CN113790589A - Process and device for realizing energy-saving and efficient drying of carbide slag - Google Patents

Process and device for realizing energy-saving and efficient drying of carbide slag Download PDF

Info

Publication number
CN113790589A
CN113790589A CN202111104283.0A CN202111104283A CN113790589A CN 113790589 A CN113790589 A CN 113790589A CN 202111104283 A CN202111104283 A CN 202111104283A CN 113790589 A CN113790589 A CN 113790589A
Authority
CN
China
Prior art keywords
furnace
hot
pipe
air
carbide slag
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.)
Pending
Application number
CN202111104283.0A
Other languages
Chinese (zh)
Inventor
张忠华
杨晓勤
熊俊
李俊
郭华文
齐北涛
张书培
窦强
邵兆强
王铮铮
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.)
Xinjiang Yihua Chemical Industry Co ltd
Original Assignee
Xinjiang Yihua Chemical Industry 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 Xinjiang Yihua Chemical Industry Co ltd filed Critical Xinjiang Yihua Chemical Industry Co ltd
Priority to CN202111104283.0A priority Critical patent/CN113790589A/en
Publication of CN113790589A publication Critical patent/CN113790589A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B11/00Machines or apparatus for drying solid materials or objects with movement which is non-progressive
    • F26B11/12Machines or apparatus for drying solid materials or objects with movement which is non-progressive in stationary drums or other mainly-closed receptacles with moving stirring devices
    • F26B11/16Machines or apparatus for drying solid materials or objects with movement which is non-progressive in stationary drums or other mainly-closed receptacles with moving stirring devices the stirring device moving in a vertical or steeply-inclined plane
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/001Drying-air generating units, e.g. movable, independent of drying enclosure
    • F26B21/002Drying-air generating units, e.g. movable, independent of drying enclosure heating the drying air indirectly, i.e. using a heat exchanger
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/004Nozzle assemblies; Air knives; Air distributors; Blow boxes
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B25/00Details of general application not covered by group F26B21/00 or F26B23/00
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D17/00Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
    • F27D17/004Systems for reclaiming waste heat
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D17/00Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
    • F27D17/008Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases cleaning gases
    • 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
    • Y02P10/00Technologies related to metal processing
    • Y02P10/25Process efficiency

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Processing Of Solid Wastes (AREA)
  • Drying Of Solid Materials (AREA)
  • Treatment Of Sludge (AREA)

Abstract

The utility model provides a realize energy-conserving high-efficient dry technology of carbide slag and device, includes preheater (1), hot-blast main (2), hot-blast furnace (3), stove air intake pipe (3I), stove air outlet pipe (3 II), carbide stove tail gas import pipe (3 III), stove air intake pipe (3 IV), helical fin (3V), hot-blast furnace outlet pipe (4), cecum (5), hot-blast main (6), carbide slag import (7), stoving-breaker (8), dry powder conveyer pipe (9), cyclone (10), dry powder storehouse (11). The invention has the following advantages: the hot blast stove (3) is added in the process, so that the drying efficiency is improved, and the tail gas of the calcium carbide furnace is recycled; the preheater 1 can recycle waste heat generated in chemical production. The upper and lower folding fins or spiral fins 3 (V) are arranged in the gap of the hot blast stove 3, so that the heat exchange area of the gap between the stoves is increased, and the air preheating efficiency is improved.

