• 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:
    A moisture-containing viscous secondary fuel is combusted in the chamber of an industrial furnace by comminuting the secondary fuel to a particle size of 5-50 mm and propelling the particles at an initial speed of 1-10 m/sec. onto a layer of intensely burning primary fuel, such as solid refuse, coal or wood. The particles are propelled from a level at 0.5-2 m above the burning layer and in such a way that the length of their flight spans is 0.2-2 m. This insures that the particles retain moisture during travel in the combustion chamber and do not agglomerate prior and/or subsequent to contacting the burning layer of primary fuel. The rate of admission of comminuted secondary fuel is regulated in dependency on changes of temperature in the chamber, in dependency on changes of the CO2 or O2 content of combustion products and/or in dependency on variations of a parameter (e.g., length) of the burning layer of primary fuel.
    公开号:SU936828A3
    申请号:SU772488992
    申请日:1977-06-03
    公开日:1982-06-15
    发明作者:Иозеф Мартин Иоханнес；Иозеф Мартин Вальтер；Каммхольц Хорст
    申请人:Иозеф Мартин Фойерунгсбау Гмбх (Фирма)；
    IPC主号:
    专利说明:

    (5) METHOD FOR C-PLASTING SECONDARY FLAMMABLE SUBSTITUTE WITH MAIN FLAMMABLE SUBSTANCE
    one
    The invention relates to a method of burning a secondary combustible substance in the form of untreated or dehydrated isham with the main combustible substance — debris in incinerating 5 kilns and installations.
    There is a known method of incineration of waste, which includes the supply of waste to the hot gas stream, its drying and burning on the hot debris layer D 3.
    The disadvantage of this method is the presence of chemical and mechanical underburning due to the fact that small particles of sludge are dried and captured by the gas flow without treatment, and large particles get into the sludge. a partially burned-out layer on the grate, coking and being discharged with slag.
    The closest to the proposed technical essence and the achieved effect is a method of burning a secondary combustible substance with the main, including grinding
    secondary combustible substance, its measured dosage and distribution on the main substance, while the basic substance is in a hot state 2.
    The main substance is granules, which are preheated.
    The disadvantage of this method is the supply of secondary combustible material to hot g | a core of an anerated layer, with which the secondary substance slowly rolls into the firing space and at the same time dries, as a result, to ensure complete combustion, fine grinding of the secondary material is required, which requires an increase in grinding costs.
    The purpose of the invention is to ensure complete combustion.
    The goal is achieved by those. According to the method of burning a secondary combustible substance with the main fuel, a substance including grinding the second combustible substance, its metered supply and distribution on the main substance layer, the secondary combustible substance is supplied directly but to the main one without preliminary drying, while the main substance is supported in a state of intense combustion. The flight time of the crushed particles of the secondary combustible material is 0.1-0.5 s. The feed rate of the secondary fuel is 1–10 m / s. The secondary combustible material is crushed and quickly without pre-drying (to preserve its moisture content / is distributed directly on the main substance, which is in a state of intense burning. During the time of flight, particles of the secondary substance can only have an outer crust, which prevents combustion. The secondary substance must reach its main state in an unchanged state. Due to the distribution of the secondary substance on the main, immediately after its distribution it reaches with complete The secondary substance can not be sintered because it gets onto the burning layer and contains moisture in each particle due to direct contact with the main burning substance, convection and radiation evaporates like a flame, which leads to an increase in the surface intensifies the combustion and excludes soot formation. The coating of the main substance is prevented by a layer of the secondary and a good aggravation of the secondary substance is achieved due to the intense burning of the main substance, and the fraction of trapped dust due to the exclusion of preliminary drying is significantly reduced. Fine grinding of the secondary substance is not required, since the reduction is achieved with an explosive rupture of a particle that has fallen on the intensely burning main substance. In order to obtain the least possible effect of the hot flue gas on the secondary substance, it is necessary to choose the acceleration of the particles so that the duration of their flight