CN1766071A - Gasifying coal for water gas furnace - Google Patents
Gasifying coal for water gas furnace Download PDFInfo
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- CN1766071A CN1766071A CN 200510110558 CN200510110558A CN1766071A CN 1766071 A CN1766071 A CN 1766071A CN 200510110558 CN200510110558 CN 200510110558 CN 200510110558 A CN200510110558 A CN 200510110558A CN 1766071 A CN1766071 A CN 1766071A
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
- Y02E20/18—Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]
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Abstract
Disclosed is a gasifying coal for water gas furnace made from mixed coal powder and bonding agent, wherein the mixed coal powder comprises (by weight ratio) anthracite coal 85-95%, bituminous coal 0-8%, brown coal 0-8%, aqueous solution of sodium silicate 3-12%, alta-mud 2-7%, potassium chloride 0.1-0.5%.
Description
Technical field: the present invention relates to a kind of moulded coal, particularly a kind of gasifying coal for water gas furnace gasification briquette that can 100% substitutes lump coal fully.
Background technology:
The chemical industry synthetic raw gas is the important application of Coal Gasification Technology at the national economy industrial circle, and wherein, synthetic ammonia occupies significant proportion in synthetic Chemicals.China produces the chemical industry synthetic raw gas, and to use maximum be blue-gas generator, fertilizer industry have more than 80% unstripped gas by in, the blue-gas generator production of small fertilizer plant.And that the raw material of blue-gas generator requires with the ature of coal figureofmerit is very high, is coal the strictest index during as primary energy source; For a long time, the domestic market is according to standard GB 7561-87 " synthetic ammonia with ature of coal amount standard ", to chemical fertilizers production enterprise supply high-quality anthracite block coal.Geology is different with envrionment conditions because coal generates, and various places hard coal mass discrepancy is very big, can be used as synthetic ammonia feedstock and uses the quantity of coal few; Along with coal mining machines degree improves, the lump coal recovery ratio only is about 20%, and this causes, and synthetic ammonia feedstock is more outstanding with the imbalance between supply and demand of coal shortage in recent years, the lump coal spurt in prices.Thereby make can utilize, relatively inexpensive coal powder formation substitutes lump coal and makes the technology of chemical industry synthetic raw gas and obtain day by day paying attention to.
Moulded coal gas making can solve problems such as anthracite fine coal overstocks in a large number, the wasting of resources, lump coal shortage, has reduced the chemical fertilizers production cost again.But because the complicacy of ammonia synthesis process, existing various moulded coals are not suitable for blue-gas generator; Can only mix burning with lump coal, mixed-fuel burning proportion is no more than 10-15%, and reactive behavior is starkly lower than lump coal, and it is insufficient to burn, lime-ash carbon residue rate height, and substitution effect is poor.Existing various moulded coals are not suitable for the major cause of blue-gas generator, are the special gasifying process requirements of failing to solve blue-gas generator; The making key of blue-gas generator gasification briquette is high temperature resistant powdered coal adhesion agent technology.The moulded coal that existing various adhesive techniques are made, its cold strength all can't be compared with replaced lump coal with hot strength, and general cold strength is lower than the 60Kg/ ball, and hot strength is lower; But the blue-gas generator gasification briquette is then just in time opposite to the requirement of intensity, requires hot strength to be higher than cold strength; Otherwise under the hot environment, moulded coal is very easily broken, produces dust in blue-gas generator, causes taking place gas stream in the stove and stops up, and gasification is uneven, hinders gasification reaction and normally carries out; The carry-over that meanwhile gasifies increases, and gasification efficiency is reduced.
Summary of the invention:
The purpose of this invention is to provide a kind of lump coal that can 100% substitutes fully and be used for the synthetic ammonia gasification moulded coal that blue-gas generator is made the chemical industry synthetic raw gas.Mainly solve existing moulded coal reactive behavior and be starkly lower than lump coal, it is insufficient to burn, the technical problem that lime-ash carbon residue rate is high.Solve this technical problem, must solve three problems.At first be the preparation of fine coal raw material, comprise that direct employing meets the fine coal of GB7561-87 " synthetic ammonia with ature of coal amount standard " coal index; Or be that main raw material is mixed in proportion with other raw coal of different atures of coal with the hard coal, adjust ature of coal, make and mix the requirement that fine coal reaches the main coal index of GB7561-87 " synthetic ammonia with ature of coal amount standard ".Secondly need to select the main composition material of the high temperature resistant powdered coal adhesion agent of preparation.Be the proportioning of determining the various composition materials of briquette binder at last.Patent of invention ZL00135180.X provides a kind of briquette molding method with through-hole structure, test shows, this through-hole structure moulded coal uses the present invention to help the air channel effect to make the moulded coal utilising efficiency reach almost ideal degree by nationality, and the lime-ash carbon residue rate after being gasified totally in blue-gas generator approaches zero.The lime-ash carbon residue rate of blue-gas generator is to characterize qualitative, the quantitative target whether coal is fully utilized, and blue-gas generator uses the high-quality anthracite block coal, and lime-ash carbon residue rate just can reach about 10% under better working of a furnace processing condition.But this patent does not provide to make and meets the main coal index of GB7561-87 " synthetic ammonia with ature of coal amount standard ", is specifically designed to the briquette binder compound method of chemical industry synthetic raw gas.The present invention can make the range of application of this patent be expanded.
