CN104449846A - Preparation and conveying method and preparation and conveying device of pulverized coal - Google Patents

Preparation and conveying method and preparation and conveying device of pulverized coal Download PDF

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Publication number
CN104449846A
CN104449846A CN201410741541.XA CN201410741541A CN104449846A CN 104449846 A CN104449846 A CN 104449846A CN 201410741541 A CN201410741541 A CN 201410741541A CN 104449846 A CN104449846 A CN 104449846A
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CN
China
Prior art keywords
coal
pulverized coal
coal dust
preparation
conveying
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
CN201410741541.XA
Other languages
Chinese (zh)
Inventor
丁振伟
郭洪君
李�杰
程建光
冯宜河
李宗立
韩梅
褚宏春
袁明磊
马怀振
吕洪浩
王建军
台波
许广宇
金俊杰
唐高荣
吴艳军
陈超
谢勇
曹昭军
张国连
金刚
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.)
Yankuang Group Corp Ltd
Original Assignee
GUIZHOU KAIYANG CHEMICAL 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 GUIZHOU KAIYANG CHEMICAL CO Ltd filed Critical GUIZHOU KAIYANG CHEMICAL CO Ltd
Priority to CN201410741541.XA priority Critical patent/CN104449846A/en
Publication of CN104449846A publication Critical patent/CN104449846A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension
    • C10J3/48Apparatus; Plants
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension
    • C10J3/48Apparatus; Plants
    • C10J3/50Fuel charging devices
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72Other features
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913Carbonaceous raw material
    • C10J2300/093Coal
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953Gasifying agents
    • C10J2300/0956Air or oxygen enriched air

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Disintegrating Or Milling (AREA)

Abstract

The invention discloses a preparation and conveying method and a preparation and conveying device of pulverized coal. The method comprises the steps of pulverized coal preparation and pulverized coal conveying; the negative-pressure pulverization technology is adopted for preparing the pulverized coal, pulverized coal leakage can be effectively prevented, the explosive-proof grade of the device can be lowered and the investment can be reduced; a fume furnace provides hot air for drying and conveying the pulverized coal in a coal pulverizer, fuel gas in the fume furnace can release heat through liquefied petroleum gas or purge gas in the system, and the energy consumption cost can be reduced; fiber impurities contained in the pulverized coal collected by a pulverized coal collecting device can be removed by a fiber separator or a vibrating screen, and then the pulverized coal enters a pulverized coal storage cabin, the pulverized coal under normal pressure in the pulverized coal storage cabin can enter a pulverized coal charging tank under the dual actions of gravity and activated gas after passing through two or three pressure charging and releasing cycling lock hopper vessels, a certain pressure difference exists between the pulverized coal charging tank and a gasifier, and the flow rate of the pulverized coal can be controlled by a regulating valve; the impurities in the pulverized coal can be removed in a conveying process, and besides, multiple pressure charging and releasing cycling lock hopper vessels can ensure stable discharging; and the design is exquisite, the cost is low and the using effect is good.

