• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    1523500 Multi-type particle fluidised bed BATTELLE DEVELOPMENT CORP 13 Oct 1976 [21 Oct 1975] 42588/76 Heading B1F [Also in Division C5] A method of operating a fluidized bed, e.g. for the efficient reaction between at least two reactants comprises (i) forming an entrained or lean phase fluidized bed in a first space region e.g. as shown as I in Fig. 2, containing a first solid bed particle component 60, (ii) forming in a more limited space region II within the first region a dense phase fluidized bed containing a second solid bed particle component 62 essentially comprising a material having longterm physical and chemical stability in the fluidized bed so as to be substantially non- agglomerating and not subject to substantial attrition therein, (iii) providing a recirculation path e.g. via separator 36, reservoir chamber 74 and recycle conduit 76, for the first particle component from the first space region through the dense fluidized bed in the more limited space region and (iv) operating the fluidized bed at a velocity such that the second component particles are effectively retained in the dense fluidized bed in the more limited space region, whereas the first component particles recirculate and interpenetrate therethrough, commingling with the second component particles. Most preferably the fluidized bed is used for the gasification of a carbonaceous material, the bed being fluidized with the gaseous reactant e.g. air and heat being withdrawn as an energy product. It is preferred that most of the carbonaceous material e.g. coal is burned in the dense fluidized bed. If the coal contains sulphur a sulphur sorbent e.g. calcium and/or magnesium carbonate may be fed into the system. The bed particle components may be an oxide of iron, aluminium oxide, nickel, nickel oxide or a carbonate of calcium and/or magnesium. Both components may be of the same material, in which case the first component is of smaller particle size than the second component.
    公开号:SU1258334A3
    申请号:SU2414096
    申请日:1976-10-21
    公开日:1986-09-15
    发明作者:Нэк Герман；Лиу Ке-Тиен
    申请人:Баттеле Дивелопмент Корп. (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to a method for treating fuel, in particular to a method for chemical treatment of fuel, and can be used in fuel combustion plants.
    The aim of the invention is to improve the economy by reducing underburning.
    The drawing shows an installation for carrying out the method of chemical treatment of fuel.
    The installation contains a combustion chamber 1, the lower part of which is provided with a pipe 2 for supplying fuel and, if necessary, a sulfur bonding agent, a pipe 3 for supplying oxygen-containing gas, for example air, a perforated distribution element 4, and also a pipe 5 dp for feeding a fine-grained component 6 and the coarse-grained component 7. In this case, the nozzle 5 includes the other nozzle indicated by the arrow 8 for air supply. The combustion chamber I is connected to the cyclone separator 9 through a pipe} 0, installed in its upper part, and a pipeline P with a ball KJta placed in it. Powder limestone,
    kg / h5.44 22.4 .10.5
    Primary air
    m / nin1,322,991,98
    Together with fuel, m VMHH
    four
    Secondary, m / min
    Fine-grained component
    In the area between the distribution element 4 and the pipe 5. In the separator 9, the particles of the fine-grained component are separated from the gas stream flowing through the pipeline 10 and recycled to the combustion chamber 1 through pipeline 1I. The lower part of the separator 9 is equipped with
    a container 13 for collecting fine-grained particles having a sight glass 14 and a conduit 15 for diverting ash 16 into the container 16, which fall together with the fine-grained particles into 13. The ash is removed by introducing air into the container 13 in the direction of the arrow 17. Recycling fine-grained particles into combustion chamber 1 contributes air supply
    and the pipe 11 in the direction of the arrow 18. The cyclone separator 9 is equipped with a pipe 19 for removal of the purified gas stream for further processing and disposal. In chamber 1
    Combustion placed boiler 20.
    The table shows examples of the method for chemical processing of the process in a fluidized bed.
