• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
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  • 引用文献
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    • 专利摘要:
    1500185 Processing coal for the production of power L & C STEINMULLER GmbH and K KNIZIA 7 Jan 1975 [8 Jan 1974] 685/75 Heading C5E A plant for the processing of coal to give low sulphur products which can be used for the generation of electric power and gas comprises: (a) a heat generating station for supplying the necessary heat for coal processing, comprising a fuel fired steam generator; (b) a coal preparation station comprising a size reducing unit and a preoxidation unit; (c) a coal processing station comprising a gasification unit and a gas coke separator unit; (d) means for conveying the coke from the separator to the combustion chamber of the steam generator or to a synthesis gas producer; (e) a station for the desulphurization of the gas from the processing station comprising a gas purifier, an H 2 S scrubber, and a sulphur recovery unit; (f) heat exchange means for recovering heat from the gas from the processing station before it is purified; and (g) means for conveying the sulphur free gas to the steam generator and other gas consuming devices. The gasification unit may be heated by a carrier gas heated in the heat generating station. A gas turbine installation may be provided before the steam generator for the production of power from the sulphur free gas. Waste heat from high temperature reactors may be used for the coal treatment, gasification, and coking. The gasification step may be a steam devolatilization.
    公开号:SU1058509A3
    申请号:SU752094996
    申请日:1975-01-08
    公开日:1983-11-30
    发明作者:Шустер Эрнст；Книциа Клаус
    申请人:Л.Унд К.Штайнмюллер,Гмбх (Фирма)；Д-Р.-Инж.Клаус Книциа (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to a plant for the processing of coal and the production of solid and gaseous products from it for the production of electricity and gas. A known plant for processing coal and producing electricity and gas, comprising a device for grinding coal, a device for coal gasification to produce coke and gas, a steam generator with a coke burning furnace, a steam turbine and a device for cleaning the produced gas 1. A disadvantage of the known installation is unstable operation as a result of uneven electricity consumption, inconsistent with production. In addition, the plant capacity is limited and must be consistent with the performance of the steam generator. The insufficient efficiency of the installation, in advantage, is due to the fact that it is necessary to expend fuel to heat the air entering the boiler of the steam boiler. The purpose of the invention is to ensure stable operation, increase productivity and overall efficiency of the charts. This goal is achieved by the installation containing the coal grinder, a device for coal gasification to produce coke and gas, a steam generator with a furnace for burning coke, a steam turbine and a Bin device. purification of the produced gas, additionally contains a device for CLEANING the produced gas from sulfur compounds and a gas turbine unit connected inlet through a gas distributor to the gas network and / or outlet to the steam generator furnace. The proposed unit works stably in case of uneven electricity consumption due to the redistribution of gas that can be supplied to the gas network either to the gas turbine or to the steam generator of the torus. In the event of a gas turbine shutdown, gas can be supplied to the furnace of a steam boiler. The efficiency of the plant is increased by the fact that the gases leaving the combustion chamber of the gas turbine have a temperature of approximately 420 ° C and a high oxygen content. These gases are supplied as oxygen-containing gas to the combustion chamber of the steam generator coke and the heat content of the flue gases is used for vaporization, which increases the efficiency of the installation from 37 to 45%. The diagram shows the proposed installation. The installation includes a coal bin 1, a dust separation device 2, a mill 3, a coal oxidation reactor 4, a steam separator 5, coal gasification chambers 6, a blower machine 7, a heater 8, connected by pipeline 9 to the oxidation reactor 4 - coal, which is connected to the separator 10 for separating the coal dust from the air Chamber 11 of the combustion of the steam generator is connected by pipe 12 to the separator 10. In the chamber b for gasification of fuel, a pipe 13 is connected to supply gas through the compressor 14 and the air heater 15. To A gasification unit is connected to a separator 16 for separating gas and coke, an intermediate bunker 17 with a pneumatic system 18, to which gas is supplied after the electrostatic precipitator 19 through a compressor 20 and a pipeline 21. A separator 22, a resin exchanger 23, a resin separator and a dust separator 23 are connected to the separator 16 removal of tar and residual coke, heat exchanger-heat exchanger 25, compressor 26, device 27 for purifying gas from hydrogen sulphide, Claus unit 28 and unit 29 for sulfur granulation with sulfur hopper 30. A device 31 for separating hydrocarbons is connected to a device 27 for purifying gas from hydrogen sulphide and through a distributor 32 to a combustion chamber 33 of a gas turbine 34. An air compressor 35 is connected to a combustion chamber 33. Gas 34 by pipe 36 is connected to a steam generator burner 11. The electrostatic precipitator 19 is connected by conduit 37 to a combustion chamber 11, from which ash is discharged into the hopper 38. The device operates as follows. The coal coming from the mine or mine is loaded into the bunker 1 and fed through the dust separator 2 to the mill 3. In contrast to the known installations, the coal dust is not carried into the air from the mills, which, due to the possibility of ignition, limits the temperature of the air mixture. coal dust to about 130 ° C, and smoke that is taken from the steam generator of the power plant on coal fuel and, if necessary, undergoes instantaneous oxidation in the reactor 4. This one contains a small amount of oxygen and carries it thus nature inert gas. The moisture contained in the coal is evaporated by the smoke and removed from the process together with the inert gas in the steam separator 5.
