JP2018002808A - Carbide manufacturing device, carbide manufacturing method and carbide manufacturing system - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a carbide manufacturing device capable of manufacturing carbide of which components other than carbon are sufficiently removed while suppressing reduction of the carbon component contained in an organic material.SOLUTION: There is provided a carbide manufacturing device having a body part 21, a cylindrical part 22 having an outer peripheral surface forming a gap 20a for carbonization of an organic waste material between an inner peripheral surface of the body part 21, an organic waste material injection part 23 for injecting the organic waste material to the gap 20a, a primary air supply part 25 for supplying air for primary burning which partially burns the organic waste material deposited in the gap 20a, a carbide discharge part 24 for discharging carbide by carbonizing the organic waste article from the gap 20a, and a control part 29 for controlling carbonization state of the organic waste material so that the organic waste material is maintained in the gap 20a at a prescribed temperature range and the organic waste material is deposited in the gap 20a over prescribed time.SELECTED DRAWING: Figure 2

Description

  The present invention relates to a carbide manufacturing apparatus, a carbide manufacturing method, and a carbide manufacturing system.

2. Description of the Related Art Conventionally, a carbonization furnace that partially burns organic matter and carbonizes the organic matter with the heat of combustion is known (for example, see Patent Document 1).
The carbonization furnace disclosed in Patent Document 1 forms a carbonization portion that carbonizes solids containing a large amount of carbide above a region formed between a substantially cylindrical main body and a cylindrical body accommodated in the main body, A non-combustible part that extinguishes the carbide is formed below.

  Patent document 1 pays attention to the problem that carbonization efficiency will fall, if the atmospheric temperature of a carbonization part will fall by the air blown from the inside of a cylindrical body. In Patent Document 1, a cylindrical body has a double wall structure including a preheating chamber inside, and air heated in the preheating chamber is supplied to the carbonization portion to prevent a decrease in the ambient temperature of the carbonization portion.

Japanese Patent No. 4222666

  Organic materials such as wood wastes contain carbon, oxygen, hydrogen, and nitrogen as main elements, and also have trace amounts of inorganic components such as calcium. In order to obtain a carbide having a high carbon component content (hereinafter also referred to as carbon content) and increase the yield of the carbon component (hereinafter also referred to as carbon yield) using such an organic material as a raw material, It is necessary to perform a carbonization treatment that sufficiently removes other components while suppressing the decrease in the amount of carbon dioxide.

However, if carbonization of an organic substance is performed at a high temperature in order to remove other components other than the carbon component, a part of the carbon component is completely burned and the carbon yield is lowered. In addition, when carbonization of an organic substance is performed at a low temperature at which the carbon component is not completely burned in order to increase the carbon yield, the carbon content of the carbide is reduced because other components other than the carbon component are not sufficiently removed. .
Patent Document 1 discloses that the cylindrical body has a double-wall structure in order to prevent a decrease in the ambient temperature of the carbonized portion, but does not disclose a structure that increases both the carbon yield and the carbon content. .

  This invention is made in view of such a situation, The carbide manufacturing apparatus which can manufacture the carbide | carbonized_material from which other components other than a carbon component were fully removed, suppressing the reduction | decrease of the carbon component contained in organic substance. An object of the present invention is to provide a carbide manufacturing method and a carbide manufacturing system.

In order to solve the above problems, the present invention employs the following means.
The carbide manufacturing apparatus which concerns on 1 aspect of this invention is formed between the main-body part formed in the cylinder shape extended along an axis, and the internal peripheral surface of the said main-body part while being formed in the cylinder shape extended along the said axis. A cylindrical portion having an outer peripheral surface that forms a gap for carbonizing organic matter, an organic matter introduction portion that introduces the organic matter into the gap, and air that supplies combustion air that partially burns the organic matter that accumulates in the gap A supply portion, a carbide discharge portion for discharging carbide obtained by carbonizing the organic matter from the gap, and the organic matter is maintained in a predetermined temperature range in the gap, and the organic matter is deposited in the gap over a predetermined time. A control unit that controls the carbonization state of the organic matter.

  According to the carbide manufacturing apparatus according to one aspect of the present invention, in the normal operation state of the carbonization furnace, the organic material is charged from the organic material charging portion into the gap formed between the inner peripheral surface of the main body portion and the outer peripheral surface of the cylindrical portion. Then, the organic matter thrown from the organic matter throwing portion is deposited from the bottom to the top of the gap along the axis. The organic matter on the upper layer side of the gap is partially combusted by the combustion air supplied from the air supply unit and guided to the lower layer side of the gap. The organic substance on the lower layer side of the gap is blocked by the organic substance on the upper layer side, and the lower layer side of the gap becomes a carbide smelting / cooling region in which solid content containing a large amount of carbon components is refined and cooled. In the carbide refining / cooling region, the solid content containing a large amount of carbon components is refined while being further carbonized in a state where the oxygen concentration is low, and gradually cooled as it approaches the lower end of the gap. Thereby, the temperature of the carbide | carbonized_material discharged | emitted from the lower end of a gap | interval can be made low.