    0.50
    The average ratio of fine-grained and coarse-grained particles
    Surface speed, m / s
    Absorption Wednesday,%
    Fuel utilization rate,%
    Compiled by V. Kruglsky Editor I. Rybchenko Tekhred L. Serdyukov and Proofreader G. Reshetnik
    Order 5046/61 Circulation 514Subscription
    VNIIPI State Committee of the USSR
    for inventions and discoveries 113035, Moscow, Zh-35, Raushsk nab., 4/5
    Production and printing company, Uzhgorod, st. Project, 4
    Continuation of the table
    0.264
    10.5
    93.9
    98.4
    96.2
    权利要求:
    Claims (1)
    [1]
    METHOD FOR CHEMICAL PROCESSING OF FUEL IN A PSEUDO-FLUIDED LAYER containing a fine-grained component and an inert wear-resistant coarse-grained component with a ratio of their sizes equal to 0.0750.854, by feeding the indicated components, fuel and oxygen-containing gas into the lower part of the fluidized bed, moving the fine-grained component upward from below followed by its removal and return to the lower part of the layer, characterized in that, in order to increase profitability by reducing burnout, the fine-grained component is changed ayut through the bed at a rate
    6-12 m / s,> SM ϊ 258334
    类似技术:
    公开号 | 公开日 | 专利标题
    SU1258334A3|1986-09-15|Method of chemical treatment of fuel in pseudoliquefied layer
    EP0676464B1|2001-10-24|Method of and apparatus for fluidized-bed gasification and melt combustion
    US4444568A|1984-04-24|Method of producing fuel gas and process heat fron carbonaceous materials
    US4165717A|1979-08-28|Process for burning carbonaceous materials
    US5855631A|1999-01-05|Catalytic gasification process and system
    US4854249A|1989-08-08|Two stage combustion
    EP0384454B1|1992-09-23|Apparatus for gasifying or combusting solid carbonaceous material
    US4539188A|1985-09-03|Process of afterburning and purifying process exhaust gases
    CA1057584A|1979-07-03|Process for burning carbonaceous material
    US4684375A|1987-08-04|Method for gasifying a material using a circulating fluidized bed
    US4154581A|1979-05-15|Two-zone fluid bed combustion or gasification process
    US5641327A|1997-06-24|Catalytic gasification process and system for producing medium grade BTU gas
    US4111158A|1978-09-05|Method of and apparatus for carrying out an exothermic process
    EP0027280B1|1983-11-23|Process and apparatus for the conversion of agglomerating hydrocarbonaceous solid material to a more valuable gaseous product
    US5665319A|1997-09-09|Method of separating carbon dioxide from carbon dioxide containing gas and combustion apparatus having function to separate carbon dioxide from the combustion gas
    US4442080A|1984-04-10|Fluid bed SOX/NOX process--"hydrated calcine absorption"
    EA010277B1|2008-08-29|Method and plant for producing low-temperature coke
    US4648331A|1987-03-10|Process for the reduction of NOx in fluidized-bed furnaces
    CN1045127A|1990-09-05|The improvement of pre-reduced iron oxide
    US5379705A|1995-01-10|Fluidized-bed incinerator
    US4389381A|1983-06-21|Limestone calcination
    US4597774A|1986-07-01|Method for improving the operation of a fluidized bed
    US3847566A|1974-11-12|Fluidized bed gasification process with reduction of fines entrainment by utilizing a separate transfer line burner stage
    CS253732B2|1987-12-17|Process for directed reduction of materials containing iron oxide
    US3852216A|1974-12-03|Process for producing coarse particles of active carbon in a fluidized bed with added inert particles
    同族专利:
    公开号 | 公开日
    DE2646860A1|1977-05-05|
    AU1869076A|1978-04-20|
    GB1523500A|1978-09-06|
    AU507091B2|1980-01-31|
    JPS5257085A|1977-05-11|
    HU176745B|1981-05-28|
    PL117560B1|1981-08-31|
    JPS6021769B2|1985-05-29|
    BE847471A|1977-02-14|
    FR2328507B1|1981-06-12|
    IT1123615B|1986-04-30|
    CA1069276A|1980-01-08|
    FR2328507A1|1977-05-20|
    US4084545A|1978-04-18|
    DE2646860C2|1993-02-11|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    RU2529300C2|2009-07-16|2014-09-27|Ифп Энержи Нувелль|Method and plant to burn in loop reactor with independent control of solid substances circulation|US2665200A|1948-07-01|1954-01-05|Hydrocarbon Research Inc|Process for the gasification of solid carbonaceous materials|