Description

Process and device for realizing energy-saving and efficient drying of carbide slag
Technical Field
The invention relates to the technical field of material drying, in particular to a process and a device for realizing energy-saving and efficient drying of carbide slag.
Background
Carbide slag belongs to general industrial solid wastes of class II and has dangerousness, and the existing treatment method mainly comprises landfill, production of building materials (such as cement) and the like. In the process of producing building materials, the carbide slag needs to be dried and crushed, the common method is to introduce the dust-containing tail gas of the rotary kiln into the drying and crushing process, but the heat of the dust-containing tail gas cannot meet the drying requirement of the carbide slag. On the other hand, the tail gas of the calcium carbide furnace contains a large amount of combustible gases including CO and H2、CH4And the combustion of these gases can release a large amount of heat energy and exit the furnace with the resulting high temperature gases. If not utilized, energy loss and waste are caused. Based on the technology, in order to realize the efficient drying of the carbide slag and the resource utilization of the tail gas of the carbide furnace, the invention introduces the high-temperature gas generated after the combustion of the tail gas of the carbide furnace into the links of drying and crushing the carbide slag, and develops the technology and the device for realizing the energy-saving and efficient drying of the carbide slag.
Disclosure of Invention
The invention provides an energy-saving and efficient carbide slag drying process and device, and simultaneously realizes full drying of carbide slag and resource utilization of carbide furnace tail gas.
In order to achieve the purpose, the invention adopts the following technical scheme: the utility model provides a realize energy-conserving high-efficient dry technology of carbide slag and device, the device includes pre-heater (1), hot-blast main (2), hot-blast furnace (3), stove air intake pipe (3I), stove air outlet pipe (3 II), carbide stove tail gas import pipe (3 III), stove air intake pipe (3 IV), helical fin (3V), hot-blast furnace outlet pipe (4), cecum (5), hot-blast main (6), carbide slag import (7), stoving-breaker (8), dry powder conveyer pipe (9), cyclone (10), dry powder storehouse (11). The dust-containing gas enters the preheater (1) through a pipeline, and the preheater (1) is connected with an outlet pipe (4) of the hot blast stove and a cecum (5) through a hot blast pipe (2). In the hot blast stove (3), air is connected with a gap between the outer wall of the stove and the inner wall of the stove through an air inlet (3I) between the stoves, spiral fins (3V) are arranged in the gap, the outer wall of the stove is connected with an air outlet pipe (3 II) between the stoves, and the air outlet pipe (3 II) between the stoves is connected with an air inlet (3 IV) in the stove. The tail gas inlet pipe (3 III) and the air inlet (3 IV) in the calcium carbide furnace are positioned at the bottom of the calcium carbide furnace (3). The hot-blast stove (3) is respectively connected with a hot-blast stove outlet pipe (4) and the cecum (5), and the hot-blast stove outlet pipe (4), the cecum (5) and the hot-blast pipe (6) are connected. The hot air pipe (6) and the carbide slag inlet (7) are both connected with a drying-crushing machine (8). The drying-crushing machine (8) is connected with a dry powder conveying pipe (9), the dry powder conveying pipe (9) is connected with a cyclone separator (10), and dry powder separated by the cyclone separator (10) enters a dry powder warehouse (11).
Compared with the existing carbide slag drying process and device, the invention has the following advantages.
1. According to the process and the device for realizing energy-saving and efficient drying of the calcium carbide slag, the hot blast stove (3) is added in the process, and the hot blast stove supplies heat source for the drying-crushing machine by burning the tail gas of the calcium carbide furnace, so that the drying efficiency is improved, and the tail gas of the calcium carbide furnace is recycled.
2. The invention relates to a process and a device for realizing energy-saving and efficient drying of carbide slag, wherein a preheater 1 is formed by combining a preheater and a cyclone separator, so that waste heat generated in chemical production can be recycled, and the aim of separating and preheating dust-containing gas can be fulfilled at the same time.
3. According to the process and the device for realizing energy-saving and efficient drying of the carbide slag, air is preheated in a gap between the inner wall and the outer wall of the hot blast stove (3), and the upper folding fin or the lower folding fin or the spiral fin (3V) is arranged in the gap, so that the heat exchange area of the gap between the stoves is increased, and the air preheating efficiency is improved.
4. According to the process and the device for realizing energy-saving and efficient drying of the carbide slag, the hot blast stove outlet pipe (4) is additionally arranged on the basis of the caecum (5) at the outlet of the original hot blast stove, so that dust in dust-containing gas is prevented from falling into the hot blast stove through the caecum (5).
Drawings
FIG. 1 is a process flow diagram of a process and a device for realizing energy-saving and efficient drying of carbide slag.
Detailed Description
The technical solution in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. It is to be understood that the described embodiments are merely a few embodiments of the invention, and not all embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
In the description of the present invention, it should be noted that the terms "top", "bottom", "outside", "inside", "top", "bottom", and the like indicate orientations or positional relationships based on those shown in the drawings, and are only for convenience of description and simplicity of description, but do not indicate or imply that the referred device or element must have a specific orientation, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention; the terms "first," "second," and "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance; furthermore, unless expressly stated or limited otherwise, the terms "mounted," "connected," and "connected" are intended to be construed broadly, as they may be fixedly connected, detachably connected, or integrally connected, for example; either directly or indirectly through intervening media, or through the communication between two elements. The specific meanings of the above terms in the present invention can be understood in specific cases to those skilled in the art.
The present invention will be described in further detail with reference to the accompanying drawings.
As shown in figure 1, the invention discloses a process and a device for realizing energy-saving and efficient drying of carbide slag, and the process and the device comprise a preheater (1), a hot air pipe (2), a hot air furnace (3), an inter-furnace air inlet pipe (3I), an inter-furnace air outlet pipe (3 II), a carbide furnace tail gas inlet pipe (3 III), an in-furnace air inlet pipe (3 IV), a spiral fin (3V), an hot air furnace outlet pipe (4), a cecum (5), a hot air pipe (6), a carbide slag inlet (7), a drying-crushing machine (8), a dry powder conveying pipe (9), a cyclone separator (10) and a dry powder warehouse (11).
The process unit is used for introducing dust-containing gas into a preheater (1) through a pipeline, wherein the preheater is composed of a cyclone separator and heat transfer equipment. The preheater (1) is connected with the hot blast stove (3) through the hot blast pipe (2) to supplement the shortage of heat. In the hot blast stove (3), air is connected with a gap between the outer wall of the stove and the inner wall of the stove through an air inlet (3I) between the stoves to preheat normal temperature air, in order to increase the heat exchange area, a spiral fin (3V) is arranged in the gap, the outer wall of the stove is connected with an air outlet pipe (3 II) between the stoves, and the air outlet pipe (3 II) between the stoves is respectively connected with a tail gas inlet (3 III) of the calcium carbide stove and an air inlet (3 IV) in the stove. The hot-blast stove (3) is respectively connected with a hot-blast stove outlet pipe (4) and the cecum (5), and the hot-blast stove outlet pipe (4), the cecum (5) and the hot-blast pipe (6) are connected. The hot air pipe (6) and the carbide slag inlet (7) are connected with a drying-crushing machine (8). The drying crusher (8) is connected with a dry powder conveying pipe (9), the dry powder conveying pipe (9) is connected with a cyclone separator (10), and dry powder separated by the cyclone separator (10) enters a dry powder warehouse (11).
It will be evident to those skilled in the art that the invention is not limited to the details of the foregoing illustrative embodiments, and that the present invention may be embodied in other specific forms without departing from the spirit or essential attributes thereof. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Furthermore, it should be understood that although the present description refers to embodiments, not every embodiment may contain only a single embodiment, and such description is for clarity only, and those skilled in the art should integrate the description, and the embodiments may be combined as appropriate to form other embodiments understood by those skilled in the art.

