EP2092043A1 - Method for gasifying fuel and a gasifying generator - Google Patents

Method for gasifying fuel and a gasifying generator

Info

Publication number
EP2092043A1
EP2092043A1 EP07823244A EP07823244A EP2092043A1 EP 2092043 A1 EP2092043 A1 EP 2092043A1 EP 07823244 A EP07823244 A EP 07823244A EP 07823244 A EP07823244 A EP 07823244A EP 2092043 A1 EP2092043 A1 EP 2092043A1
Authority
EP
European Patent Office
Prior art keywords
oxidation
fuel channel
fuel
pipes
combustion
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.)
Granted
Application number
EP07823244A
Other languages
German (de)
French (fr)
Other versions
EP2092043A4 (en
EP2092043B1 (en
EP2092043B8 (en
Inventor
Leo Ruokamo
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.)
CCM-Power Oy
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to PL07823244T priority Critical patent/PL2092043T3/en
Publication of EP2092043A1 publication Critical patent/EP2092043A1/en
Publication of EP2092043A4 publication Critical patent/EP2092043A4/en
Publication of EP2092043B1 publication Critical patent/EP2092043B1/en
Application granted granted Critical
Publication of EP2092043B8 publication Critical patent/EP2092043B8/en
Not-in-force legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/58—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels combined with pre-distillation of the fuel
    • C10J3/60—Processes
    • C10J3/64—Processes with decomposition of the distillation products
    • C10J3/66—Processes with decomposition of the distillation products by introducing them into the gasification zone
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
    • C10B49/04—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated
    • C10B49/06—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated according to the moving bed type
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72—Other features
    • C10J3/723—Controlling or regulating the gasification process
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/16—Integration of gasification processes with another plant or parts within the plant
    • C10J2300/1625—Integration of gasification processes with another plant or parts within the plant with solids treatment
    • C10J2300/1637—Char combustion