    US2654665A|1950-02-21|1953-10-06|Consolidation Coal Co|Gasification of carbonaceous solids|
    US2638684A|1950-04-07|1953-05-19|Dorr Co|Process for heat-treating combustible solids|
    NL91935C|1951-05-23|
    US2774661A|1951-08-07|1956-12-18|Dorr Co|Method of heat-treating fines in a coarse solids fluidized bed|
    US2741549A|1952-11-01|1956-04-10|Exxon Research Engineering Co|Conversion of carbonaceous solids into volatile products|
    US3066017A|1953-07-28|1962-11-27|Exxon Research Engineering Co|Control of flow of particulate solids|
    US3508506A|1968-06-13|1970-04-28|Us Interior|Process and apparatus for reduction of unburned combustible in fly ash|
    US3645237A|1970-06-10|1972-02-29|American Standard Inc|Water heater having fluidized bed combustion and heat exchange region|
    US3807090A|1970-12-02|1974-04-30|Exxon Research Engineering Co|Purifications of fuels|
    US3784676A|1971-04-30|1974-01-08|Exxon Research Engineering Co|Removing sulphur from hydrocarbons|
    US3840354A|1972-03-23|1974-10-08|Us Interior|Three-stage gasification of coal|
    US3823676A|1972-10-10|1974-07-16|Warren Cook Chem Inc|Method of reducing sulphur dioxide emissions from coal|
    US3763830A|1973-01-24|1973-10-09|Us Interior|Apparatus for burning sulfur containing fuels|JPS5817366B2|1977-07-20|1983-04-06|Hitachi Shipbuilding Eng Co|
    US4154581A|1978-01-12|1979-05-15|Battelle Development Corporation|Two-zone fluid bed combustion or gasification process|
    US4177741A|1978-06-19|1979-12-11|Foster Wheeler Energy Corporation|System and method for improving the reaction efficiency of a fluidized bed|
    US4191115A|1978-06-23|1980-03-04|The United States Of America As Represented By The United States Department Of Energy|Carbonaceous fuel combustion with improved desulfurization|
    ZA801294B|1979-03-14|1981-10-28|British Petroleum Co|Fluidised bed combustor|
    US4704084A|1979-12-26|1987-11-03|Battelle Development Corporation|NOX reduction in multisolid fluidized bed combustors|
    US4312301A|1980-01-18|1982-01-26|Battelle Development Corporation|Controlling steam temperature to turbines|
    US4303469A|1980-04-14|1981-12-01|International Paper Company|Process and apparatus for recovery of spent pulping liquors|
    US4389381A|1980-09-19|1983-06-21|Battelle Development Corporation|Limestone calcination|
    US4357907A|1980-10-27|1982-11-09|Rockwell International Corporation|Fluidized bed combustor with improved indirect heat exchanger units|
    JPS57136005A|1981-02-18|1982-08-21|Babcock Hitachi Kk|Fluidized bed boiler capable of recovering heat held of discharged medium|
    US4388877A|1981-07-07|1983-06-21|Benmol Corporation|Method and composition for combustion of fossil fuels in fluidized bed|
    US4483259A|1981-07-07|1984-11-20|Benmol Corporation|Method and composition for removal of gaseous contaminants produced in combustion of fossil fuels or present in reducing gases|
    US4355601A|1981-09-25|1982-10-26|Conoco Inc.|Recirculating flue gas fluidized bed heater|
    CA1184743A|1981-10-09|1985-04-02|Herbert A. Arbib|Superjet gas agitation process|
    US4419965A|1981-11-16|1983-12-13|Foster Wheeler Energy Corporation|Fluidized reinjection of carryover in a fluidized bed combustor|
    US4539939A|1981-12-15|1985-09-10|Johnson William B|Fluidized bed combustion apparatus and method|
    CA1225292A|1982-03-15|1987-08-11|Lars A. Stromberg|Fast fluidized bed boiler and a method of controlling such a boiler|
    US4441959A|1982-07-21|1984-04-10|International Paper Company|Recovery of heat and chemical values from spent pulping liquors|
    FR2537701B1|1982-12-08|1985-03-08|Creusot Loire|
    GB2132500B|1982-12-17|1986-06-04|Coal Ind|Classification and recycling of fluidised bed material|
    US4453497A|1982-12-21|1984-06-12|Struthers Wells Corporation|Augmented heat transfer method and apparatus|
    US4530207A|1983-05-05|1985-07-23|Asea-Stal Ab|Power plant with a fluidized bed combustion chamber|
    US4572086A|1983-10-27|1986-02-25|Convenient Energy, Inc.|Fine fuel delivery system with remote drying and on site storage|
    JPH0513698B2|1984-02-27|1993-02-23|Denryoku Chuo Kenkyujo|
    US4589927A|1984-05-29|1986-05-20|Battelle Development Corporation|Liquid multisolid fluidized bed processing|