  Moreover, according to the carbide manufacturing apparatus concerning 1 aspect of this invention, the carbonization state of organic substance is controlled by a control part so that organic substance may be maintained in a predetermined temperature range with a gap | interval. Therefore, the organic matter is heated to a high temperature and most of the carbon components are completely burned, or the organic matter is lowered to a low temperature in the gap and other problems other than the carbon component cannot be sufficiently removed. it can. Here, for example, the predetermined temperature range is preferably 900 ° C. or more and 1200 ° C. or less, and more preferably 1000 ° C. or more and 1100 ° C. or less.

Further, according to the carbide manufacturing apparatus according to one aspect of the present invention, the control unit controls the organic substance to be deposited in the gap over a predetermined time. For this reason, it is possible to suppress a problem that the time during which the organic substance is deposited in the gap is shortened and other components other than the carbon component cannot be sufficiently removed from the organic substance. Here, the predetermined time is preferably in the range of, for example, 30 minutes or more and 50 minutes or less.
Thus, according to the carbide manufacturing apparatus concerning 1 aspect of this invention, the carbide | carbonized_material from which other components other than a carbon component were fully removed can be manufactured, suppressing the reduction | decrease of the carbon component contained in organic substance. .

In the carbide manufacturing apparatus according to one aspect of the present invention, the control unit controls a supply amount of the combustion air supplied by the air supply unit so that the organic substance is maintained in the predetermined temperature range through the gap. And it is good also as a structure which controls the discharge | emission amount of the said carbide | carbonized_material discharged | emitted by the said carbide | carbonized_material discharge part so that the said organic substance may accumulate in the said gap | interval over the said predetermined time.
By doing this, the supply amount of combustion air is controlled to maintain the organic matter in a predetermined temperature range with a gap, and the discharge amount of carbide is controlled so that the organic matter is deposited in the gap over a predetermined time, A carbide having a high carbon content can be produced while increasing the carbon yield.

In the carbide manufacturing apparatus having the above-described configuration, the first temperature detection unit that detects the ambient temperature of the fuel region in which the organic matter is partially burned by the combustion air, and the second temperature that detects the temperature of the organic matter that accumulates in the gap. A detection unit, wherein the control unit controls a supply amount of the combustion air supplied by the air supply unit according to a temperature detected by the first temperature detection unit, and the second temperature detection unit You may control the discharge | emission amount of the said carbide | carbonized_material which the said carbide | carbonized_material discharge part discharge | releases according to the temperature to detect.
By doing so, the supply amount of combustion air is controlled according to the ambient temperature of the combustion region to maintain the organic matter within a predetermined temperature range, and the discharge amount of carbide is controlled according to the temperature of the organic matter accumulated in the gap. Thus, it is possible to produce a carbide having a high carbon content while increasing the carbon yield by depositing organic matter in the gaps over a predetermined time.

In the carbide manufacturing apparatus according to one aspect of the present invention, the carbide discharged from the carbide discharge portion and steam are thermally decomposed to generate water gas, and the heat decomposition portion is discharged from the pyrolysis portion. The structure provided with the carbide | carbonized_material collection | recovery part which collect | recovers the said carbide | carbonized_material may be sufficient.
By doing in this way, unreacted carbide | carbonized_material can be collect | recovered, carrying out the pyrolysis reaction of the carbide | carbonized_material with high carbon content, and water vapor | steam in a thermal decomposition part, and producing | generating water gas. This unreacted carbide is one obtained by washing with steam to remove other components other than the carbon component. Therefore, it is possible to obtain a carbide having a high carbon content in which other components other than the carbon component are well removed.

  The carbide manufacturing method which concerns on 1 aspect of this invention is formed between the main-body part formed in the cylinder shape extended along an axis, and the internal peripheral surface of the said main-body part while forming in the cylinder shape extended along the said axis. Using a carbide manufacturing apparatus comprising a cylindrical portion having an outer peripheral surface for carbonizing organic matter, and supplying an organic matter into the gap, supplying combustion air to the gap, and supplying the combustion air to the gap. An air supply step for partially burning the organic matter deposited in the gap; a carbide discharge step for discharging carbide obtained by carbonizing the organic matter from the gap; and the organic matter is maintained in a predetermined temperature range in the gap and the organic matter is kept for a predetermined time. And a control step of controlling the carbonization state of the organic substance so as to be deposited in the gap over the period.