Description

The preparation of coal dust and carrying method and device
Technical field
The present invention relates to chemical field, especially a kind of preparation of coal dust and carrying method and device.
Background technology
Pulverized coal gasification furnace uses raw material to be coal dust, and combustion reactions and coal dust conveying all have strict demand to the granularity, water-content etc. of coal dust.Existing coal dust is produced can produce higher pressure usually, and therefore, for meeting gasification reaction needs, usual device anti-hazard classification requires higher, and the cost of investment of equipment is also larger, and existing production technology energy consumption is also higher.Coal dust is after production completes, and its impurity is many, and transport neither be very convenient.
Summary of the invention
The object of the invention is: provide a kind of preparation of coal dust and carrying method and device, its production safety is reliable, and equipment cost is low, effectively can remove the impurity in coal dust, and conveying good stability, to overcome the deficiencies in the prior art.
The present invention is achieved in that preparation and the carrying method of coal dust, comprises the preparation of coal dust and the conveying of fine coal, and the preparation of coal dust is, after feed coal being sent into raw material coal bunker, coal to be fed fuel dropping pipe through feeder and enters coal pulverizer and be polished by the coal in raw material coal bunker; Warm air is provided to enter in coal pulverizer in combustion gas furnace, the coal dust that fineness is qualified rises with warm air, being entered by transfer lime receives in powder device, after the fine coal that warm air is brought into by receipts powder device is collected, one branch's warm air is sent back in rear combustion gas furnace by induced draft fan and circulates, another warm air is exported emptying by induced draft fan; The conveying of coal dust is, to the coal dust of powder device collection be received by sending into coal dust bunker after the fiber impurity in separating screen device removing coal dust, normal pressure pulverized coal in coal dust bunker is entered powder coal charge tank after lock hopper container under gravity and activation gas dual function, and coal dust is sent in vapourizing furnace by powder coal charge tank.
The preparation of coal dust and the device of carrying method, be divided into fuel pulverizing plant and pulverized coal conveying device, fuel pulverizing plant comprises combustion gas furnace, the output terminal of combustion gas furnace is communicated with the bottom of coal pulverizer by pipeline, the top of coal pulverizer is connected with receipts powder device by pipeline, and the air vout end receiving powder device connects drain and combustion gas furnace respectively by the pipeline with induced draft fan; Pulverized coal conveying device comprises the separating screen device be connected with the powder outlet end receiving powder device, is provided with coal dust bunker, is connected with coal dust lock hopper container in the bottom of coal dust bunker, be connected with powder coal charge tank in the bottom of coal dust lock hopper container in the below of separating screen device.
Described separating screen device is Celloco fractionator Celloco or vibratory screening apparatus.
Described coal dust lock hopper container is two or more.
Owing to have employed technique scheme, compared with prior art, pulverized coal preparation of the present invention adopts negative pressure powder-making technique, effectively can prevent leakage of pulverized coal, reduces device anti-hazard classification, reduces investment; Combustion gas furnace provides the drying of warm air for coal dust in coal pulverizer and conveying, and combustion gas furnace fuel gas can use liquefied petroleum gas (LPG) or system periodic off-gases to produce heat, reduces energy consumption cost; Coal dust bunker is entered after the coal dust that coal powder collection device is collected removes by Celloco fractionator Celloco or vibratory screening apparatus the fiber impurity contained in coal dust, again normal pressure pulverized coal in coal dust bunker is entered powder coal charge tank after the coal dust lock hopper container of pressure release is filled in two or three circulations under gravity and activation gas dual function, powder coal charge tank and vapourizing furnace keep certain pressure reduction, by governor valve control pulverized coal flow.Not only eliminate the impurity in coal dust in course of conveying, and the lock hopper container that pressure release is filled in multiple circulation can ensure the stable of blanking.Deft design of the present invention, with low cost, result of use is good.
Accompanying drawing explanation
Accompanying drawing 1 is the structural representation of fuel pulverizing plant of the present invention;
Accompanying drawing 2 is the structural representation of pulverized coal conveying device of the present invention.
Embodiment
Embodiments of the invention: the preparation of coal dust and carrying method, comprise the preparation of coal dust and the conveying of fine coal, and the preparation of coal dust is, after feed coal being sent into raw material coal bunker, coal to be fed fuel dropping pipe through feeder and enters coal pulverizer 3 and be polished by the coal in raw material coal bunker; Warm air is provided to enter in coal pulverizer 3 in combustion gas furnace 2, the coal dust that fineness is qualified rises with warm air, entered by transfer lime 1 and receive the cloth bag collection machine that powder device 4(can adopt routine) in, after the fine coal that warm air is brought into by receipts powder device 4 is collected, one branch's warm air is sent back in rear combustion gas furnace 2 by induced draft fan 6 and circulates, another warm air is exported emptying by induced draft fan 6; The conveying of coal dust is, the coal dust collected by receipts powder device 4 sends into coal dust bunker 8 removed the fiber impurity in coal dust by separating screen device 7 after, normal pressure pulverized coal in coal dust bunker 8 is entered powder coal charge tank 10 after lock hopper container 9 under gravity and activation gas dual function, and coal dust is sent in vapourizing furnace 11 by powder coal charge tank 10.
The preparation of coal dust and the device of carrying method, be divided into fuel pulverizing plant and pulverized coal conveying device, fuel pulverizing plant comprises combustion gas furnace 2, the output terminal of combustion gas furnace 2 is communicated with the bottom of coal pulverizer 3 by pipeline 1, the top of coal pulverizer 3 is connected with receipts powder device 4 by pipeline 1, and the air vout end receiving powder device 4 connects drain 5 and combustion gas furnace 2 respectively by the pipeline 1 with induced draft fan 6; Pulverized coal conveying device comprises the separating screen device 7 be connected with the powder outlet end receiving powder device 4, coal dust bunker 8 is provided with in the below of separating screen device 7, be connected with three coal dust lock hoppers 9 in the bottom of coal dust bunker 8, be connected with powder coal charge tank 10 in the bottom of coal dust lock hopper 9; Described separating screen device 7 is Celloco fractionator Celloco or vibratory screening apparatus.