Definitions

  • the invention relates to a method for gasifying fuel in the fuel channel of a gasifying generator, the fuel channel having a combustion area for fuel combustion and one or more oxidation pipes for supplying oxidation gas to the combustion area.
  • the invention also relates to a gasifying generator used in the method.
  • the fuel is generally supplied to the upper part of the gasifying generator, from which it flows by means of gravity through the pyrolysis, combustion and reduction areas.
  • the heat required for gasification is obtained by burning fuel, whereby a pyrolysis area is formed between the combustion area and the fuel, in which the volatile materials are separated from the fuel. These volatile materials form the product gas of the gasifying generator together with the gases generated in the reduction area.
  • the prior art gasifying generators are divided into cocurrent gasifiers and counter- current gasifiers according to the oxidation gas supply method.
  • cocurrent gasifi- ers the oxidation gas is fed directly to the combustion area.
  • countercurrent gasifiers the oxidation gas is conducted upwards from below, in the direction opposite to the fuel flow. In this method, the pyrolysis products end up in the product gas almost as such, i.e. the tars do not decompose.
  • An essential property of the product gas created in the gasifying generator with regard to its use is its purity.
  • tar generated in the gasification is a problematic ingredient of the product gas because of the emissions caused by it, limitations of use and the problems caused to the equipment.
  • Tar compounds decompose in temperatures exceeding 850°C.
  • Another essential impurity that arises in gasification is the nitrogen oxides that are generated in temperatures exceeding 1000 0 C. For these reasons, temperature control especially in the combustion zone after the pyrolysis phase is important in gasification.
  • Patent publication GB 456111 A describes a gasifying generator, in which oxidation gas is fed by oxidation pipes into the fuel channel.
  • the oxidation pipes are movable inside the fuel channel. This adjustment possibility has been made for enabling the adaptation of the gasifying generator for different fuels.
  • the location of the oxidation pipes is not changed during the combustion event.
  • An attempt is i made to control the combustion event by adjusting the amount of oxidation gas getting into the oxidation pipes.
  • the advantage achieved by the possibility of moving the pipes is that the oxidation pipes can be installed at different heights in the fuel channel. Adjusting the temperature of the combustion event is cumbersome with the method described in the specification.
  • oxidation pipes coming from above cause additional friction in the fuel flow, and the oxidation gas may form flow channels in the vicinity of the surface of the oxidation pipe.
  • the gasifying generator used in the method according to the invention there is a body, a fuel channel for fuel feed and the gasification processes, and one or more oxidation pipes for feeding the oxidation gas to the fuel channel.
  • the invention is characterized in that the oxidation gas discharge ends of the oxidation pipes are movable within the fuel channel in such a way that the point of oxidation can be moved in the gasification process.
  • the temperature of the combustion area is controlled by moving the oxidation pipes against the fuel stream or in the direction of the fuel stream.
  • the oxidation pipes can be moved either separately or in groups.
  • the number of oxidation pipes can be selected according to the size of the gasifying generator and the desired control accuracy of the combustion process.
  • Each oxidation pipe can have its own combustion area, but they have a common fuel feed and lower combustion area.
  • the fuel channel of the gasifying generator can have a narrowing or other structural solution, which restrains the free flow of the fuel.
  • the combustion area is generally located at this narrowing.
  • the temperature of the combustion area is measured by a thermometer.
  • the thermometer is preferably connected to the first actuator, which controls the oxidation pipes and especially their oxidation gas dis- charge ends within the fuel channel.
  • the first actuator adjusts the location of the oxidation pipes on the basis of readings obtained from the thermometer according to predetermined instructions.
  • This first actuator may be computer-controllable, automated in some other way or manually controllable. In the method, the temperature is given a desired set value, which is given to the first actuator or some device controlling it.
  • the first actuator moves the oxidation gas discharge end of the oxidation pipes in the direction of the pyrolysis area, whereby the combustion area receives less oxidation gas, combustion slows down in the combustion area, and the temperature thus falls.
  • the oxidation gas discharge end of the oxidation pipes is moved towards the combustion process, whereby the combustion in the combustion area accelerates and the temperature rises. It has been found experimentally that the best results with regard to the gasification processes and the product gas are obtained when a temperature exceeding 850 0 C is chosen as the set value of the temperature.
  • the cross-sectional area of the fuel channel can be changed by one or more movable adjuster(s) for adjusting the fuel flow and for determining the size of the combustion area.
  • These adjusters are in compliance with the prior art as such.
  • One possible way of implementing the adjusters is to place in the fuel channel two heat-resistant plates perpendicular to the main axis of the fuel channel, which move towards each other from the opposite sides of the fuel channel and thus reduce the cross-sectional area of the narrowing. In order to increase the cross- sectional area of the fuel channel, the plates are moved away from each other.
  • thermometer measuring the temperature of the combustion area is connected to the second actuator, which changes the position of the movable actuators that adjust the cross-sectional area of the fuel channel. Then the second actuator con- trols the position of the adjusters on the basis of readings obtained from the thermometer in accordance with predetermined instructions.
  • the cross-sectional area is reduced, the amount of materials evaporated in the pyrolysis area is reduced and more carbon is burnt in the combustion area, in which case the tem- perature rises.
  • the cross-sectional area is increased, the temperature of the combustion area can be reduced, because the pyrolysis phase accelerates and more material to be heated gets to the combustion area.
  • This second actuator may be computer- controllable, automated in some other way or manually controllable. Adjusting the cross-sectional area thus also changes the size of the combustion area. This can be used for adjusting the power of the gasifying generator and for compensating for the properties of the fuel.
  • the combustion process of the gasifying generator can be controlled and its temperature caused to remain within the desired limits.
  • the invention also relates to equipment for applying the above described method.
  • the equipment comprises a gasifying generator with a body, a fuel channel for fuel feed and the gasification processes, and one or more oxidation pipes, by which oxidation gas is fed to the combustion area.
  • the equipment is characterized in that the oxidation pipes are movable within the fuel channel for feeding the oxidation gas to the desired point in the fuel channel.
  • the oxidation pipes are arranged to be adjusted separately or in one or more groups.
  • thermometer for measuring the temperature of the combustion area.
  • the thermometer is preferably connected to the first actuator, which has been programmed to adjust the location of the oxidation gas discharge end of the oxidation pipes within the fuel channel in accordance with the measurement results obtained from the thermometer.
  • the gasifying generator has an oxidation pipe essentially parallel with the longitudinal axis of the fuel channel, to which the oxidation gas has been directed and from the discharge end of which the oxidation gas flows out to the desired area.
  • the fuel channel is preferably vertical.
  • the pipe moving mechanism is a solution suitable for the purpose, which may be, for example, a hydraulic or motorized solution. The movement of the end of the pipe takes place between the pyrolysis and the combustion areas. The flow of the gas is accomplished ei- ther by over- or underpressure.
  • the discharge end of the oxidation pipe has been formed in such a way that the oxidizer gas coming from it remains in the desired place and does not disturb the movements of the fuel flow.
  • this has been done by adding to the discharge end of the oxidation pipe an oxidizer gas controller, which guides the gas to the near environment of the oxidation pipe to an area in which the oxidizer gas is wanted to have an effect.
  • the pipe can be closed and have holes made in it, which direct the discharge of the oxidizer gas in the desired direction.
  • the oxidation pipes can have ro- tatable discharge ends for guiding the oxidizer gas.
  • the place of oxidation can be controlled in many different ways.