Claims (5)

1. A process and a device for realizing energy-saving and efficient drying of carbide slag comprise a preheater (1), a hot air pipe (2), a hot air furnace (3), an air inlet (3I) between furnaces, an air outlet pipe (3 II) between furnaces, a tail gas inlet pipe (3 III) of the carbide furnace, an air inlet pipe (3 IV) in the furnace, a spiral fin (3V), an outlet pipe (4) of the hot air furnace, a cecum (5), a hot air pipe (6), an carbide slag inlet (7), a drying-crushing machine (8), a dry powder conveying pipe (9), a cyclone separator (10) and a dry powder warehouse (11), and are characterized in that dust-containing gas enters the preheater (1) through a pipeline, the preheater (1) is connected with the hot air furnace (3) through the hot air pipe (2), in the hot air furnace (3), air is connected with a gap between the outer wall of the furnace and the inner wall of the furnace through the air inlet (3I) between furnaces, the spiral fins (3V) are arranged in the gap, the outer wall of the furnace is connected with an inter-furnace air outlet pipe (3 II), the inter-furnace air outlet pipe (3 II) is respectively connected with a calcium carbide furnace tail gas inlet (3 III) and a furnace air inlet (3 IV), the hot blast furnace (3) is respectively connected with a hot blast furnace outlet pipe (4) and a cecum (5), the hot blast furnace outlet pipe (4), the cecum (5) and a hot blast pipe (6) are connected, the hot blast pipe (6) and the carbide slag inlet (7) are both connected with a drying-crushing machine (8), the drying-crushing machine (8) is connected with a dry powder conveying pipe (9), the dry powder conveying pipe (9) is connected with a cyclone separator (10), and dry powder separated by the cyclone separator (10) enters a dry powder warehouse (11).
2. The process and the device for realizing the energy-saving and high-efficiency drying of the carbide slag as claimed in claim 1 are characterized in that the hot blast stove (3) can be connected in parallel by a single preheater or a plurality of preheaters.
3. The process and the device for realizing the energy-saving and high-efficiency drying of the carbide slag according to claim 1 are characterized in that air is preheated in a gap between the inner wall and the outer wall of the hot blast stove (3), and an upper folding fin or a lower folding fin or a spiral fin (3V) is arranged in the gap.
4. The process and the device for realizing the energy-saving and efficient drying of the carbide slag according to claim 1 are characterized in that the original cecum (5) is changed into an outlet pipe 4 of a hot blast stove with three 90-degree elbows.
5. The process and the device for realizing the energy-saving and efficient drying of the carbide slag according to claim 1 are characterized in that a blast cap used by a tail gas inlet (3 III) of the carbide furnace can be a plane porous blast cap or a blast cap used by a fluidized bed gasification furnace.
CN202111104283.0A 2021-09-22 2021-09-22 Process and device for realizing energy-saving and efficient drying of carbide slag Pending CN113790589A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202111104283.0A CN113790589A (en) 2021-09-22 2021-09-22 Process and device for realizing energy-saving and efficient drying of carbide slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202111104283.0A CN113790589A (en) 2021-09-22 2021-09-22 Process and device for realizing energy-saving and efficient drying of carbide slag

