature too high in the quirk below four layers.
Second technical characterictic of the present utility model is the structure of having improved the preheated air road, changes furnace bottom preheated air road individual layer useful area into 308 millimeters * 400 millimeters * 2 by existing 236 millimeters * 210 millimeters, increases to four layers by original two-layer.Last layer is walked to remain fugitive constituent and it is caused in the outer main flue of body of heater to burn, at Lu Houqiang a gas blower is set, air is introduced in the basecoat preheated air road, made it successively by two, three layers of preheated air road, the high temperature air after the preheating is drawn the outer use rationally of stove.The preheated air road is arranged on the both sides of material chamber, and air is in the process of preheating, and it can play cooling effect to the material chamber simultaneously, thereby has also reduced dump temperature.
All there is quirk its both sides, material chamber of the plain can-type calcine furnace of existing charcoal, and also are provided with partition wall between the quirk of adjacent two material chambers.In the present design, the partition wall between adjacent two quirks is removed, made the quirk number reduce half, make every group of material chamber become shared one group of quirk by two groups of quirks of original use, and the corresponding width that has increased material chamber and quirk.The utility model will have the material chamber now and be widened to 500 millimeters from 360 millimeters, and material chamber height also suitably increases, and make material chamber volume increase about 50%; Simultaneously again the quirk number of plies is increased to nine layers by eight layers, to increase the time that material stops in the material chamber, these aggregate measures can make pot furnace output improve 50% or higher.
The heat that burning is produced in view of the raw petroleum coke fugitive constituent is enough to keep the ordinary production of calcining furnace, does not need extra fuel again, and the utility model is cancelled the former fuel nozzle device that is arranged on the calcining furnace front wall, and baker is displaced to the back wall with simple and easy burner.In addition, 1800 millimeters of the outstanding bodies of heater of intrinsic main flue, and the design moves after main flue is in body of heater now, has reduced the total width of body of heater.At last, the design has also suitably increased around the body of heater and the thickness of end face thermal insulation layer, to strengthen the heat insulation effect of body of heater, like this, both can improve the labor condition in workshop; Can reduce dissipation of heat energy, save energy again.
In a word, the plain can-type calcine furnace of novel charcoal of the present utility model possesses following advantage:
(1) improved single jar output, furnace binding is rationally compact, and the initial cost of unit output reduces, and calcining furnace efficient is improved, and can realize the maximization of calcining furnace;
(2) owing to unnecessary fugitive constituent in the raw material obtains fully, reasonably utilizes, add the reasonable setting in preheated air road, can save energy.
Description of drawings
Fig. 1 is the overall structure synoptic diagram of the plain can-type calcine furnace of novel charcoal of the present utility model; Fig. 2 is this calcining furnace quirk, preheated air road diagrammatic cross-section; Fig. 3 is this calcining furnace fugitive constituent road, preheated air road diagrammatic cross-section.In above-mentioned each figure, 1 reinforced hopper; Material chambers 2; 3 quirks; 4 flues; 5 fugitive constituent roads; 6 baker burners; 7 preheated air roads; 8 support frames; 9 special-purpose fugitive constituent roads.
Embodiment
Below in conjunction with embodiment design of the present utility model is further described and replenishes.
As shown in Figure 1, install the support frame 8 of can-type calcine furnace earlier, on the platform of support frame, from bottom to top build body of heater by laying bricks or stones, the preheated air road 7 of elder generation masonry heater bottom, be material chamber 2, quirk 3, flue 4, fugitive constituent road 5 then, these all are prior arts, so useless detailed description.The utility model prolongs the fugitive constituent road, and two, three layers of quirk of wall after only being led to by old stove fugitive constituent road, the special-purpose fugitive constituent road of being set up 9 then extend to furnace bottom always and are horizontally through through front wall main flue at furnace bottom.Material chamber, quirk width have also been done adjustment, and have increased thermal insulation layer around body of heater.Also saved original fuel nozzle that is located at front wall in the present design, pacified a baker burner 6, so just constituted carbon element can-type calcine furnace of the present utility model and add at the back wall of body of heater.
In the actual application of charcoal ink factory, the specification of the plain can-type calcine furnace of charcoal has varied, and its technical parameter will be different, now slightly lifts numerical example and be illustrated:
1 12 jars of tank type carbon calciners of embodiment
The design of 12 potcal pot calcination stoves has 9 groups of quirks, and material chamber section effective width is 500 millimeters, and length is 1780 millimeters; The quirk effective cross section is 400 millimeters and 200 millimeters.Fugitive constituent road size: vertical 204 millimeters * 236 millimeters of back wall; Horizontal 408 millimeters * 250 millimeters of furnace roof, furnace bottom (special use) fugitive constituent road sectional dimension: 308 millimeters * 150 millimeters.Preheated air road size: 308 millimeters * 150 millimeters * 2.
2 40 jars of tank type carbon calciners of embodiment
The design of 40 potcal pot calcination stoves has 30 groups of quirks, and material chamber section effective width is 550 millimeters, and length is 1860 millimeters; The quirk effective cross section is 400 millimeters.Fugitive constituent road size: vertical 236 millimeters * 204 millimeters of back wall; Horizontal 408 millimeters * 250 millimeters of furnace roof, furnace bottom fugitive constituent road sectional dimension: 150 millimeters * 308 millimeters.Preheated air road size: 150 millimeters * 308 millimeters * 2.
3 60 jars of tank type carbon calciners of embodiment
The design of 60 potcal pot calcination stoves has 45 groups of quirks, and material chamber section effective width is 500 millimeters, and length is 1860 millimeters; The quirk effective cross section is 400 millimeters.Fugitive constituent road size: vertical 236 millimeters * 204 millimeters of back wall; Horizontal 408 millimeters * 250 millimeters of furnace roof.Furnace bottom fugitive constituent road sectional dimension: 150 millimeters * 308 millimeters.Preheated air road size: send out a part road sectional dimension for 150 millimeters: 150 millimeters * 308 millimeters.Preheated air road size: 150 millimeters * 308 millimeters * 2.
The plain can-type calcine furnace of charcoal of the present utility model in experimentation, has been brought into play good energy-saving and environmental protection effect, and calcination efficiency also is improved.What is more important, it can be adapted to the requirement of the equipment enlarging of current aluminium industry well, has great application value.