inside the furnace space before they hit the main substance is no more than 1 s, preferably 0.1 - 0.5 s. In order to achieve such a residence time, the input velocity of the particles of the secondary substance must be maintained in the range of 1-10 m / s, while the grinding of the initial secondary substance is carried out to a particle size of 5-50 mm. The amount of the secondary substance fed is controlled depending on the temperature in the combustion space and the CO or O content in the exhaust gases. FIG. 1 shows a device in which a method of burning a secondary combustible substance with a main, longitudinal section of the furnace space is carried out; in fig. 2 is a cross section A-A in FIG. one; in FIG. 3 a combustion space with two inputs of the secondary substance, an option; in fig. 4 and 5 - the path of flight of particles of the secondary substance, depending on the speed and time of flight. The device comprises a loading device 1, a grate 2, on which a layer 3 of the main combustible substance is located. The opening C for supplying the secondary substance is made in the wall of the furnace space 5. The device for supplying the secondary substance consists of a tray 6, a grinding mechanism 7 and a distributor 8. Particles 9 of a secondary combustible substance are distributed on the wasp layer; The main substance 3. To protect the grinding mechanisms, mechanical gate valves 10, or pipelines 11 are provided for padding the locking medium in the form of gas or steam. Burnt residues are discharged from the firebox through an outlet 12. The method is carried out as follows. The main substance (debris, waste or other combustible substances is transferred by the charging device 1 and gets onto the grate 2, on which it is ignited and burns in the third layer of foaming fuel. Through the hole in the side wall of the furnace space 5 secondary fuel is introduced into the paste-like form which, through the tray 6, enters the grinding mechanism 7 and, through the distributor 8, is thrown into the furnace in the form of particles 9 Separate particles 9 of the secondary combustible substance fall into direct contact a heated mass, thereby preventing the sintering of particles still able to flow.The explosive evaporation of the secondary fuel in the water particles is further crushed and ignited from the burning base substance layer 3. Together with the burned layer, the fully combusted: the secondary substance moves through the neck 3. to the outlet 1 2. An opening j, through which the secondary combustible substance is supplied, depending on the specific features it has, can be provided in various places to reach, possibly It is possible to have shorter particles in the furnace space before they fall on the main layer. The openings may be somewhat in the furnace to evenly distribute the secondary hot substance.
    The implementation of the method is not associated with a specific type of furnaces, but STV devices for supplying secondary combustible material can be used in fluidized bed furnaces, in grateless furnaces, etc., if the secondary substance is allowed to penetrate the main substance without pre-drying.
    FIG. 4 and 5 show the flight paths of the particles of the secondary substance with different initial velocities of 1 m / s, 2 m / s, 3 m / s and 5 m / s at different angles of the beam. to horizontal. When calculating individual curves, time intervals equal to 0.1 s were selected.
    Thus, with the usual width of the grate and correspondingly low positioning of the device for giving over the grate, the length of stay is between 0.1 and 0, s. In this short period of time, there are no noticeable changes in particles with a diameter of 5-50 mm, and practically unchanged particles are placed on the cutting layer, which ensures complete combustion of them on the layer and reduces chemical and mechanical underburning.
    权利要求:
    Claims (3)
    [1]
    1. A method of burning a secondary combustible with the main combustible substance, including grinding the secondary combustible substance, metering it and distributing it on the main substance layer, characterized in that, in order to ensure complete combustion, the secondary combustible substance is fed directly to the main substance without pre-drying while the base material is maintained in a state of intense burning.
    [2]
    2. Method of pop, 1, characterized by the fact that the time of flight of the crushed particles of the secondary combustible material is 0.1 - 0.5 s.
    [3]
    3. Method pop; 1, differing from and in that the feed rate of the secondary combustible substance is 1-10 m / s
    Sources of information taken into account in the examination 1. Thermal methods of waste disposal. Ed. KN Bogushevskaya and G. P, Bespam tnova. L., (Himi, 1975.
    . 2. Japan patent number 48-39990, yl. 92/7 / CO, 1973 (prototype).