Publications (1)

Publication Number Publication Date
CN113790589A true CN113790589A (en) 2021-12-14

Family

ID=78878981

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202111104283.0A Pending CN113790589A (en) 2021-09-22 2021-09-22 Process and device for realizing energy-saving and efficient drying of carbide slag

Country Status (1)

Country Link
CN (1) CN113790589A (en)

Citations (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06117780A (en) * 1992-10-02 1994-04-28 Nippon Steel Corp Equipment for disposing of exhaust gas from electric furnace or scrap-preheating apparatus therefor
TW200944493A (en) * 2008-03-10 2009-11-01 Taiheiyo Cement Corp Cement manufacturing method
DE102009055942A1 (en) * 2009-11-26 2011-06-01 Chemisch-Thermische Prozesstechnik Gmbh Process and apparatus for purifying exhaust gases
CN102607287A (en) * 2012-04-10 2012-07-25 上海瑞恩能源投资有限公司 Ferro-nickel smelting process waste heat generating system
CN102620571A (en) * 2012-04-10 2012-08-01 上海瑞恩能源投资有限公司 Waste-heat power generating system in smelting process of rotary kiln and ore-smelting electric furnace
CN102661666A (en) * 2012-04-20 2012-09-12 南京苏冶钙业技术有限公司 Tail gas utilization method and tail gas utilization system of rotary lime kiln
DE102012013877A1 (en) * 2012-07-12 2014-01-16 Khd Humboldt Wedag Gmbh Process for the treatment of biomass in a plant for the production of cement
CN103575068A (en) * 2013-11-30 2014-02-12 河北联合大学 Lignite drying water recycling and drying tail gas recycling system
CN103922624A (en) * 2014-04-16 2014-07-16 南京凯盛国际工程有限公司 Clinker sintering system taking carbide slag as calcareous raw material and being used for treating smoke generated in waste incineration
CN103922625A (en) * 2014-04-16 2014-07-16 南京凯盛国际工程有限公司 System for drying and decomposing wet acetylene sludge and firing cement clinker by using wet acetylene sludge as calcium raw material
CN104131127A (en) * 2014-07-28 2014-11-05 四川金广实业(集团)股份有限公司 RKEF process nickel-iron smelting waste heat utilizing method
DE102013016701A1 (en) * 2013-10-08 2015-04-09 Khd Humboldt Wedag Gmbh Process for the denitrification of bypass exhaust gases in a plant for the production of cement clinker
CN108114589A (en) * 2018-02-07 2018-06-05 福建龙净脱硫脱硝工程有限公司 A kind of system and method for calcining flue gas desulfurization and dedusting auxiliary drying carbide slag
CN207850007U (en) * 2018-02-01 2018-09-11 广东世纪青山镍业有限公司 A kind of dry kiln heating system of dry laterite
CN207850029U (en) * 2018-02-01 2018-09-11 广东世纪青山镍业有限公司 A kind of pretreatment system of laterite
CN210346365U (en) * 2019-06-13 2020-04-17 扬州一川镍业有限公司 Rotary kiln high temperature flue gas recycle device
CN111589176A (en) * 2020-05-28 2020-08-28 中国石油化工股份有限公司 Semi-circulating FCC catalyst spray drying system