    Coal dust is fed to a fuel processing facility, which consists mainly of a fast oxidation reactor 4 and a gasification chamber 6.
    After the coal dust mixture passes through the steam separator 5, the coal dust enters the reactor 4 for rapid oxidation. Here, to the coal, dust is supplied through the blower machine 7 air heated. In the air heater 8 by the steam generator of the power plant, through line 9. The air heater 8 can also be located outside the steam generator and / or loaded by other heat carriers as gas from the boilers. After pre-oxidation, the coal dust mixture is separated from the air in the separator 10. This air is fed through pipe 12 into the combustion chamber 11 of the steam generator. Since the coal dust it introduces burns in the combustion chamber to produce electricity, i.e. this is not lost, the efficiency of the separator 10 is not significant. The separated carbon is then supplied to the chamber or gasification chambers 6. This is where the h: asthmatic gassing of fuel. At this point, water vapor can be blown into the coal mixture, if necessary, will increase the gas flow,. part of the carbon must be additionally gasified. This water vapor could be taken from the reactor at high temperatures. At this point, when indirectly heated, one could however take heat gels from the high-temperature reactor for the fuel reprocessing process. The diagram shows the supply of heat for processing fuel using gas that is supplied through compressor 14 and the heater 15 to the steam generator of a coal-fired power station, and through pipe 13 a portion of the heat supplied to the gasification chamber 6 (or chambers). The heater 15 can be is located outside the steam generator and / or loaded by other heat carriers as gas from the boilers. In coke and gas separator 16, the resulting gas is separated from coke dust. Coke dust through the intermediate hopper 17 is supplied by means of a pneumatic system 18 to ignite a steam generator. An inert gas such as smoke can be used as a carrier. This gas is taken up behind the electrostatic precipitator 19 and through the compressor 20 and the pipe 21 is supplied to the pneumatic system 18. The quality of separation in the separator 16 is sufficient to load the resin and dust separator 23. The gas gives off its heat to
    heat exchangers 22 and. 25, for example, a steam power plant and coal-fired power plants. Smolite separation, meanwhile, occurs in a favorable temperature range. Through pipe 24, the separated resin and residual coke are also fed to the combustion chamber 11 and the steam generator. The purified and cooled gas is supplied through gas compressor 26 to device 27 for purifying gas from hydrogen sulphide. Here, hydrogen sulphide is discharged from the gas and supplied to the Claus 28 unit, the 29 unit to collect sulfur from sulfur, and finally to the sulfur bunker 30. J structure 15 separates the upper hydrocarbons so that gas is available, which through the distributor 32 can be recovered as synthesis gas or as methane, or for further conversion using water vapor and heat from the reactor temperatures. Since at a certain power of coal-fired power plants, for example, 690 MW and the corresponding power of the gas turbine process, for example, 110 MW, depending on the grade used
    0 coal, more gas is produced, then this gas, if it is not brought out, can be used either in another open gas turbine process, whose heat is used for heating plant, or supplied to a steam generator for combustion. In an additional gas turbine plant, which consists of an air compressor 35 of the gas turbine combustion chamber 33 and gas turbine 34, part of the gas is combusted. Since, depending on the allowable inlet temperature of the gas turbine, this combustion must occur with a high excess of air , the output gas from the gas turbine flows with temperature and excess residual air into the steam generator combustion chamber 11 via pipeline 37. Flying ash, which is separated
    0 in the electrostatic precipitator 19 of the steam generator through conduit 37, is again supplied to the steam generator and melts in this chamber and then — as is customary at the present time — precipitates
    5 in granular form. Granular coal granular ash with granular sulfur can enter the mining enterprise through the hopper 38.