  • the pipe or pipes may come from the sides of the body of the gasifying generator, for example, and can be directed therefrom to the desired point, or the pipes are otherwise entirely outside the body, but their discharge ends coming to the fuel channel have been shaped in a way that their movements can be used to guide the oxidation gas jets in the fuel channel.
  • a lower combustion area in the lower part of the gasifying generator in which the carbonized resi- due formed in the gasification processes is burnt up.
  • Oxidizer gas is led to this lower combustion area by its own, separate feed connection.
  • This lower combustion causes the reduction area to flow downwards, and the ash created in the actual combustion area cannot thus block the fuel channel. This also reduces the amount of ash created.
  • the product gas of the gasifying generator according to the invention can be led out from the gasifier for the desired purpose.
  • the gas created can also be combusted in the gasifier itself after the reduction area, in which case the gasifying generator according to the invention can be used for heat production, for example.
  • the materials of the parts used in the gasifying generator described are preferably metallic, ceramic or other materials that withstand high temperatures.
  • the invention has the advantage that it improves the purity and quality of the product gas. It has been found in analyses that the composition of the product gas obtained by the method according to the invention is, on the average, 21 % CO, 15% H 2 , 11% CO 2 , 2% CH 4 , while the rest is mainly nitrogen, which is a relatively good result.
  • the purity of the product gas enables its use in a versatile manner. In addition, it simplifies and makes the costs of manufacture and use of the equipment lower than earlier.
  • the purification process of the product gas is also substantially simplified.
  • the invention has the advantage that the temperatures are accurately controlled, and thus the gasification reactions also remain under control and do not produce undesired ingredients, such as tar compounds, which could harm the processes and the operation of the gasifying generator by accruing onto the inner surface of the fuel channel, for example.
  • the invention has the advantage that the fuel will thus be used as efficiently as possible, and the process becomes more economical than the earlier solutions.
  • Fig. 1 shows a cross-section of a preferred embodiment of a gasifying generator according to the invention.
  • Fig. 1 shows an example of a gasifying generator according to the invention, used in a vertical position, in cross-section.
  • the gasifying generator has a cylindrical body 1 , inside which there is a fuel channel 2, which mostly follows the shapes of the body.
  • a fuel channel 2 In the upper part of the fuel channel there is fuel feed equipment 3.
  • the feed equipment 3 is closed by an airtight cover 25, which is only opened when fuel is added.
  • the fuel channel 2 can be divided into the following areas: the area of uncombusted fuel 4, pyrolysis area 5, combustion area 6, reduction area 7 and the lower combustion area 8.
  • the area 4 of uncombusted fuel is uppermost and the lower combustion area 8 is the lowest.
  • oxidation pipe 10 Inside the fuel channel there is an oxidation pipe 10, in the first upward pointed end of which there is a discharge end 11 , from which the oxidizer gas is directed to the combustion area 6.
  • the oxidation pipe 10 runs in the fuel channel 2 in the direction of its longitudinal axis.
  • One end of the oxidation pipe extends through the bottom of the fuel channel to the chamber 13 in the lower part of the body.
  • the oxidation gas transport system belonging to the gasifying generator also comprises oxidation gas transport piping 12 running around the fuel channel 2, the first end of which opens outside the body 1 and the second end of which leads to a chamber 13 in the lower part of the body.
  • the oxidation gas is pumped through the transport piping to the chamber, in which overpressure is formed.
  • the second end of the oxidation pipe 10 extending to the chamber 13 has been connected to the first actuator 14, by which the oxidation pipe can be moved in the up and down directions within the fuel chamber.
  • the oxidation pipe 10 is surrounded at its lower part by a casing pipe 9 fixedly installed to the body 1 , which penetrates through the bottom of the body 1 of the gasifying generator, and the upward pointed aperture of which has been sealed so that when the oxidation pipe 10 is moving, no oxidation gas gets to the fuel channel from the overpressurized oxidation gas chamber 13.
  • the lower combustion area 8 in the lower part of the fuel channel 2 gets its oxidation gas along the oxidizer pipe 15.
  • the ash and other material accumulated on the bottom of the fuel channel 2 are removed by an ash removal system 16, which leads the ash to the container 17. This technique is known as such.
  • the fuel channel 2 has a narrowing 18, which has been implemented by shaping the fuel channel at this point to the shape of a narrowing and opening funnel.
  • a thermometer 20 At the point of the narrowing in the fuel channel there is a thermometer 20 and movable adjustors 19 for changing the cross-sectional area of the fuel channel.
  • the movable adjustors 19 that change the cross-sectional area of the fuel channel are controlled by the second actuator 21.
  • thermometer 20 and the first and the second actuators 14 and 21 of the cross-sectional area control means are connected to a control unit 22, which controls their operation.
  • This control unit is preferably a computer.
  • the product gas created in the fuel channel 2 is led out from the gasifying generator to the product gas outlet pipe 23.
  • the processing of the product gas in the generator and the method for bringing it outside the body depend on the purpose of use of the product gas and the generator.
  • the gasification process takes place in the following manner: Inside the body 1 of the gasifying generator there is a fuel channel 2, in which the gasification processes take place.
  • the fuel is fed to the upper part of the fuel channel 2 by fuel feed equipment 3.
  • the fuel flows by means of gravity to the pyrolysis area 5 heated by the combustion area 6, where volatile materials are separated from the fuel.
  • the fuel flows further to the combustion area 6, in which it participates in the combustion reaction, which is maintained by the oxidation gas coming from the discharge end 11 of the oxidation pipe 10.
  • the combustion gases, carbonized residue and ash created in the combustion area 6 are moved to the reduction area 7, where the combustion gases are reduced.
  • the carbonized residue created in the reactions mentioned above is burnt up in the lower combustion area 8, to which oxidation gas is led from the pipe 15.
  • the combustion waste created can be removed by ash removal equipment 16, which leads the waste to the container 17.
  • the product gas generated in the process exits from the gasifying generator along the discharge pipe 23.
  • the temperature of the combustion area 6 is measured by a thermometer 20.
  • the measurement results given by the thermometer are read by the control unit 22. If the measured temperature is higher than the temperature set value given to the control unit 22, the first actuator 14 raises the oxidising pipe 10. Then the discharge end 11 of the oxidation pipe moves towards the pyrolysis area 5, whereby the amount of oxidation gas in the combustion area 6 is reduced, the combustion process slows down and the temperature falls.
  • control unit 22 can also be used to control second actuator 21 , which, when it is desired to lower the temperature measured by the thermometer 20, increases the cross-sectional area of the fuel channel 2 by adjustors, whereby the pyrolysis reactions accelerate and more material to be heated comes to the combustion area, and thus the temperature of the combustion area falls.
  • second actuator 21 when it is found by the control unit 22 that the temperature of the combustion area 6 measured by the thermometer 20 is too low compared to the set value, the oxidation pipe 10 is lowered by the first actuator 14. Then the dis- charge end 11 of the oxidation pipe directs more oxidation gas to the combustion area 6, causing the combustion process to accelerate and the temperature to rise.
  • the pyrolysis reaction is attenuated and thus more carbon, which can participate in the combustion, comes to the combustion area 6.
  • the combustion reaction is intensified.
  • the temperature of the combustion area 6 can be made to stay within the desired limits.
  • the adjustment of the temperature of the combustion process is mainly accomplished by moving the oxidation pipes 10.
  • the system according to the invention can also be implemented in ways that differ from those described above.
  • the entire gasifying generator can be in some other than vertical position in the system.
  • some adjustments can be implemented manually or automatically according to predetermined programming. Only one oxidation pipe is shown in the preferred embodiment of the gasifying generator in Fig. 1. There can naturally be more than one oxidation pipe, and they can be moved either each one separately or in groups.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