Patent Citations (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06117780A (en) * 1992-10-02 1994-04-28 Nippon Steel Corp Equipment for disposing of exhaust gas from electric furnace or scrap-preheating apparatus therefor
TW200944493A (en) * 2008-03-10 2009-11-01 Taiheiyo Cement Corp Cement manufacturing method
DE102009055942A1 (en) * 2009-11-26 2011-06-01 Chemisch-Thermische Prozesstechnik Gmbh Process and apparatus for purifying exhaust gases
CN102607287A (en) * 2012-04-10 2012-07-25 上海瑞恩能源投资有限公司 Ferro-nickel smelting process waste heat generating system
CN102620571A (en) * 2012-04-10 2012-08-01 上海瑞恩能源投资有限公司 Waste-heat power generating system in smelting process of rotary kiln and ore-smelting electric furnace
CN102661666A (en) * 2012-04-20 2012-09-12 南京苏冶钙业技术有限公司 Tail gas utilization method and tail gas utilization system of rotary lime kiln
DE102012013877A1 (en) * 2012-07-12 2014-01-16 Khd Humboldt Wedag Gmbh Process for the treatment of biomass in a plant for the production of cement
DE102013016701A1 (en) * 2013-10-08 2015-04-09 Khd Humboldt Wedag Gmbh Process for the denitrification of bypass exhaust gases in a plant for the production of cement clinker
CN103575068A (en) * 2013-11-30 2014-02-12 河北联合大学 Lignite drying water recycling and drying tail gas recycling system
CN103922624A (en) * 2014-04-16 2014-07-16 南京凯盛国际工程有限公司 Clinker sintering system taking carbide slag as calcareous raw material and being used for treating smoke generated in waste incineration
CN103922625A (en) * 2014-04-16 2014-07-16 南京凯盛国际工程有限公司 System for drying and decomposing wet acetylene sludge and firing cement clinker by using wet acetylene sludge as calcium raw material
CN104131127A (en) * 2014-07-28 2014-11-05 四川金广实业(集团)股份有限公司 RKEF process nickel-iron smelting waste heat utilizing method
CN207850007U (en) * 2018-02-01 2018-09-11 广东世纪青山镍业有限公司 A kind of dry kiln heating system of dry laterite
CN207850029U (en) * 2018-02-01 2018-09-11 广东世纪青山镍业有限公司 A kind of pretreatment system of laterite
CN108114589A (en) * 2018-02-07 2018-06-05 福建龙净脱硫脱硝工程有限公司 A kind of system and method for calcining flue gas desulfurization and dedusting auxiliary drying carbide slag
CN210346365U (en) * 2019-06-13 2020-04-17 扬州一川镍业有限公司 Rotary kiln high temperature flue gas recycle device
CN111589176A (en) * 2020-05-28 2020-08-28 中国石油化工股份有限公司 Semi-circulating FCC catalyst spray drying system

Similar Documents

Publication Publication Date Title
CN101591731B (en) Reduction roasting method and device for high-valence manganese ores
CN101318632B (en) Method for decomposing phosphogypsum to produce sulphuric acid and cement with suspended state
CN214571574U (en) Powdery lime calcining system
CN103373822A (en) Light calcined magnesia powder calcination device
CN111977995A (en) Powder lime calcining and reforming system based on novel dry-process cement clinker calcining system
CN111825350B (en) Device with light burned magnesia preparation and carbon dioxide collection functions
CN106282467A (en) A kind of iron mine fine coal base produces direct-reduction facilities and method
CN115340304A (en) Device and method for producing light-burned magnesium oxide through decomposition outside five-stage suspension preheating kiln
CN100431957C (en) Technique of fluidized instant calcinations of kaolin in coal series
CN203212470U (en) Temperature-controllable suspension roaster
CN101122388A (en) Method and device for making fluid bed to produce super high-temperature fume
CN211445544U (en) Method for capturing and purifying CO by using external combustion type rotary kiln in cement kiln2And an emission reduction system
CN113790589A (en) Process and device for realizing energy-saving and efficient drying of carbide slag
CN208038322U (en) A kind of lime shaft kiln cooling air cyclic utilization system
CN113045224B (en) System and method for preparing powdery active lime by modifying cement clinker production line
CN206916007U (en) A kind of new boiling limekiln
CN202543074U (en) Calcining device for producing light calcined magnesia powder
CN214792497U (en) Spodumene calcining and converting device
CN214009940U (en) Energy-saving suspension roasting coal gangue treatment system
CN212640307U (en) Device with light-burned magnesium oxide preparation and carbon dioxide collection functions
CN108855941A (en) A kind of steel slag micro mist using steel plant's waste heat flue gas selects powder system
CN107162443A (en) A kind of new boiling limekiln
CN204058259U (en) A kind of take coal dust as the roasting assembly of fuel
CN203699937U (en) System for producing alpha-Al2O3 by adopting predecomposition process by taking hydrogen and aluminum as raw materials
CN101255989A (en) Sorting kiln outside cement kiln having furnace for cremation of house refuse

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
WD01 Invention patent application deemed withdrawn after publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20211214