Claims (4)

1. the preparation of coal dust and a carrying method, comprise the preparation of coal dust and the conveying of fine coal, it is characterized in that: the preparation of coal dust is, after feed coal being sent into raw material coal bunker, coal to be fed fuel dropping pipe through feeder and enters coal pulverizer and be polished by the coal in raw material coal bunker; Warm air is provided to enter in coal pulverizer in combustion gas furnace, the coal dust that fineness is qualified rises with warm air, being entered by transfer lime receives in powder device, after the fine coal that warm air is brought into by receipts powder device is collected, one branch's warm air is sent back in rear combustion gas furnace by induced draft fan and circulates, another warm air is exported emptying by induced draft fan; The conveying of coal dust is, to the coal dust of powder device collection be received by sending into coal dust bunker after the fiber impurity in separating screen device removing coal dust, normal pressure pulverized coal in coal dust bunker is entered powder coal charge tank after lock hopper container under gravity and activation gas dual function, and coal dust is sent in vapourizing furnace by powder coal charge tank.
2. one kind adopts the preparation of coal dust as claimed in claim 1 and the device of carrying method, be divided into fuel pulverizing plant and pulverized coal conveying device, it is characterized in that: fuel pulverizing plant comprises combustion gas furnace (2), it is characterized in that: the output terminal of combustion gas furnace (2) is communicated with the bottom of coal pulverizer (3) by pipeline (1), the top of coal pulverizer (3) is connected with receipts powder device (4) by pipeline (1), and the air vout end receiving powder device (4) connects drain (5) and combustion gas furnace (2) respectively by the pipeline (1) with induced draft fan (6); Pulverized coal conveying device comprises the separating screen device (7) be connected with the powder outlet end receiving powder device (4), coal dust bunker (8) is provided with in the below of separating screen device (7), be connected with coal dust lock hopper container (9) in the bottom of coal dust bunker (8), be connected with powder coal charge tank (10) in the bottom of coal dust lock hopper container (9).
3. the preparation of coal dust according to claim 2 and e Foerderanlage, is characterized in that: described separating screen device (7) is Celloco fractionator Celloco or vibratory screening apparatus.
4. the preparation of coal dust according to claim 2 and e Foerderanlage, is characterized in that: described coal dust lock hopper container (9) is two or more.
CN201410741541.XA 2014-12-09 2014-12-09 Preparation and conveying method and preparation and conveying device of pulverized coal Pending CN104449846A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410741541.XA CN104449846A (en) 2014-12-09 2014-12-09 Preparation and conveying method and preparation and conveying device of pulverized coal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410741541.XA CN104449846A (en) 2014-12-09 2014-12-09 Preparation and conveying method and preparation and conveying device of pulverized coal