The gasifying generator according to the invention has a body (1), a fuel channel (2) for fuel feed and the gasification processes, and one or more oxidation pipes (10) for feeding the oxidation gas to the fuel channel. The oxidation gas discharge ends (11 ) of the oxidation pipes are movable within the fuel channel so that the oxidation point can be moved in the gasification process. They can be moved either separately or in groups. The number of oxidation pipes can be chosen according to the size of the gasifying generator and on the basis of the desired adjusting accuracy of the combustion process. The fuel channel of the gasifying generator can have a narrowing (18), which restrains the free flow of the fuel. The combustion area (6) is generally located at this narrowing. The temperature of the combustion area is measured by a thermometer (20). The location of the oxidation pipes is adjusted on the basis of readings obtained from the thermometer in ac¬ cordance with predetermined instructions. The temperature is given a desired set value. If the measured temperature is higher than the set value of the temperature, the oxidation gas discharge end of the oxidation pipes is moved away from the combustion area, whereby it gets less oxidation gas, combustion slows down and the temperature thus falls. In a corresponding manner, if the measured temperature is lower than the set value, the oxidation gas discharge end of the oxidation pipes is moved towards the combustion process, whereupon the combustion in the combustion area accelerates and the temperature rises.

Description

Method for gasifying fuel and a gasifying generator
The invention relates to a method for gasifying fuel in the fuel channel of a gasifying generator, the fuel channel having a combustion area for fuel combustion and one or more oxidation pipes for supplying oxidation gas to the combustion area. The invention also relates to a gasifying generator used in the method.
The fuel is generally supplied to the upper part of the gasifying generator, from which it flows by means of gravity through the pyrolysis, combustion and reduction areas. The heat required for gasification is obtained by burning fuel, whereby a pyrolysis area is formed between the combustion area and the fuel, in which the volatile materials are separated from the fuel. These volatile materials form the product gas of the gasifying generator together with the gases generated in the reduction area.
The prior art gasifying generators are divided into cocurrent gasifiers and counter- current gasifiers according to the oxidation gas supply method. In cocurrent gasifi- ers, the oxidation gas is fed directly to the combustion area. In these solutions, it is difficult to make the combustion area equally hot throughout, and also the efficiency remains low, because the carbonized residue created in the processes does not burn completely. In countercurrent gasifiers, the oxidation gas is conducted upwards from below, in the direction opposite to the fuel flow. In this method, the pyrolysis products end up in the product gas almost as such, i.e. the tars do not decompose.
An essential property of the product gas created in the gasifying generator with regard to its use is its purity. Especially the tar generated in the gasification is a problematic ingredient of the product gas because of the emissions caused by it, limitations of use and the problems caused to the equipment. Tar compounds decompose in temperatures exceeding 850°C. Another essential impurity that arises in gasification is the nitrogen oxides that are generated in temperatures exceeding 10000C. For these reasons, temperature control especially in the combustion zone after the pyrolysis phase is important in gasification.
Patent publication GB 456111 A describes a gasifying generator, in which oxidation gas is fed by oxidation pipes into the fuel channel. The oxidation pipes are movable inside the fuel channel. This adjustment possibility has been made for enabling the adaptation of the gasifying generator for different fuels. The location of the oxidation pipes is not changed during the combustion event. An attempt is i made to control the combustion event by adjusting the amount of oxidation gas getting into the oxidation pipes. According to the specification, the advantage achieved by the possibility of moving the pipes is that the oxidation pipes can be installed at different heights in the fuel channel. Adjusting the temperature of the combustion event is cumbersome with the method described in the specification. In addition, oxidation pipes coming from above cause additional friction in the fuel flow, and the oxidation gas may form flow channels in the vicinity of the surface of the oxidation pipe.
In the gasifying generator disclosed in the patent specification Fl 113781 B, the horizontal cross-section of the throat is adjusted by an adjusting cone moving in the vertical direction, the movements of which control the flow of the gas and thus control the operation of the generator. In patent specification Fl 112798 B, there is disclosed a method having fixed feed connections of the oxidizing gas to different parts of the gasifying generator, and the use of water vapour to restrain the com- bustion. A similar solution has also been found in patent specification US 5226927, in which oxidizing gas is fed to the combustion area from apertures in the casing of the gasifying generator. Although these methods improve the gasification result, the combustion event itself and its temperature cannot be regulated accurately.
It is an objective of the invention to accomplish a method for gasifying fuel in a gasifying generator and a gasifying generator, by which the disadvantages and deficiencies related to the prior art can be substantially reduced. Especially the combustion temperature can be well controlled in the invention.
The method and equipment according to the invention are characterized in what is set forth in the independent claims. Some preferred embodiments of the invention are set forth in the dependent claims.
In the gasifying generator used in the method according to the invention there is a body, a fuel channel for fuel feed and the gasification processes, and one or more oxidation pipes for feeding the oxidation gas to the fuel channel. The invention is characterized in that the oxidation gas discharge ends of the oxidation pipes are movable within the fuel channel in such a way that the point of oxidation can be moved in the gasification process.
The temperature of the combustion area is controlled by moving the oxidation pipes against the fuel stream or in the direction of the fuel stream. The oxidation pipes can be moved either separately or in groups. The number of oxidation pipes can be selected according to the size of the gasifying generator and the desired control accuracy of the combustion process. Each oxidation pipe can have its own combustion area, but they have a common fuel feed and lower combustion area.
The fuel channel of the gasifying generator can have a narrowing or other structural solution, which restrains the free flow of the fuel. The combustion area is generally located at this narrowing. The temperature of the combustion area is measured by a thermometer. The thermometer is preferably connected to the first actuator, which controls the oxidation pipes and especially their oxidation gas dis- charge ends within the fuel channel. The first actuator adjusts the location of the oxidation pipes on the basis of readings obtained from the thermometer according to predetermined instructions. This first actuator may be computer-controllable, automated in some other way or manually controllable. In the method, the temperature is given a desired set value, which is given to the first actuator or some device controlling it. If the measured temperature is higher than the set value of the temperature, the first actuator moves the oxidation gas discharge end of the oxidation pipes in the direction of the pyrolysis area, whereby the combustion area receives less oxidation gas, combustion slows down in the combustion area, and the temperature thus falls. Correspondingly, if the measured temperature is lower than the set value, the oxidation gas discharge end of the oxidation pipes is moved towards the combustion process, whereby the combustion in the combustion area accelerates and the temperature rises. It has been found experimentally that the best results with regard to the gasification processes and the product gas are obtained when a temperature exceeding 8500C is chosen as the set value of the temperature.