Technical scheme of the present invention is: at first carry out the fine coal feedstock production: obtain synthetic ammonia gasification fine coal raw material by blending method, adjust main coal index and make volatile matter≤10%, ash content＜16 ∽ 24%, fixed carbon＞65 ∽ 75%, moisture＜6%; When between ash content, the fixed carbon content when contradictory, be as the criterion with ash content; Mix the main coal index of fine coal, participate in the weighted mean of the corresponding coal index of various raw coal of coal blending exactly, calculation formula is as follows:
The corresponding coal index of raw coal * this raw coal that the coal index=∑ that mixes fine coal participates in coal blending accounts for the per-cent that mixes fine coal after the coal blending
Wherein, this raw coal accounts for the per-cent that mixes fine coal after the coal blending, the coal index that need adjust by main raw coal and this coal index of waiting to join raw coal, and this coal index that mixes fine coal is determined jointly.Be described as follows:
If in mixed coal powder and binding agent total amount 100%, mixed coal powder comprises pulverized anthracite, pulverized bituminous coal, brown coal coal dust, and high temperature resistant powdered coal adhesion agent comprises: sodium silicate aqueous solution, wilkinite, Potcrate; The weight percent ratio range that each component is concrete is as follows:
Hard coal 85%-95%
Bituminous coal 0-8%
Brown coal 0-8%
Sodium silicate aqueous solution 3%-12%
Wilkinite 2%-7%
Potcrate 0.1%-0.5%
High temperature resistant powdered coal adhesion agent proportion technique provided by the invention, compare with existing other briquette binder, have following remarkable advantage: cold strength can reach the 100Kg/ ball, and above (testing standard: MT/T 748-1997 " industrial shaping coal cold pressing strength measuring method "), hot strength can reach 120Kg/ ball above (recommending testing method by Inst. of Coal Industry, Fujian Province); Thermostability 〉=80% (testing standard: MT/T 924-2003 " industrial shaping coal thermal stability determination method "), ash fusibility＞1350 ℃ (testing method is according to GB/T 212-2001 " the technical analysis method of coal "); It is low to have overcome existing other briquette binder cold strength fully, and hot strength is lower than the drawback of cold strength, helps moulded coal and maintains the original state in blue-gas generator, and gasification is stable, and gasification efficiency greatly improves; In addition, adopt binding agent proportion technique of the present invention, can reduce the binding agent consumption, compare, can improve moulded coal fixed carbon content relatively, thereby finally reach the effect that increases chemical industry synthetic raw gas gas production rate with existing other briquette binder.
Therefore, the through-hole structure moulded coal that uses the present invention to make is a kind ofly can 100% to substitute lump coal fully and be used for blue-gas generator, makes the synthetic ammonia gasification moulded coal of chemical industry synthetic raw gas.
Preparation method of the present invention comprises two steps: at first carry out the configuration of mixed coal powder by proportioning, add binding agent by proportioning then and be prepared according to the common process that moulded coal prepares.
Embodiment: embodiment 1-4, each composition weight proportioning of the present invention sees the following form
| Hard coal % | Bituminous coal % | Brown coal % | Sodium silicate aqueous solution % | Wilkinite % | Potcrate % | |
| The present invention | 85-95 | 0-8 | 0-8 | 3-12 | 2-7 | 0.1-0.5 |
| Embodiment 1 | 85 | 1 | 2 | 8 | 3.5 | 0.5 |
| Embodiment 2 | 88 | 2 | 4 | 3 | 2.8 | 0.2 |
| Embodiment 3 | 93 | 0 | 0 | 4 | 2.7 | 0.3 |
| Embodiment 4 | 86 | 5 | 1 | 3 | 4.8 | 0.2 |
The fine coal preparation method for raw material of gasifying coal for water gas furnace is mixed main raw coal (hard coal), raw coal to be joined (bituminous coal), raw coal to be joined (brown coal) in proportion, adjusts ature of coal, obtains mixing fine coal after reaching the main coal index requirement of GB7561-87; Add sodium silicate aqueous solution, wilkinite, Potcrate by proportioning then; Make the common process flow process according to moulded coal, the powder that will meet the moulding requirement is sent into molding device, after the oven dry of moulded coal making common process flow process, makes gasifying coal for water gas furnace.Concrete preparation method is with reference to patent of invention ZL00135180.X.