    US4676733A|1984-09-24|1987-06-30|Ohio State University|Method for producing a clean heated fluid|
    US4671251A|1984-09-24|1987-06-09|Ohio State University|Fluidized bed combustor|
    US4579070A|1985-03-01|1986-04-01|The M. W. Kellogg Company|Reducing mode circulating fluid bed combustion|
    DK158531C|1985-06-13|1990-10-29|Aalborg Vaerft As|PROCEDURE FOR CONTINUOUS OPERATION OF A CIRCULATING FLUIDIZED BED REACTOR AND REACTOR TO USE IN EXERCISE OF THE PROCEDURE|
    FR2587090B1|1985-09-09|1987-12-04|Framatome Sa|CIRCULATING FLUIDIZED BED BOILER|
    FI853615L|1985-09-20|1987-03-21|Tampella Oy Ab|FOERFARANDE FOER MINSKNING AV UTSLAEPPEN AV KVAEVE- OCH SVAVELOXIDER VID FOERBRAENNING AV KVAEVE- OCH SVAVELHALTIGT BRAENSLE.|
    US4665864A|1986-07-14|1987-05-19|Foster Wheeler Energy Corporation|Steam generator and method of operating a steam generator utilizing separate fluid and combined gas flow circuits|
    US4709662A|1987-01-20|1987-12-01|Riley Stoker Corporation|Fluidized bed heat generator and method of operation|
    JPS63121212U|1987-02-02|1988-08-05|
    US4776288A|1987-07-31|1988-10-11|Metallgesellschaft Aktiengesellschaft|Method for improving solids distribution in a circulating fluidized bed system|
    JPS6475808A|1987-09-14|1989-03-22|Sanki Eng Co Ltd|Temperature distribution uniformizing method for fluidized bed type incinerator|
    US5239945A|1991-11-13|1993-08-31|Tampella Power Corporation|Apparatus to reduce or eliminate combustor perimeter wall erosion in fluidized bed boilers or reactors|
    US5325796A|1992-05-22|1994-07-05|Foster Wheeler Energy Corporation|Process for decreasing N2 O emissions from a fluidized bed reactor|
    JPH07301799A|1994-05-10|1995-11-14|Seikosha Co Ltd|El for back light of liquid crystal|
    US5795548A|1996-03-08|1998-08-18|Mcdermott Technology, Inc.|Flue gas desulfurization method and apparatus|
    CN1262791C|1998-06-16|2006-07-05|三菱重工业株式会社|Fluidized-bed incinerator and operating method thereof|
    US6276287B1|1999-05-03|2001-08-21|Toda Kogyo Corporation|Iron compound catalyst for inhibiting generation of dioxin and incineration process of municipal solid waste using the same|
    US6615750B2|2002-02-11|2003-09-09|AlstomLtd|Sorbent conditioning and direct feed apparatus for a steam generator and a method for retrofitting a steam generator with same|
    CN100436941C|2005-07-05|2008-11-26|中国石油大学|Coal-tar powder combustion method and apparatus|
    US20090031967A1|2007-07-31|2009-02-05|Alstom Technology Ltd|Integral waterwall external heat exchangers|
    US8105541B2|2008-10-13|2012-01-31|Pratt & Whitney Rocketdyne, Inc.|Reactor system and method therefore|
    FI123853B|2009-03-06|2013-11-15|Metso Power Oy|A method for reducing nitrogen oxide emissions from oxygen combustion|
    US9638418B2|2009-05-19|2017-05-02|General Electric Technology Gmbh|Oxygen fired steam generator|
    JP5417068B2|2009-07-14|2014-02-12|株式会社日立製作所|Oxyfuel boiler and control method for oxygen fired boiler|
    US9617087B2|2010-10-28|2017-04-11|General Electric Technology Gmbh|Control valve and control valve system for controlling solids flow, methods of manufacture thereof and articles comprising the same|
    US9557115B2|2010-10-28|2017-01-31|General Electric Technology Gmbh|Orifice plate for controlling solids flow, methods of use thereof and articles comprising the same|
    US8920737B2|2012-07-27|2014-12-30|General Electric Company|System for catalytic reaction|
    EP3186554B1|2014-07-04|2019-09-18|Tubitak|Method for operating a circulating fluidized bed gasification or combustion system|
    DE102015107435A1|2015-05-12|2016-11-17|OutotecOy|Process for the partial roasting of copper- and / or gold-containing concentrates|
    CN104910986B|2015-06-19|2017-01-04|合肥德博生物能源科技有限公司|A kind of biomass double fluidized-bed vaporizing system gas plant and technique|
    CN109073213B|2016-03-24|2020-11-24|由加拿大自然资源部长代表的加拿大女王陛下|System and method for oxygen carrier assisted oxygen combustion fluidized bed combustion|
    CN111174198B|2020-01-13|2020-12-22|浙江大学|Coupled jacketed carbon separator chemical-looping combustion/gasification device with two juxtaposed fluidized beds|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US62454275A| true| 1975-10-21|1975-10-21|
    [返回顶部]