The cross-sectional area of the fuel channel can be changed by one or more movable adjuster(s) for adjusting the fuel flow and for determining the size of the combustion area. These adjusters are in compliance with the prior art as such. One possible way of implementing the adjusters is to place in the fuel channel two heat-resistant plates perpendicular to the main axis of the fuel channel, which move towards each other from the opposite sides of the fuel channel and thus reduce the cross-sectional area of the narrowing. In order to increase the cross- sectional area of the fuel channel, the plates are moved away from each other.
The thermometer measuring the temperature of the combustion area is connected to the second actuator, which changes the position of the movable actuators that adjust the cross-sectional area of the fuel channel. Then the second actuator con- trols the position of the adjusters on the basis of readings obtained from the thermometer in accordance with predetermined instructions. When the cross-sectional area is reduced, the amount of materials evaporated in the pyrolysis area is reduced and more carbon is burnt in the combustion area, in which case the tem- perature rises. When the cross-sectional area is increased, the temperature of the combustion area can be reduced, because the pyrolysis phase accelerates and more material to be heated gets to the combustion area. When the temperature of the combustion process rises too much, combustion can be restrained by this increasing of the cross-sectional area, in addition to by moving the oxidation pipe, and thus the temperature be lowered. In a corresponding way, when the temperature is too low, the combustion process can be accelerated by reducing the above mentioned cross-sectional area. This second actuator may be computer- controllable, automated in some other way or manually controllable. Adjusting the cross-sectional area thus also changes the size of the combustion area. This can be used for adjusting the power of the gasifying generator and for compensating for the properties of the fuel.
In the method according to the invention, by adjusting the location of the oxidation pipes in the fuel channel and the adjusters that change the cross-sectional area of the fuel channel either together or separately by the first and the second actuator, the combustion process of the gasifying generator can be controlled and its temperature caused to remain within the desired limits.
The invention also relates to equipment for applying the above described method. The equipment comprises a gasifying generator with a body, a fuel channel for fuel feed and the gasification processes, and one or more oxidation pipes, by which oxidation gas is fed to the combustion area. The equipment is characterized in that the oxidation pipes are movable within the fuel channel for feeding the oxidation gas to the desired point in the fuel channel.
In a preferred embodiment of the equipment according to the invention, the oxidation pipes are arranged to be adjusted separately or in one or more groups.
In another preferred embodiment of the equipment according to the invention, there is a narrowing in the fuel channel of the gasifying generator, with a thermometer for measuring the temperature of the combustion area. The thermometer is preferably connected to the first actuator, which has been programmed to adjust the location of the oxidation gas discharge end of the oxidation pipes within the fuel channel in accordance with the measurement results obtained from the thermometer.
In an embodiment, the gasifying generator has an oxidation pipe essentially parallel with the longitudinal axis of the fuel channel, to which the oxidation gas has been directed and from the discharge end of which the oxidation gas flows out to the desired area. The fuel channel is preferably vertical. The pipe moving mechanism is a solution suitable for the purpose, which may be, for example, a hydraulic or motorized solution. The movement of the end of the pipe takes place between the pyrolysis and the combustion areas. The flow of the gas is accomplished ei- ther by over- or underpressure.
The discharge end of the oxidation pipe has been formed in such a way that the oxidizer gas coming from it remains in the desired place and does not disturb the movements of the fuel flow. In a preferred embodiment of the invention this has been done by adding to the discharge end of the oxidation pipe an oxidizer gas controller, which guides the gas to the near environment of the oxidation pipe to an area in which the oxidizer gas is wanted to have an effect. There are also other possible solutions for shaping the end of the pipe. For example, the pipe can be closed and have holes made in it, which direct the discharge of the oxidizer gas in the desired direction. In these embodiments, the oxidation pipes can have ro- tatable discharge ends for guiding the oxidizer gas.
The place of oxidation can be controlled in many different ways. For example, there can be a number of pipes like the one described above, and they can all be adjusted separately or in groups. The pipe or pipes may come from the sides of the body of the gasifying generator, for example, and can be directed therefrom to the desired point, or the pipes are otherwise entirely outside the body, but their discharge ends coming to the fuel channel have been shaped in a way that their movements can be used to guide the oxidation gas jets in the fuel channel.
In a preferred embodiment of the method of the invention there is a lower combustion area in the lower part of the gasifying generator, in which the carbonized resi- due formed in the gasification processes is burnt up. Oxidizer gas is led to this lower combustion area by its own, separate feed connection. This lower combustion causes the reduction area to flow downwards, and the ash created in the actual combustion area cannot thus block the fuel channel. This also reduces the amount of ash created. The product gas of the gasifying generator according to the invention can be led out from the gasifier for the desired purpose. The gas created can also be combusted in the gasifier itself after the reduction area, in which case the gasifying generator according to the invention can be used for heat production, for example.
The materials of the parts used in the gasifying generator described are preferably metallic, ceramic or other materials that withstand high temperatures.
The invention has the advantage that it improves the purity and quality of the product gas. It has been found in analyses that the composition of the product gas obtained by the method according to the invention is, on the average, 21 % CO, 15% H2, 11% CO2, 2% CH4, while the rest is mainly nitrogen, which is a relatively good result. The purity of the product gas enables its use in a versatile manner. In addition, it simplifies and makes the costs of manufacture and use of the equipment lower than earlier. The purification process of the product gas is also substantially simplified.