According to the carbide manufacturing method according to one aspect of the present invention, the carbonization state of the organic substance is controlled by the control step so that the organic substance is maintained in a predetermined temperature range with a gap. Therefore, the organic matter is heated to a high temperature and most of the carbon components are completely burned, or the organic matter is lowered to a low temperature in the gap and other problems other than the carbon component cannot be sufficiently removed. it can.
Further, according to the carbide manufacturing method according to one aspect of the present invention, the control step controls the organic material to be deposited in the gap over a predetermined time. For this reason, it is possible to suppress a problem that the time during which the organic substance is deposited in the gap is shortened and other components other than the carbon component cannot be sufficiently removed from the organic substance.
Thus, according to the carbide manufacturing method according to one aspect of the present invention, it is possible to manufacture a carbide from which other components other than the carbon component are sufficiently removed while suppressing a decrease in the carbon component contained in the organic material. .

In the carbide manufacturing method according to one aspect of the present invention, the control step controls a supply amount of the combustion air supplied by the air supply step so that the organic matter is maintained in the predetermined temperature range, It is good also as a structure which controls the discharge | emission amount of the said carbide | carbonized_material discharged | emitted by the said carbide | carbonized_material discharge process so that organic substance may accumulate in the said gap | interval over the said predetermined time.
By doing this, the supply amount of combustion air is controlled to maintain the organic matter in a predetermined temperature range with a gap, and the discharge amount of carbide is controlled so that the organic matter is deposited in the gap over a predetermined time, A carbide having a high carbon content can be produced while increasing the carbon yield.

In the carbide manufacturing method having the above-described configuration, a first temperature detection step of detecting an ambient temperature of a fuel region in which the organic matter is partially burned by the combustion air, and a second temperature of detecting the temperature of the organic matter deposited in the gap. A detection step, wherein the control step controls a supply amount of the combustion air supplied by the air supply step according to a temperature detected by the first temperature detection step, and the second temperature detection step The amount of carbide discharged in the carbide discharging step may be controlled according to the temperature to be detected.
By doing so, the supply amount of combustion air is controlled according to the ambient temperature of the combustion region to maintain the organic matter within a predetermined temperature range, and the discharge amount of carbide is controlled according to the temperature of the organic matter accumulated in the gap. Thus, it is possible to produce a carbide having a high carbon content while increasing the carbon yield by depositing organic matter in the gaps over a predetermined time.

A carbide manufacturing system according to an aspect of the present invention includes the carbide manufacturing device according to any one of the above, a heat exchange unit that exchanges heat between the combustion gas discharged from the carbide manufacturing device and a heat medium, And a power generation unit that generates power by obtaining power from the heat medium heated by the heat exchange unit.
By doing in this way, the heat | fever of the combustion gas discharged | emitted from the carbide manufacturing apparatus can be collect | recovered as motive power of an electric power generation part, and the energy efficiency of the whole system can be raised.

The carbide manufacturing system according to one aspect of the present invention may include a drying unit that dries the organic matter charged from the organic matter charging unit by the combustion gas heat-exchanged by the heat exchange unit.
By doing in this way, the heat of the combustion gas discharged | emitted from the carbide manufacturing apparatus can be used for drying of organic substance, and the heat of combustion gas can be used still more effectively.

  According to the present invention, it is possible to provide a carbide manufacturing apparatus, a carbide manufacturing method, and a carbide manufacturing system capable of manufacturing a carbide from which components other than carbon are sufficiently removed while suppressing a decrease in the carbon component contained in the organic material. it can.

It is a whole lineblock diagram showing one embodiment of a water gas generation system. It is a longitudinal cross-sectional view of the carbonization furnace shown in FIG. It is a principal part enlarged view of the carbonization furnace shown in FIG. It is an end view of the carbonization furnace shown in FIG. 2, (a) is an AA arrow end view, (b) is an BB arrow end view. It is a flowchart which shows the control method of the ventilation volume of the primary combustion fan by a carbonization furnace control part. It is a flowchart which shows the control method of the ventilation volume of the secondary combustion fan by a carbonization furnace control part. It is a flowchart which shows the control method of the rotational speed of the turntable by a carbonization furnace control part. It is a longitudinal cross-sectional view of the pyrolysis furnace shown in FIG. It is a block diagram which shows the thermal decomposition furnace, temperature reducer, cyclone, steam generator, and steam superheater which are shown in FIG. It is a block diagram which shows the dryer shown in FIG. It is a figure which shows the image which imaged the carbide | carbonized_material obtained by a water gas production | generation system with the scanning electron microscope. It is a whole block diagram which shows the carbide manufacturing system of 2nd Embodiment.

<First Embodiment>
Hereinafter, a water gas generation system (carbide production apparatus; carbide production system) 100 according to a first embodiment of the present invention will be described with reference to the drawings.
The water gas generation system 100 of the present embodiment carbonizes organic waste, which is carbon-containing waste, to generate carbide, and then uses superheated steam (hereinafter also referred to as “steam”) as a gasifying agent. It is a system that generates a water gas (a mixed gas containing hydrogen gas, carbon monoxide gas, carbon dioxide gas as a main component) by causing thermal decomposition reaction of carbides.
The water gas generation system 100 of the present embodiment is also a carbide manufacturing system capable of manufacturing a carbide from which other components other than the carbon component are sufficiently removed while suppressing a decrease in the carbon component contained in the organic waste. .