    For desulfurization, it is not necessary to convert all the fuel into gaseous form, since the sulfur in the coal, when degassing, passes predominantly into the produced gas and it is only necessary to desulfurize
    5 this gas. Coal gasification could
    to occur only with the use of coal, since otherwise it would have resulted in high costs for obtaining oxygen, which is uneconomical. Along with hydrogen, hydrocarbons and carbon monoxide it. would lead to a high nitrogen content. and not only to a low-calorific gas storage, but would require an expensive installation to provide gas. In the proposed plant, only hydrogen / hydrocarbons, a small amount of carbon monoxide and sulfur combined with hydrogen are obtained from coal.
    It is not necessary to impose special requirements on coal, for example, insignificant sintering, a certain content of volatile components, etc. You can use any coal or lignite.
    Depending on the separation of the entrapment device and the gasification device, the partially high-calorific gas can be used for the gas turbine process preceding the steam-power process, as a result of which the advantages of the combined steam-power and gas turbine lead to a higher efficiency than that of conventional coal-powered turbines and, moreover, reduce investment expenses.
    The resulting gas can be used as an industrial gas, such as synthesis gas, for the chemical industry or for the reduction of ore, it can be used in part as well as high-calorific gas for general provision.
    The solid product (coke dust) arising during the processing combines in this form all the ash brought in by the coal, which can be separated by burning coal dust in the combustion chamber of the steam generator, filled as a smelting chamber.
    The steam turbine power station, apart from gas recovery, desulfurization and gas turbine, can operate as a conventional power plant. The utilization rates of all series-connected installations thereby reduce installation costs for producing current. This gives a significant advantage in comparison with the known installation, which is especially noticeable when using high-temperature reagents.
    Processes for gas and desulfurization must be separated from the owner of the power plant so that a coal-fired power station can be built earlier taking into account the use of the plant.
    to produce gas and desulfurization and work for the first time on depleted gray coal.
    The gas turbine and steam power processes should also be separated 5 from one another. For the case of the gas turbine off state, as well as for the case of an undesirable return of the produced gas as an industrial gas or for public purposes, this gas can be supplied to the steam generator for combustion and thereby to produce current. The advantage of carbon exchanging is valid.
    5 The sulfur combined with hydrogen can be converted to elemental sulfur, for example, in molten, granulated, or unit form, and together with granulated coal slag from the steam generator can be returned to the mining enterprise.
    The proposed facility also allows heat to be separated from high temperature reactors for enrichment and reprocessing processes. The proposed connection of high-temperature reactors with coal-fired power plants provides a solution to the problem of producing gas using nuclear energy, while simultaneously solving the problem of removing ash, desulfurizing and generating electrical energy with high economic efficiency.
    5 The proposed installation is also separated from the high-temperature reactor with the possibility of operation, i.e. several coal-fired power plants can be developed, combined into one unit, with enrichment and processing of fuel into fuel with a combined sulfur content, and the need for heat covered by the steam generator smoke,
    5, to enrich and process the fuel, it is then coated with one or more: and high temperature reactors.
    Fuel enrichment as well
    Q processing of the source energy carrier (coal into a gaseous product) makes it possible to economically transport this energy carrier in the field of useless minerals. for recycling there in electric
     energy or for other uses.
    In the proposed installation due to the processing of coal into various gaseous and solid products in
    At any time, matching of the current consumption and gas can occur.