Furthermore, the invention has the advantage that the temperatures are accurately controlled, and thus the gasification reactions also remain under control and do not produce undesired ingredients, such as tar compounds, which could harm the processes and the operation of the gasifying generator by accruing onto the inner surface of the fuel channel, for example.
In addition, the invention has the advantage that the fuel will thus be used as efficiently as possible, and the process becomes more economical than the earlier solutions.
In the following, the equipment and method according to the invention will be described more closely with reference to the accompanying drawing, in which
Fig. 1 shows a cross-section of a preferred embodiment of a gasifying generator according to the invention.
Fig. 1 shows an example of a gasifying generator according to the invention, used in a vertical position, in cross-section. The gasifying generator has a cylindrical body 1 , inside which there is a fuel channel 2, which mostly follows the shapes of the body. In the upper part of the fuel channel there is fuel feed equipment 3. The feed equipment 3 is closed by an airtight cover 25, which is only opened when fuel is added. The fuel channel 2 can be divided into the following areas: the area of uncombusted fuel 4, pyrolysis area 5, combustion area 6, reduction area 7 and the lower combustion area 8. When the gasifying generator is in the vertical position shown in Fig. 1 , the area 4 of uncombusted fuel is uppermost and the lower combustion area 8 is the lowest. Inside the fuel channel there is an oxidation pipe 10, in the first upward pointed end of which there is a discharge end 11 , from which the oxidizer gas is directed to the combustion area 6. The oxidation pipe 10 runs in the fuel channel 2 in the direction of its longitudinal axis. One end of the oxidation pipe extends through the bottom of the fuel channel to the chamber 13 in the lower part of the body.
The oxidation gas transport system belonging to the gasifying generator also comprises oxidation gas transport piping 12 running around the fuel channel 2, the first end of which opens outside the body 1 and the second end of which leads to a chamber 13 in the lower part of the body. The oxidation gas is pumped through the transport piping to the chamber, in which overpressure is formed. The second end of the oxidation pipe 10 extending to the chamber 13 has been connected to the first actuator 14, by which the oxidation pipe can be moved in the up and down directions within the fuel chamber. The oxidation pipe 10 is surrounded at its lower part by a casing pipe 9 fixedly installed to the body 1 , which penetrates through the bottom of the body 1 of the gasifying generator, and the upward pointed aperture of which has been sealed so that when the oxidation pipe 10 is moving, no oxidation gas gets to the fuel channel from the overpressurized oxidation gas chamber 13.
The lower combustion area 8 in the lower part of the fuel channel 2 gets its oxidation gas along the oxidizer pipe 15. The ash and other material accumulated on the bottom of the fuel channel 2 are removed by an ash removal system 16, which leads the ash to the container 17. This technique is known as such.
The fuel channel 2 has a narrowing 18, which has been implemented by shaping the fuel channel at this point to the shape of a narrowing and opening funnel. At the point of the narrowing in the fuel channel there is a thermometer 20 and movable adjustors 19 for changing the cross-sectional area of the fuel channel. The movable adjustors 19 that change the cross-sectional area of the fuel channel are controlled by the second actuator 21.
The thermometer 20 and the first and the second actuators 14 and 21 of the cross-sectional area control means are connected to a control unit 22, which controls their operation. This control unit is preferably a computer. The product gas created in the fuel channel 2 is led out from the gasifying generator to the product gas outlet pipe 23. The processing of the product gas in the generator and the method for bringing it outside the body depend on the purpose of use of the product gas and the generator.
In the method according to the invention, the gasification process takes place in the following manner: Inside the body 1 of the gasifying generator there is a fuel channel 2, in which the gasification processes take place. The fuel is fed to the upper part of the fuel channel 2 by fuel feed equipment 3. The fuel flows by means of gravity to the pyrolysis area 5 heated by the combustion area 6, where volatile materials are separated from the fuel. The fuel flows further to the combustion area 6, in which it participates in the combustion reaction, which is maintained by the oxidation gas coming from the discharge end 11 of the oxidation pipe 10. The combustion gases, carbonized residue and ash created in the combustion area 6 are moved to the reduction area 7, where the combustion gases are reduced. The carbonized residue created in the reactions mentioned above is burnt up in the lower combustion area 8, to which oxidation gas is led from the pipe 15. The combustion waste created can be removed by ash removal equipment 16, which leads the waste to the container 17. The product gas generated in the process exits from the gasifying generator along the discharge pipe 23.
In the method according to the invention, the temperature of the combustion area 6 is measured by a thermometer 20. The measurement results given by the thermometer are read by the control unit 22. If the measured temperature is higher than the temperature set value given to the control unit 22, the first actuator 14 raises the oxidising pipe 10. Then the discharge end 11 of the oxidation pipe moves towards the pyrolysis area 5, whereby the amount of oxidation gas in the combustion area 6 is reduced, the combustion process slows down and the temperature falls. When required, the control unit 22 can also be used to control second actuator 21 , which, when it is desired to lower the temperature measured by the thermometer 20, increases the cross-sectional area of the fuel channel 2 by adjustors, whereby the pyrolysis reactions accelerate and more material to be heated comes to the combustion area, and thus the temperature of the combustion area falls. When it is found by the control unit 22 that the temperature of the combustion area 6 measured by the thermometer 20 is too low compared to the set value, the oxidation pipe 10 is lowered by the first actuator 14. Then the dis- charge end 11 of the oxidation pipe directs more oxidation gas to the combustion area 6, causing the combustion process to accelerate and the temperature to rise. In addition, by closing the adjustors 19 for the cross-sectional area of the fuel channel 2 by the second actuator 21 , the pyrolysis reaction is attenuated and thus more carbon, which can participate in the combustion, comes to the combustion area 6. Thus the combustion reaction is intensified. By the functions described above, the temperature of the combustion area 6 can be made to stay within the desired limits. The adjustment of the temperature of the combustion process is mainly accomplished by moving the oxidation pipes 10.
The system according to the invention can also be implemented in ways that differ from those described above. For example, the entire gasifying generator can be in some other than vertical position in the system. In addition, some adjustments can be implemented manually or automatically according to predetermined programming. Only one oxidation pipe is shown in the preferred embodiment of the gasifying generator in Fig. 1. There can naturally be more than one oxidation pipe, and they can be moved either each one separately or in groups.
Some preferred embodiments of the gasifying generator according to the invention have been described above. The invention is not limited to the solutions described above, but the inventive idea can be applied in numerous ways within the limits set by the claims.