  Organic waste is, for example, food waste, construction waste, shredder dust, livestock waste, wood waste such as thinned wood and pruned branches, sludge, and general waste discharged from households. Various organic wastes as exemplified above can be used as a raw material for generating water gas, but it is particularly preferable to use wood waste (also referred to as “woody biomass”). Moreover, in this embodiment, although organic waste was used, you may use the organic matter which should not be discarded as a raw material of a carbide | carbonized_material.

  As shown in the overall configuration diagram of FIG. 1, the water gas generation system 100 includes a dryer (drying unit) 10 that dries organic waste, a hopper 11 that stores organic waste to be input to the dryer 10, and a drying unit. Pyrolysis reaction of the hopper 12 which stores the organic waste dried with the machine 10, the carbonization furnace 20 which produces | generates a carbide | carbonized_material from the dried organic waste, and the carbide | carbonized_material and gasification agent which were produced | generated in the carbonization furnace 20 A pyrolysis furnace (pyrolysis section) 30 that generates water gas, a temperature reducer 40 that cools the water gas generated in the pyrolysis furnace 30, and a char that collects the carbides discharged from the pyrolysis furnace 30. A recovery device (carbide recovery unit) 41, a cyclone 50 for removing unreacted carbide and residue from the water gas supplied from the temperature reducer 40, and a residue for recovering unreacted carbide and residue removed by the cyclone 50 Recovery device ( And a product recovery section) 51.

In addition, the water gas generation system 100 includes a water gas cooling device 60 that cools the water gas from which carbides and residues are removed by the cyclone 50, a water gas holder 70 that stores the water gas cooled by the water gas cooling device 60, and A flare stack 71 that incinerates surplus water gas or the like, a power generation facility 72 using water gas as fuel, a hydrogen purifier 73 that purifies hydrogen gas from water gas, and a steam generator 80 that generates saturated steam from water A steam superheater 81 that superheats the steam generated by the steam generator 80, a water supply device 82 that supplies water to the steam generator 80, and a control device 90 that controls the entire water gas generation system 100. .
Hereinafter, each part with which the water gas production | generation system 100 is provided is demonstrated.

  The dryer 10 is an apparatus that dries organic waste with combustion gas and supplies the dried organic waste to the carbonization furnace 20. The dryer 10 is supplied with organic waste from a hopper 11 that stores the organic waste through a raw material supply path 11a. Moreover, the combustion gas discharged | emitted from the steam generator 80 is supplied to the dryer 10 through the combustion gas flow path 200d as a heat source which dries organic waste.

  The organic waste supplied from the hopper 11 to the dryer 10 is, for example, woody biomass crushed to a length of 5 mm or more and 60 mm or less by a crusher (not shown). Moreover, what contains a water | moisture content by the weight ratio of about 55% is used for an organic waste, for example. The dryer 10 lowers the moisture content of the organic waste to a weight ratio of about 15% by heating and drying the woody biomass containing the moisture at a weight ratio of about 55%.

  The dryer 10 supplies the organic waste dried by the heat of the combustion gas to the hopper 12 through the raw material supply path 10a. Further, the dryer 10 supplies the combustion gas used as a heat source for drying the organic waste to the exhaust gas cooling and cleaning device 13 through the combustion gas channel 200e. The temperature of the combustion gas supplied from the dryer 10 to the exhaust gas cooling and cleaning device 13 is adjusted to be 150 ° C. or higher and 210 ° C. or lower.

The exhaust gas cooling and cleaning device 13 is a device that removes harmful substances such as sulfur oxide (SO _x ), sulfuric acid (H ₂ SO ₄ ), and hydrochloric acid (HCl) contained in the combustion gas to render the combustion gas harmless. The exhaust gas cooling and cleaning device 13 cools the combustion gas (exhaust gas) from which harmful substances have been removed while detoxifying it, and then discharges it into the atmosphere.
The exhaust gas cooling and cleaning device 13 is a scrubber, for example, and is adjusted so that the temperature of the combustion gas discharged into the atmosphere is 120 ° C. or higher and 180 ° C. or lower.

The carbonization furnace 20 is an apparatus that generates carbide and combustion gas by partially burning dry organic waste. The carbonized furnace 20 is supplied with the dried organic waste from the hopper 12 that stores the organic waste through the raw material supply path 12a.
The carbonization furnace 20 supplies carbide generated by partial combustion of organic waste to the pyrolysis furnace 30 via the carbide supply path 101. Moreover, the carbonization furnace 20 supplies the combustion gas produced | generated by the partial combustion of the organic waste to the thermal decomposition furnace 30 via the combustion gas flow path 200a.