    Fossil fuels serve as energy storage and can
    5 result — power increase in
    the site of enrichment and processing will briefly cover the maximum need for leaking without the need to accumulate it.
    Common in the present technology, according to which coal in steam turbine power plants is converted into electrical energy, leads together with coal costs to high costs for generating electrical energy that cannot compete with nuclear energy. It should be added that, at present, the method of smoke desulfurization has not been sufficiently tested, so that it could not satisfy the environmental protection requirements in terms of suppressing 5O: emissions. The desulfurization process, moreover, is more than 20% higher than the cost of generating electrical energy. Owing to the growing decrease in liquid and gaseous carriers, energy is becoming more and more important for the production of gas in electricity, energy is given to solid minerals4. This requires an installation that, with low investment costs, allows for the production of gas and electricity with a relatively high efficiency and, moreover, does not require significant costs for
    fuel desulfurization (as was the case when smoke was desulfurized).
    Since the proposed plant is for an improved process of producing electricity from coal while simultaneously desulfurizing and is associated with
    By removing gas and, if necessary, gasifying the fuel, it is possible to use not only pierced gas, {thus obtained, or gas (for general use, but also other gasification products, such as benzene. The need to produce large quantities of industrial gas or gas). general provision causes the generation of heat from high-temperature reactors to enrich and process fuel and improve the efficiency of the whole process due to the cheaper heat from the reactors in High temperatures.
    The use of the produced coke as a fuel in the steam generator reduces the C / I ratio of the produced gas in an amount comparable to the use of oil.
    In addition, it is possible to gasify a part of the produced coke dust with water vapor by partially burning them or supplying heat outside, for example, heat from nuclear energy.
    权利要求:
    Claims (1)
    [1]
    PLANT FOR COAL PROCESSING AND ELECTRIC POWER PRODUCTION
    A GAS containing a device for crushing coal, a device for gas-ia fication of coal to produce coke and gas, a steam generator with a furnace for burning coke, a steam turbine and a device for purifying the obtained gas, characterized in that, in order to ensure stable operation, increase productivity and the overall efficiency of the installation, it additionally contains a device for cleaning the obtained gas from sulfur compounds and a gas turbine installation connected at the inlet through a gas distributor to the gas network and / or to the torus.
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    同族专利:
    公开号 | 公开日
    AU7717075A|1976-07-08|
    FR2256954B1|1980-03-07|
    JPS6150995B2|1986-11-06|
    ZA75124B|1976-01-28|
    JPS50116502A|1975-09-11|
    DE2400772C3|1978-03-02|
    GB1500185A|1978-02-08|
    DE2400772B2|1977-07-14|
    FR2256954A1|1975-08-01|
    DE2400772A1|1975-09-25|
    引用文献:
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    DE2659751A1|1976-12-31|1978-07-13|Steinmueller Gmbh L & C|METHOD FOR GENERATING ELECTRICAL ENERGY AND GAS FROM COAL PUMPED BAKING COAL|
    DE2659752C3|1976-12-31|1981-04-23|L. & C. Steinmüller GmbH, 5270 Gummersbach|Process for the desulphurisation of coal which has been crushed to less than 0.1 mm|
    JPS5565296A|1978-11-06|1980-05-16|Texaco Development Corp|Production of hydrogen and carbon monoxide contained gas flow|
    DE3525676C2|1985-07-18|1991-05-08|Siemens Ag, 1000 Berlin Und 8000 Muenchen, De|
    AT49627T|1985-09-02|1990-02-15|Siemens Ag|COMBINED GAS AND STEAM TURBINE POWER PLANT.|
    CH668290A5|1987-09-02|1988-12-15|Sulzer Ag|Combined gas turbine steam plant - has overheating device for saturated steam coupled to steam generator|
    DE3921439A1|1989-06-27|1991-01-03|Siemens Ag|COMBINED GAS-STEAM TURBINE PROCESS WITH COAL GASIFICATION|
    US8951314B2|2007-10-26|2015-02-10|General Electric Company|Fuel feed system for a gasifier|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE2400772A|DE2400772C3|1974-01-08|1974-01-08|
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