Claims

Claims
1. A method for gasifying fuel in the fuel channel of a gasifying generator operating on the cocurrent principle, the fuel channel (2) having a combustion area (6) for the combustion of the fuel and one or more movable oxidation pipe(s) (10) for feeding oxidation gas to the combustion area (6), characterized in that the oxidation pipes are moved within the fuel channel during the combustion process for feeding oxidation gas to the desired point in the fuel channel.
2. A method according to Claim 1 , characterized in that the temperature of the combustion area (6) is adjusted by moving the oxidation pipes (10) against the fuel flow or in the direction of the fuel flow.
3. A method according to Claim 1 , characterized in that each oxidation pipe (10) is moved independently.
4. A method according to Claim 1 , characterized in that a plurality of oxidation pipes (10) are moved simultaneously as one or more groups.
5. A method according to any one of the claims 1 to 4, characterized in that the temperature of the combustion area (6) is measured by a thermometer (20), and the oxidation pipes (10) are moved on the basis of the measured temperature in accordance with predetermined instructions for maintaining the temperature of the combustion area (6) in the desired range.
6. A method according to any one of the claims 1 to 5, characterized in that the cross-sectional area of the fuel channel (2) is changed at the combustion area (6).
7. A method according to Claim 6, characterized in that the cross-sectional area of the fuel channel (2) is changed by movable adjustors (19) on the basis of the measured temperature of the combustion area according to predetermined instructions for keeping the temperature of the combustion area (6) within the desired range.
8. A gasifying generator operating on the cocurrent principle, comprising a body (1), a fuel channel (2) for fuel feed and the gasification processes, and one or more movable oxidation pipes (10) for feeding oxidation gas to the fuel channel, characterized in that the oxidation pipes (10) are movable during the combustion process within the fuel channel for feeding the oxidation gas to the desired point in the fuel channel.
9. A gasifying generator according to Claim 8, characterized in that the oxidation pipes (10) are movable within the fuel channel (2) substantially in the direction of the longitudinal axis of the fuel channel.
10. A gasifying generator according to any one of the Claims 8 to 9, characterized in that the oxidation pipes (10) are arranged to come to the fuel channel (2) substantially from below.
11. A gasifying generator according to any one of the Claims 8 to 10, character- ized in that the oxidation pipes (10) have discharge ends (11), which have been shaped for directing the oxidation gas to the fuel channel (2) in the desired manner.
12. A gasifying generator according to Claim 11 , characterized in that the discharge ends (11) of the oxidation pipes (10) have been shaped so as to prevent flows in the direction of the fuel flow.
13. A gasifying generator according to any one of the claims 8 to 12, characterized in that it additionally comprises a first actuator (14) for moving the oxidation pipes and a control unit (22) for controlling the first actuator.
14. A gasifying generator according to Claim 8, characterized in that there is a narrowing (18) in the fuel channel (2) for forming a combustion area (6) in the fuel channel.
15. A gasifying generator according to Claim 14, characterized in that in connection with the narrowing (18) of the fuel channel (2) there is a thermometer (20), which has been connected to the control unit (22) for moving the oxidation pipes (10) on the basis of the temperature of the combustion area (6).
16. A gasifying generator according to Claim 14 or 15, characterized in that there are movable adjusters (19) in the fuel channel (2) for changing the cross- sectional area of the narrowing (18).
17. A gasifying generator according to Claim 16, characterized in that it has a second actuator (21 ) for moving the movable adjustors (19).
18. A gasifying generator according to Claim 17, characterized in that the second actuator has been connected to the control unit (22) for controlling its operation.
19. A gasifying generator according to any one of the Claims 8 to 18, character- ized in that the oxidation pipes (10) have been arranged as independently movable.
20. A gasifying generator according to any one of the Claims 8 to 18, characterized in that the oxidation pipes (10) have been arranged to be movable as groups.
21. A gasifying generator according to any one of the Claims 8 to 20, character- ized in that the control unit (22) is a computer, to the memory of which the control program of the gasifying generator has been loaded.
EP07823244.4A 2006-11-17 2007-11-13 Method for gasifying fuel and a gasifying generator Not-in-force EP2092043B8 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL07823244T PL2092043T3 (en) 2006-11-17 2007-11-13 Method for gasifying fuel and a gasifying generator