  In addition, you may supply the whole quantity of the carbide | carbonized_material manufactured in the carbonization furnace 20 to the thermal decomposition furnace 30, and collect | recover part of the carbide | carbonized_material manufactured in the carbonization furnace 20 with a collection device (illustration omitted). Also good. When a part of the carbide is recovered by the recovery device, the carbide itself can be obtained as a product of the water gas generation system 100.

  The thermal decomposition furnace 30 is an apparatus that generates water gas by heating the carbide generated by the carbonization furnace 20 with combustion gas together with superheated steam to cause a thermal decomposition reaction. The pyrolysis furnace 30 is supplied with the carbide generated by the carbonization furnace 20 through the carbide supply path 101. The pyrolysis furnace 30 is supplied with superheated steam generated by the steam superheater 81 as a gasifying agent. The pyrolysis furnace 30 is supplied with combustion gas from the combustion gas channel 200a as a heat source for promoting the pyrolysis reaction.

The pyrolysis furnace 30 causes a pyrolysis reaction of the carbide and superheated steam to generate a water gas mainly composed of hydrogen gas, carbon monoxide gas, and carbon dioxide gas. The thermal decomposition reaction between carbide and superheated steam is a reaction mainly represented by the following formulas (1) and (2).
C + H ₂ O → CO + H ₂ (1)
CO + H ₂ O → CO ₂ + H ₂ (2)
The water gas reaction shown in Formula (1) is an endothermic reaction, and the water gas shift reaction shown in Formula (2) is an exothermic reaction. The endothermic amount of the endothermic reaction shown in formula (1) is larger than the exothermic amount of the exothermic reaction shown in formula (2). Therefore, the thermal decomposition reaction between the carbide and the superheated steam is an endothermic reaction as a whole.

  The temperature of the carbide supplied to the pyrolysis furnace 30 is adjusted so as to be normal temperature (for example, 25 ° C.) or higher and 350 ° C. or lower. Moreover, the temperature of the superheated steam supplied to the pyrolysis furnace 30 is adjusted to be 730 ° C. or more and 830 ° C. or less. The temperature of the combustion gas supplied to the pyrolysis furnace 30 is adjusted to be 900 ° C. or higher and 1300 ° C. or lower. Moreover, the temperature of the water gas which the pyrolysis furnace 30 produces | generates is adjusted so that it may become 650 degreeC or more and 850 degrees C or less.

  The pyrolysis furnace 30 supplies the water gas generated by the pyrolysis reaction, unreacted carbide and residue to the temperature reducer 40 via the water gas supply path 102. Further, the pyrolysis furnace 30 supplies the combustion gas used as a heat source for the pyrolysis reaction to the steam superheater 81 through the combustion gas channel 200b. The temperature of the combustion gas supplied to the steam superheater 81 is adjusted to be 820 ° C. or more and 920 ° C. or less.

The temperature reducer 40 is a device that lowers the temperature of the water gas supplied from the water gas supply path 102 by spraying liquid water. Water is supplied to the temperature reducer 40 from a water supply device 82 by a water supply pump (not shown). The temperature reducer 40 supplies the temperature-reduced water gas to the cyclone 50 through the water gas supply path 103. The temperature reducer 40 supplies unreacted carbide residues and residues supplied from the water gas supply path 102 to the char recovery device 41.
The temperature reducer 40 adjusts the amount of water sprayed so that the water gas adjusted in the pyrolysis furnace 30 is 650 ° C. or higher and 750 ° C. or lower and the water gas is 220 ° C. or higher and 280 ° C. or lower.

The char recovery device 41 is a device that recovers an unreacted portion of the carbide and supplies it to the pyrolysis furnace 30 again.
By providing the char recovery device 41, it is avoided that unreacted carbide is not used for generating water gas and is discarded. Therefore, by providing the char recovery device 41, the yield of water gas from the carbide is improved.

In FIG. 1, the unreacted carbide recovered by the char recovery device 41 is supplied again to the pyrolysis furnace 30, but the unreacted carbide recovered by the char recovery device 41 is supplied to the pyrolysis furnace 30. You may make it not supply to. In this case, the carbide itself recovered by the char recovery device 41 can be obtained as a product of the water gas generation system 100.
The unreacted carbide recovered by the char recovery device 41 is cleaned by superheated steam (water vapor) in the pyrolysis furnace 30 to remove other components other than the carbon component. Therefore, in the char recovery device 41, it is possible to obtain a carbide having an extremely high carbon content in which other components other than the carbon component are well removed.

  The cyclone 50 is a device that removes carbides and residues contained in the water gas supplied through the water gas supply path 103. The cyclone 50 turns the water gas supplied through the water gas supply path 103 inside to centrifuge the carbide and the residue contained in the water gas, guide them downward, and supply them to the residue collecting device 51. Further, the cyclone 50 guides the water gas from which the carbides and the residue are removed upward and supplies the water gas to the water gas cooling device 60 via the water gas supply path 104. The carbide recovered by the residue recovery device 51 becomes a product of the water gas generation system 100.