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    类似技术:
    公开号 | 公开日 | 专利标题
    SU936828A3|1982-06-15|Method for burning secondary fuel substance with primary fuel substance
    US4859177A|1989-08-22|Apparatus for incinerating combustible material
    JP2709193B2|1998-02-04|Process and apparatus for igniting a burner in an inert atmosphere
    US4279205A|1981-07-21|Storage
    US3680501A|1972-08-01|Incinerator
    US3333556A|1967-08-01|Method for the combustion of partially dewatered sewage sludge as well as improved furnace incorporating grate firing for carrying out the aforesaid method
    US3921543A|1975-11-25|Method of incinerating salt-containing liquid sludge
    CA2101318C|2003-09-16|Method of burning a particulate fuel and use of the method for burning sludge
    CA1051719A|1979-04-03|Method and apparatus for burning coal and refuse
    RU2090803C1|1997-09-20|Method of burning solid and liquid wastes and device for realization of this method
    KR880002397B1|1988-11-04|Fluidized bed combustion apparatus
    US4377117A|1983-03-22|Particulate waste wood firing system
    US4485747A|1984-12-04|Reducing pollutant emissions by fines removal
    FI60402C|1982-01-11|FOERFARANDE OCH ANORDNING FOER FRAMSTAELLNING AV KOKS ELLER AKTIVT KOL FRAON FUKTIG ORGANISK SUBSTANS
    US3332375A|1967-07-25|Refuse incinerator
    US578531A|1897-03-09|abell
    US3533365A|1970-10-13|Method and combined furnace for the simultaneous incineration of refuse or garbage and sewage sludge
    US4377115A|1983-03-22|Furnace for burning particulate wood waste material
    RU2015450C1|1994-06-30|Solid fuel burning device
    US4307702A|1981-12-29|Grating structure
    JPS5819385A|1983-02-04|Method and apparatus for recovering oil and gas from oil shale
    SU767456A1|1980-09-30|Apparatus for burning industrial wastes
    SU1089358A2|1984-04-30|Installation for incinerating waste
    Raghavan2022|Solid Fuel Systems
    SU964352A1|1982-10-07|Incinerator
    同族专利:
    公开号 | 公开日
    DK143817B|1981-10-12|
    DE2724228B2|1978-08-10|
    CA1066137A|1979-11-13|
    UA5931A1|1994-12-29|
    JPS6137526B2|1986-08-25|
    GB1544571A|1979-04-19|
    DE2724228A1|1977-12-15|
    AT373987B|1984-03-12|
    NL7706057A|1977-12-06|
    SE7706331L|1977-12-04|
    BE845481A|1976-12-16|
    FR2353796B1|1980-10-17|
    US4143603A|1979-03-13|
    JPS52148973A|1977-12-10|
    NL166115C|1981-06-15|
    IT1082369B|1985-05-21|
    CH622874A5|1981-04-30|
    DD132020A5|1978-08-16|
    DE2724228C3|1979-05-17|
    NL166115B|1981-01-15|
    BR7703611A|1978-04-18|
    SE433661B|1984-06-04|
    DK143817C|1982-03-29|
    FR2353796A1|1977-12-30|
    ATA406276A|1983-07-15|
    DK244177A|1977-12-04|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US2005082A|1931-06-17|1935-06-18|John E Greenawalt|Incinerator furnace|
    CH434539A|1964-08-20|1967-04-30|Von Roll Ag|Process for the joint incineration of waste and sewage sludge as well as an incinerator with grate firing for carrying out this process|
    US3322079A|1965-10-22|1967-05-30|Komline Sanderson Eng Corp|Sludge incineration|
    FR1473583A|1966-03-30|1967-03-17|Von Roll Ag|Method for burning waste fuels, in particular household refuse, as well as a combustion furnace for carrying out this method|
    US3769921A|1971-12-27|1973-11-06|Mullen F Mc|Waste materials processing system|
    GB1499405A|1975-04-07|1978-02-01|Imp Metal Ind Kynoch Ltd|Burning refuse and coal|US4326469A|1979-11-02|1982-04-27|Detroit Stoker Company|Multi-fuel feeder distributor|
    JPS6160323B2|1981-04-30|1986-12-20|Hitachi Shipbuilding Eng Co|
    FR2584480B1|1985-07-05|1989-11-17|Charbonnages De France|METHOD FOR REGULATING THE THERMAL POWER OF A HOUSEHOLD WASTE INCINERATOR AND INSTALLATION FOR CARRYING OUT SAID METHOD|
    JPS6374213A|1986-09-17|1988-04-04|Matsushita Electric Ind Co Ltd|Input device for apparatus|
    JPS63226618A|1986-11-29|1988-09-21|Furukawa Electric Co Ltd:The|Optical input keyboard system|
    JPH0337090B2|1987-06-30|1991-06-04|Takuma Kk|
    JPH0192713A|1987-10-03|1989-04-12|Furukawa Electric Co Ltd:The|Optical keyboard system|
    JPH0787913B2|1990-12-17|1995-09-27|株式会社オゼ|Sterilization water heater that doubles as an incinerator|
    US5271340A|1991-11-05|1993-12-21|Rineco Chemical Industries|Apparatus and methods for burning waste, and waste slurries|
    GR1001456B|1992-02-11|1993-12-30|Oze Kk|Combination sterilized hot-water and incineration system.|
    DE10060516A1|2000-12-06|2002-06-20|Mg Technologies Ag|Process for introducing granular ore into a roasting furnace|
    US6745706B2|2001-10-24|2004-06-08|Richard B. Pallett|Process and apparatus for disposing of municipal solid waste|
    CN104251496B|2013-12-25|2018-08-21|山东尧舜热能科技有限公司|A kind of coal slime incinerator|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    AT0406276A|AT373987B|1976-06-03|1976-06-03|METHOD AND DEVICE FOR BURNING A SECOND FUEL WITH A BASE FUEL IN BURNERS|
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