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI20065733A FI122109B (en) 2006-11-17 2006-11-17 Method for gasification of fuel and gasification generator
PCT/FI2007/050608 WO2008059109A1 (en) 2006-11-17 2007-11-13 Method for gasifying fuel and a gasifying generator

Publications (4)

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EP2092043A1 true EP2092043A1 (en) 2009-08-26
EP2092043A4 EP2092043A4 (en) 2011-02-23
EP2092043B1 EP2092043B1 (en) 2014-02-12
EP2092043B8 EP2092043B8 (en) 2014-06-11

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EP (1) EP2092043B8 (en)
DK (1) DK2092043T3 (en)
ES (1) ES2461863T3 (en)
FI (1) FI122109B (en)
PL (1) PL2092043T3 (en)
PT (1) PT2092043E (en)
WO (1) WO2008059109A1 (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011101022A1 (en) * 2010-02-16 2011-08-25 Big Dutchman International Gmbh Gasification device and gasification method
FR2965816B1 (en) 2010-10-12 2014-04-25 S3D DEVICE FOR TRANSFORMING A FUEL
DE202011004328U1 (en) 2011-03-22 2012-06-25 Big Dutchman International Gmbh Manhole carburetor for operation in substoichiometric oxidation
FI123804B (en) * 2012-04-20 2013-10-31 Volter Oy Carburetor
DE202012008777U1 (en) * 2012-09-13 2015-10-06 Big Dutchman International Gmbh Apparatus for producing fuel gas from a solid fuel
DE102013015920B4 (en) * 2013-09-20 2015-12-17 Recom Patent & License Gmbh Device in the form of a 3-zone carburetor and method for operating such a carburetor for the thermal conversion of waste products and wastes
DE102014225166A1 (en) * 2014-12-08 2016-06-09 Autark Energy Gmbh DC fixed-bed gasifier for producing a product gas from pourable biomass particles
IT201600082716A1 (en) * 2016-08-05 2018-02-05 Leandro Mini Gasifier and method of use

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB884740A (en) * 1957-09-30 1961-12-13 Ferdinand Lentjes Stiftung Improvements relating to gas producers
EP1148295A1 (en) * 1999-01-27 2001-10-24 Sumitomo Metal Industries, Ltd. Gasification melting furnace for wastes and gasification melting method
WO2002046331A1 (en) * 2000-12-04 2002-06-13 Emery Energy Company L.L.C. Multi-faceted gasifier and related methods

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE653320C (en) * 1934-12-03 1937-11-20 Banki App G M B H Double-jacketed gas generator with a downward draft
GB456111A (en) * 1935-04-11 1936-11-03 Humboldt Deutzmotoren Ag Improvements in or relating to gas producers with simultaneous up and down draught
SE453670C (en) * 1986-07-08 1989-09-25 Waste Gas Energy Ab Wge DEVICE FOR THE PREPARATION OF GAS FROM FIXED BRAINS
DE19916931C2 (en) * 1999-03-31 2001-07-05 Deponie Wirtschaft Umweltschut Air supply pipe for a gasifier for generating fuel gas
JP2001234175A (en) * 2000-02-23 2001-08-28 Nippon Steel Corp Process for operating vertical self-burning carbonization oven
JP4372302B2 (en) * 2000-03-09 2009-11-25 株式会社環境技術開発研究機構 Rotary carbonization equipment
FI113781B (en) * 2002-11-01 2004-06-15 Timo Saares gas generator

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB884740A (en) * 1957-09-30 1961-12-13 Ferdinand Lentjes Stiftung Improvements relating to gas producers
EP1148295A1 (en) * 1999-01-27 2001-10-24 Sumitomo Metal Industries, Ltd. Gasification melting furnace for wastes and gasification melting method
WO2002046331A1 (en) * 2000-12-04 2002-06-13 Emery Energy Company L.L.C. Multi-faceted gasifier and related methods

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of WO2008059109A1 *

Also Published As

Publication number Publication date
EP2092043A4 (en) 2011-02-23
FI122109B (en) 2011-08-31
FI20065733A (en) 2008-05-18
EP2092043B1 (en) 2014-02-12
WO2008059109A1 (en) 2008-05-22
EP2092043B8 (en) 2014-06-11
PT2092043E (en) 2014-05-06
FI20065733A0 (en) 2006-11-17
DK2092043T3 (en) 2014-05-05
ES2461863T3 (en) 2014-05-21
PL2092043T3 (en) 2014-07-31

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