  The water gas cooling device 60 is a device that lowers the temperature of the water gas supplied from the water gas supply path 104 by spraying liquid water. The water gas cooling device 60 circulates the cooling water so that the cooling water sprayed in the water gas is recovered and sprayed again into the water gas by a circulation pump (not shown).

  The water gas cooling device 60 supplies the cooled water gas to the water gas holder 70. The water gas cooling device 60 is provided with a temperature sensor (not shown) for detecting the temperature of the water gas supplied to the water gas holder 70 and is circulated by a circulation pump (not shown) so that the detected temperature matches the target temperature. Control the amount of cooling water. The water gas cooling device 60 adjusts the spray amount of water so that the water gas adjusted by the temperature reducer 40 is 220 ° C. or more and 280 ° C. or less, and the water gas is 30 ° C. or more and 50 ° C. or less.

  The water gas holder 70 is a device that stores the water gas supplied from the water gas cooling device 60. The water gas holder 70 can supply the stored water gas individually to the flare stack 71, the power generation facility 72, and the hydrogen purifier 73.

  The flare stack 71 is an apparatus for incineration when excess water gas is generated, such as when the storage amount of the water gas holder 70 becomes excessive. The flare stack 71 is always combusted by a fuel such as liquefied natural gas. Therefore, when water gas is supplied to the flare stack 71, the water gas is incinerated.

  The power generation facility 72 is a facility that obtains a power generation output by driving a generator by operating with water gas as a fuel. As the power source for driving the generator by the power generation facility 72, for example, a gas engine that operates by burning water gas is used.

  The hydrogen purifier 73 is an apparatus that purifies high-purity hydrogen gas (for example, hydrogen gas having a purity of 99.995% or more) by removing components such as carbon monoxide gas and carbon dioxide gas contained in the water gas. is there. The hydrogen purifier 73 is an adsorption tower filled with an adsorbent (suitable for removing components such as carbon monoxide gas and carbon dioxide gas) by pressurizing water gas to a predetermined pressure with a compressor (not shown). (Not shown). The hydrogen purifier 73 opens and closes a valve (not shown) for controlling the conduction with the outside air provided in the adsorption tower and depressurizes the adsorption tower to atmospheric pressure, so that the carbon monoxide gas is removed from the adsorbent. Then, components such as carbon dioxide gas are removed, and high purity hydrogen gas is purified.

  The steam generator 80 is an apparatus that generates saturated steam by evaporating water by heating with combustion gas. Water is supplied to the steam generator 80 from the water supply device 82 via a water supply pump (not shown). Further, the combustion gas discharged from the steam superheater 81 is supplied to the steam generator 80 via the combustion gas flow path 200c. The temperature of the combustion gas supplied to the steam generator 80 is adjusted to be 750 ° C. or higher and 850 ° C. or lower.

  The saturated steam generated by the steam generator 80 is supplied to the steam superheater 81. The combustion gas used as a heat source for vaporizing water in the steam generator 80 is supplied to the dryer 10 through the combustion gas flow path 200d. The temperature of the combustion gas supplied to the dryer 10 is adjusted to be 540 ° C. or higher and 640 ° C. or lower.

The steam superheater 81 is a device that generates superheated steam from saturated steam by heating the saturated steam with combustion gas. The steam superheater 81 is supplied with saturated steam generated by the steam generator 80. Further, the combustion gas discharged from the pyrolysis furnace 30 is supplied to the steam superheater 81 through the combustion gas flow path 200b. The temperature of the combustion gas supplied to the steam superheater 81 is adjusted to be 820 ° C. or more and 920 ° C. or less.
The superheated steam generated by the steam superheater 81 is supplied to the pyrolysis furnace 30 as a gasifying agent. The combustion gas used as a heat source for generating superheated steam in the steam superheater 81 is supplied to the steam generator 80 via the combustion gas flow path 200c.

The control device 90 is a device that controls the water gas generation system 100. The control device 90 can communicate with a control unit (not shown) provided in each unit constituting the water gas generation system 100. The control device 90 can control each unit by transmitting a control command to a control unit included in each unit constituting the water gas generation system 100. In addition, the control device 90 can receive a signal indicating the state of each part such as temperature and pressure from each part constituting the water gas generation system 100.
The control device 90 can cause each unit constituting the water gas generation system 100 to perform a desired operation by reading and executing a control program stored in a storage unit (not shown).