Publications (1)

Publication Number Publication Date
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107954218A (en) * 2017-12-13 2018-04-24 航天长征化学工程股份有限公司 Coal grinding and pulverized coal conveying system
CN109652142A (en) * 2019-01-22 2019-04-19 安徽昊源化工集团有限公司 A kind of control method for powdered coal pressure and transferring program for powdered coal gasification

Citations (8)

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Publication number Priority date Publication date Assignee Title
CN101037620A (en) * 2007-04-27 2007-09-19 兖矿鲁南化肥厂 Coal spraying nozzle for coal gasification device and combustion device
CN101294765A (en) * 2008-06-05 2008-10-29 神华集团有限责任公司 Low rank coal high temperature flue gas drying method and device
CN101939264A (en) * 2007-11-09 2011-01-05 芬欧汇川集团 Waste water treatment from a biomass-to-liquid process comprising synthesis gas production and integrated factory facility
CN102140371A (en) * 2010-12-11 2011-08-03 水煤浆气化及煤化工国家工程研究中心 Pulverized coal gasification device capable of measuring feeding quantity and performing on-line calibration of solid mass flow meter and on-line calibration method thereof
CN102352268A (en) * 2011-09-08 2012-02-15 西北化工研究院 Method for producing synthesis gas by using coal powder as raw material
CN102559272A (en) * 2011-12-29 2012-07-11 武汉凯迪工程技术研究总院有限公司 Microwave plasma biomass entrained flow gasifier and process
CN203174052U (en) * 2013-01-30 2013-09-04 河南开祥精细化工有限公司 Powder feeding system of gasification furnace
CN204325267U (en) * 2014-12-09 2015-05-13 贵州开阳化工有限公司 The preparation of coal dust and e Foerderanlage

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101037620A (en) * 2007-04-27 2007-09-19 兖矿鲁南化肥厂 Coal spraying nozzle for coal gasification device and combustion device
CN101939264A (en) * 2007-11-09 2011-01-05 芬欧汇川集团 Waste water treatment from a biomass-to-liquid process comprising synthesis gas production and integrated factory facility
CN101294765A (en) * 2008-06-05 2008-10-29 神华集团有限责任公司 Low rank coal high temperature flue gas drying method and device
CN102140371A (en) * 2010-12-11 2011-08-03 水煤浆气化及煤化工国家工程研究中心 Pulverized coal gasification device capable of measuring feeding quantity and performing on-line calibration of solid mass flow meter and on-line calibration method thereof
CN102352268A (en) * 2011-09-08 2012-02-15 西北化工研究院 Method for producing synthesis gas by using coal powder as raw material
CN102559272A (en) * 2011-12-29 2012-07-11 武汉凯迪工程技术研究总院有限公司 Microwave plasma biomass entrained flow gasifier and process
CN203174052U (en) * 2013-01-30 2013-09-04 河南开祥精细化工有限公司 Powder feeding system of gasification furnace
CN204325267U (en) * 2014-12-09 2015-05-13 贵州开阳化工有限公司 The preparation of coal dust and e Foerderanlage

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107954218A (en) * 2017-12-13 2018-04-24 航天长征化学工程股份有限公司 Coal grinding and pulverized coal conveying system
CN109652142A (en) * 2019-01-22 2019-04-19 安徽昊源化工集团有限公司 A kind of control method for powdered coal pressure and transferring program for powdered coal gasification

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TA01 Transfer of patent application right

Effective date of registration: 20160308

Address after: 273500 Shandong city of Jining province Fushan Road No. 298

Applicant after: YANKUANG GROUP Co.,Ltd.

Address before: Guizhou province Guiyang City Kaiyang County 550306 Yong Wen Xiang Huang Bai wells

Applicant before: GUIZHOU KAIYANG CHEMICAL Co.,Ltd.

SE01 Entry into force of request for substantive examination
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Application publication date: 20150325

RJ01 Rejection of invention patent application after publication