Claims (2)

1. the plain can-type calcine furnace of novel charcoal comprises reinforced hopper, material chamber, quirk, flue, fugitive constituent road, preheated air road and support frame, it is characterized in that:
(1) special-purpose fugitive constituent road is set, and adds and be equipped with adjusting control valve;
Expect that the quirk between the chamber is a quirk for (2) two;
(3) furnace bottom preheated air road is divided into four layers, last layer is communicated with special-purpose fugitive constituent road, below three layers be the preheated air road;
(4) at the back wall baker being set chews with burning.
2. by the plain can-type calcine furnace of the described novel charcoal of claim 1, it is characterized in that said preheated air road is arranged on the both sides of material chamber.
CNU2008202189639U 2008-11-07 2008-11-07 Novel carbon tank type calciner Expired - Fee Related CN201321381Y (en)

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Application Number Priority Date Filing Date Title
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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102745671A (en) * 2012-08-02 2012-10-24 济南澳海炭素有限公司 Pot-type carbon calciner
CN102829626A (en) * 2011-06-15 2012-12-19 贵阳铝镁设计研究院有限公司 Tank type calcinating furnace
WO2013063867A1 (en) * 2011-11-01 2013-05-10 中铝国际工程股份有限公司 Counterflow tank-type calcine furnace
WO2013177952A1 (en) * 2012-05-31 2013-12-05 中铝国际工程股份有限公司 Large downstream tank type incinerator
CN103663408A (en) * 2012-09-21 2014-03-26 贵阳铝镁设计研究院有限公司 Large-tank type tank furnace structure
CN103663409A (en) * 2012-09-21 2014-03-26 贵阳铝镁设计研究院有限公司 Multi-tank tank type furnace
CN104132542A (en) * 2014-05-29 2014-11-05 山东宇佳新材料有限公司 Petroleum coke calcinator
CN105883784A (en) * 2016-04-06 2016-08-24 东莞市凯金新能源科技股份有限公司 Artificial graphite precursor hot kettle feeding method
CN106324180A (en) * 2015-06-24 2017-01-11 沈阳铝镁设计研究院有限公司 Research device capable of simulating tank-type calcination conditions of petroleum coke and using method thereof
CN107014208A (en) * 2017-06-05 2017-08-04 索通发展股份有限公司 Drop-bottom mechanism and calcining furnace
CN111018369A (en) * 2019-12-11 2020-04-17 东北大学 Magnesite suspension decomposing furnace
CN111578732A (en) * 2020-05-15 2020-08-25 河南华索科技有限公司 Temperature control system of carbon tank type calcining furnace based on multi-flame path monitoring and implementation method thereof

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102829626A (en) * 2011-06-15 2012-12-19 贵阳铝镁设计研究院有限公司 Tank type calcinating furnace
CN102829626B (en) * 2011-06-15 2014-12-17 贵阳铝镁设计研究院有限公司 Tank type calcinating furnace
WO2013063867A1 (en) * 2011-11-01 2013-05-10 中铝国际工程股份有限公司 Counterflow tank-type calcine furnace
WO2013177952A1 (en) * 2012-05-31 2013-12-05 中铝国际工程股份有限公司 Large downstream tank type incinerator
CN102745671B (en) * 2012-08-02 2014-05-14 济南澳海炭素有限公司 Pot-type carbon calciner
CN102745671A (en) * 2012-08-02 2012-10-24 济南澳海炭素有限公司 Pot-type carbon calciner
CN103663408A (en) * 2012-09-21 2014-03-26 贵阳铝镁设计研究院有限公司 Large-tank type tank furnace structure
CN103663409A (en) * 2012-09-21 2014-03-26 贵阳铝镁设计研究院有限公司 Multi-tank tank type furnace
CN103663409B (en) * 2012-09-21 2015-12-02 贵阳铝镁设计研究院有限公司 Multi-tank tank type furnace
CN103663408B (en) * 2012-09-21 2016-02-24 贵阳铝镁设计研究院有限公司 Large pot pot furnace structure
CN104132542A (en) * 2014-05-29 2014-11-05 山东宇佳新材料有限公司 Petroleum coke calcinator
CN106324180A (en) * 2015-06-24 2017-01-11 沈阳铝镁设计研究院有限公司 Research device capable of simulating tank-type calcination conditions of petroleum coke and using method thereof
CN105883784A (en) * 2016-04-06 2016-08-24 东莞市凯金新能源科技股份有限公司 Artificial graphite precursor hot kettle feeding method
CN107014208A (en) * 2017-06-05 2017-08-04 索通发展股份有限公司 Drop-bottom mechanism and calcining furnace
CN107014208B (en) * 2017-06-05 2023-04-18 索通发展股份有限公司 Furnace bottom plate mechanism and calcining furnace
CN111018369A (en) * 2019-12-11 2020-04-17 东北大学 Magnesite suspension decomposing furnace
CN111578732A (en) * 2020-05-15 2020-08-25 河南华索科技有限公司 Temperature control system of carbon tank type calcining furnace based on multi-flame path monitoring and implementation method thereof

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Granted publication date: 20091007

Termination date: 20121107