In the water gas generation system 100 shown in FIG. 1, the combustion gas generated in the carbonization furnace 20 is circulated as follows through the combustion gas flow path including the combustion gas flow paths 200a, 200b, 200c, 200d, and 200e.
First, the combustion gas generated by the carbonization furnace 20 is supplied to the pyrolysis furnace 30 through the combustion gas flow path 200a.
Secondly, the combustion gas discharged from the pyrolysis furnace 30 is supplied to the steam superheater 81 through the combustion gas channel 200b.
Third, the combustion gas discharged from the steam superheater 81 is supplied to the steam generator 80 through the combustion gas flow path 200c.
Fourth, the combustion gas discharged from the steam generator 80 is supplied to the dryer 10 through the combustion gas channel 200d.
Fifthly, the combustion gas discharged from the dryer 10 is supplied to the exhaust gas cooling and cleaning device 13 through the combustion gas channel 200e.
Sixth, the combustion gas detoxified by the exhaust gas cooling and cleaning device 13 is discharged into the atmosphere by the exhaust gas cooling and cleaning device 13.

  Here, the combustion gas generated by the carbonization furnace 20 is supplied to the pyrolysis furnace 30 without performing heat exchange with other heat medium. The reason is that the combustion gas maintained at a high temperature is used for the pyrolysis furnace. This is because the thermal decomposition reaction at 30 is promoted to improve the yield of water gas from the carbide. Compared to the case where the combustion gas generated by the carbonization furnace 20 is supplied to the pyrolysis furnace 30 after heat exchange with another heat medium, the inside of the pyrolysis furnace 30 can be maintained at a high temperature. The reaction is accelerated and the yield of water gas from the carbide is improved.

Next, the carbonization furnace 20 of this embodiment will be described in detail.
FIG. 2 is a longitudinal sectional view of the carbonization furnace 20 shown in FIG. In FIG. 2, the axis X indicates the vertical direction (gravity direction) orthogonal to the installation surface (not shown) on which the carbonization furnace 20 is installed.

  As shown in FIG. 2, the carbonization furnace 20 of the present embodiment includes a main body part 21, a cylindrical part 22, an organic waste input part 23, a carbide discharge part 24, a primary air supply part 25, and a secondary part. Air supply unit 26, combustion gas discharge unit 27, temperature sensor 28a, temperature sensor 28b (first temperature detection unit), temperature sensor 28c (second temperature detection unit), level sensor 28d (deposition amount detection unit) ), An ignition burner 20c, and a carbonization furnace control unit 29 (control unit).

The main body 21 is a member that is formed in a substantially cylindrical shape that extends along the axis X and that is an exterior of the carbonization furnace 20. The main body 21 forms a primary combustion region R2 in which organic waste is partially combusted and a secondary combustion region R4 in which combustible gas contained in the combustion gas generated from the organic waste is combusted. Yes.
The main body 21 is attached to a metal (for example, iron) housing 21a that forms the exterior of the carbonization furnace 20, a heat insulating material 21b that is attached to the inner peripheral surface of the housing 21a, and an inner peripheral surface of the heat insulating material 21b. Refractory material 21c.

The cylindrical portion 22 is a member formed in a substantially cylindrical shape extending along the axis X. The cylindrical portion 22 has an outer peripheral surface 22a that forms a gap 20a for combusting organic waste to generate carbides with the inner peripheral surface 21d of the main body portion 21. Since the cylindrical part 22 becomes high temperature by combustion of organic waste, it is preferable to form the cylindrical part 22 from a heat-resistant material (for example, a metal material such as stainless steel).
As shown in FIG. 2, the inside of the cylindrical portion 22 is a hollow closed space, and this closed space is not in communication with other spaces. For this reason, the cylindrical portion 22 can store a certain amount of heat, and is not easily affected by an external temperature change.

  The cylindrical portion 22 is attached to the turntable 24a shown in FIG. 3, and rotates around the axis X in response to the turntable 24a rotating around the axis X. As the cylindrical portion 22 rotates about the axis X, the gap 20a and the organic waste existing above the gap 20a are guided along the gap 20a from above to below.

The organic waste supplied to the gap 20a is partially combusted by the primary combustion air supplied from the primary air supply unit 25 in the primary combustion region R2, and burns containing solids containing a large amount of carbides and combustible gas. Gas is generated. The solid content containing a large amount of carbide is guided to the lower carbide refining / cooling region R1 along the gap 20a, and the combustion gas containing combustible gas is guided to the secondary combustion region R4.
The carbide refining / cooling region R <b> 1 is a region where the upper side is closed with organic waste and the primary combustion air from the primary air supply unit 25 is not supplied. Therefore, the carbide is refined while being cooled in the carbide refinement / cooling region R1.