Claims (2)
1, gasifying coal for water gas furnace, form by mixed coal powder and binding agent, it is characterized in that: mixed coal powder is made up of pulverized anthracite, pulverized bituminous coal, brown coal coal dust, described binding agent is that high temperature resistant powdered coal adhesion agent is made up of sodium silicate aqueous solution, wilkinite, Potcrate, and the weight percent ratio range of each component is as follows:
Hard coal 85%-95%
Bituminous coal 0-8%
Brown coal 0-8%
Sodium silicate aqueous solution 3%-12%
Wilkinite 2%-7%
Potcrate 0.1%-0.5%.
2, gasifying coal for water gas furnace according to claim 1 is characterized in that: described moulded coal is the through-hole structure moulded coal.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005101105586A CN100360647C (en) | 2005-11-21 | 2005-11-21 | Gasifying coal for water gas furnace |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005101105586A CN100360647C (en) | 2005-11-21 | 2005-11-21 | Gasifying coal for water gas furnace |
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| Publication Number | Publication Date |
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| CN1766071A true CN1766071A (en) | 2006-05-03 |
| CN100360647C CN100360647C (en) | 2008-01-09 |
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| CNB2005101105586A Expired - Fee Related CN100360647C (en) | 2005-11-21 | 2005-11-21 | Gasifying coal for water gas furnace |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101275086B (en) * | 2008-05-15 | 2011-03-16 | 王承信 | Joint production method for methanol and synthesis ammonia |
| CN105419834A (en) * | 2015-12-01 | 2016-03-23 | 西安科技大学 | Method for preparing formed coke |
| CN106587069A (en) * | 2016-12-14 | 2017-04-26 | 昆明理工大学 | Brown coal semi-coke reducing agent used for industrial silicon production and preparation method thereof |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3441757A1 (en) * | 1984-11-15 | 1986-05-15 | Metallgesellschaft Ag, 6000 Frankfurt | METHOD FOR PRODUCING CARBONATED PELLETS FOR GASIFICATION |
| CN1039051A (en) * | 1988-07-01 | 1990-01-24 | 赵庆纯 | Inorganics bonding formed coke (coal) and moulding process thereof |
| CN1062592C (en) * | 1996-06-28 | 2001-02-28 | 北京建昊实业公司 | High-efficieney pollution-reducing and coal-saving agent |
| CN1199904C (en) * | 2003-05-07 | 2005-05-04 | 淄博博纳科技发展有限公司 | Building material additives with automatic humidity-regulating function and preparation process and use thereof |
-
2005
- 2005-11-21 CN CNB2005101105586A patent/CN100360647C/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101275086B (en) * | 2008-05-15 | 2011-03-16 | 王承信 | Joint production method for methanol and synthesis ammonia |
| CN105419834A (en) * | 2015-12-01 | 2016-03-23 | 西安科技大学 | Method for preparing formed coke |
| CN106587069A (en) * | 2016-12-14 | 2017-04-26 | 昆明理工大学 | Brown coal semi-coke reducing agent used for industrial silicon production and preparation method thereof |
| CN106587069B (en) * | 2016-12-14 | 2019-06-11 | 昆明理工大学 | A kind of industrial silicon production lignite semi-coke reducing agent and preparation method thereof |
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| CN100360647C (en) | 2008-01-09 |
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Assignee: Xiamen profit Xuan Industrial Co., Ltd. Assignor: Shanghai Yuanbao Energy Techn Co., Ltd. Contract fulfillment period: 2009.7.22 to 2025.11.20 contract change Contract record no.: 2009310000145 Denomination of invention: Gasifying coal for water gas furnace Granted publication date: 20080109 License type: General permission Record date: 2009.8.4 |
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Free format text: COMMON LICENSE; TIME LIMIT OF IMPLEMENTING CONTACT: 2009.7.22 TO 2025.11.20; CHANGE OF CONTRACT Name of requester: XIAMEN YINGLIXUAN INDUSTRY CO.,LTD. Effective date: 20090804 |
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Owner name: XIAMEN GUOBEN NEW ENERGY TECHNOLOGY CO., LTD. Free format text: FORMER OWNER: SHANGHAI YUANBAO ENERGY TECHN CO., LTD. Effective date: 20110302 |
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Free format text: CORRECT: ADDRESS; FROM: 200092 ROOM 403, NO.17, LANE 242, TIANBAO WEST ROAD, HONGKOU DISTRICT, SHANGHAI TO: 361000 UNIT 201E, NO.16, XINFENG ROAD 3, TORCH PARK, TORCH NEW AND HIGH TECHNOLOGY AREA, XIAMEN CITY, FUJIAN PROVINCE |
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Effective date of registration: 20110302 Address after: 361000 201E unit, torch 16, three Xinfeng Road, torch hi tech Zone, Fujian, Xiamen Patentee after: Xiamen Guoben New Energy Technology Co.,Ltd. Address before: 200092, room 17, No. 242, Lane 403, Tianbao West Road, Shanghai, Hongkou District Patentee before: Shanghai Yuanbao Energy Techn Co., Ltd. |
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