  The organic waste input part 23 is provided in the main body part 21 and is provided with an opening and an opening part for supplying organic waste (not shown) supplied from the hopper 12 through the raw material supply path 12a into the main body part 21. A transport unit (not shown) for transporting organic waste. An inclined surface 23a is formed below the organic waste throwing portion 23. The inclined surface 23a is inclined downward from above as it approaches the axis X. The input amount of the organic waste that the organic waste input unit 23 inputs into the opening is adjusted by the control device 90 controlling the transport speed of the transport unit. The organic waste supplied from the organic waste input part 23 is guided to the upper surface 22b of the cylindrical part 22 and the gap 20a along the inclined surface 23a.

  As shown in FIG. 2, the region where the organic waste charging unit 23 is disposed is a raw material charging region R3. In the raw material charging region R3, an inspection window 20b is provided on the side opposite to the organic waste charging unit 23 with respect to the axis X. The inspection window 20b makes the inside of the carbonization furnace 20 visible.

The carbide discharge unit 24 is a mechanism for discharging carbide generated by partial combustion of organic waste in the gap 20 a to the carbide supply path 101. The carbide discharged from the carbide discharge unit 24 to the carbide supply path 101 is supplied to the pyrolysis furnace 30.
As shown in FIGS. 2 and 3, the carbide discharge unit 24 includes a turntable 24a (rotating body), a drive unit 24b, and a carbide discharge port 24c.

As shown in FIG. 3, the turntable 24 a is a member provided at a position facing the lower end of the gap 20 a in the axis X direction, and is an annular rotator extending in the circumferential direction around the axis X. The turntable 24a rotates around the axis X by the driving force transmitted from the driving unit 24b.
As shown in FIG. 3, the surface of the turntable 24 a that faces the lower end of the gap 20 a is an inclined surface that is inclined downward as the distance from the axis X increases. Therefore, a gap is formed between the lower end of the gap 20a and the inclined surface of the turntable 24a.

  Carbide (not shown) existing at the lower end of the gap 20a moves downward along the inclined surface of the turntable 24a as the turntable 24a rotates about the axis X, and is guided to the carbide discharge port 24c. . Therefore, the amount of carbide discharged from the lower end of the gap 20a to the carbide discharge port 24c increases as the rotational speed of the turntable 24a increases. Similarly, as the rotational speed of the turntable 24a decreases, the amount of carbide discharged from the lower end of the gap 20a to the carbide outlet 24c decreases.

  The driving unit 24b is a device that transmits driving force to the turntable 24a and rotates the turntable 24a around the axis X. As shown in FIG. 2, the drive unit 24b includes a drive motor 24e, a speed reducer 24f, a drive belt 24g, and a drive shaft 24h.

The drive motor 24 e is an inverter motor whose rotation speed is controlled by a control signal transmitted from the carbonization furnace control unit 29. The rotational power of the drive motor 24e is transmitted to the speed reducer 24f by the drive belt 24g.
The speed reducer 24f is a device that increases the torque while reducing the rotational speed of the rotational power transmitted from the drive motor 24e by the drive belt 24g. The speed reducer 24f transmits the rotational power with increased torque to the drive shaft 24h extending around the axis X.
The turntable 24a is connected to the drive shaft 24h. Therefore, the turntable 24a rotates about the axis X as the drive shaft 24h rotates about the axis X.

  The carbide discharge port 24 c is an opening through which the carbide is discharged to the carbide supply path 101. The carbide discharged from the carbide discharge port 24 c to the carbide supply path 101 is supplied to the pyrolysis furnace 30 through the carbide supply path 101.

  The clinker crusher 24d is a member for crushing a clinker that is a lump larger than a gap formed between the lower end of the gap 20a and the inclined surface of the turntable 24a. Here, the clinker is obtained by melting the combustion ash generated by the combustion of the organic waste in the primary combustion region R2 into a lump.

  As shown in FIG. 3, the clinker crusher 24d is attached to the main body portion 21 by fastening bolts. The clinker crusher 24d remains fixed to the main body 21 even when the turntable 24a rotates about the axis X. Therefore, when the clinker moves as the turntable 24a rotates, the clinker collides with the clinker crusher 24d and is crushed.

Next, the primary air supply unit 25 will be described.
The primary air supply unit 25 is a device that supplies primary combustion air that partially burns organic waste toward the organic waste accumulated in the gap 20a. As shown in FIG. 2, the primary air supply unit 25 includes a primary combustion fan 25a (blower unit), a cover unit 25b, and an air supply port 25c.

  The primary combustion fan 25a is a device that blows air (atmosphere) introduced from the outside, and includes an inverter motor (not shown) and a fan (not shown) driven by the inverter motor. The primary combustion fan 25a can adjust the air volume to blow by controlling the rotation speed of the inverter motor.

The cover portion 25b is a member that forms a closed space 25d that introduces air blown from the primary combustion fan 25a and supplies air to the air supply port 25c.
As shown in FIG. 4A (end view taken along the line AA of the carbonization furnace 20 shown in FIG. 2), the cover portion 25 b is a closed space extending around the axis X between the outer peripheral surface 21 e of the main body portion 21. 25d is formed.

The air supply port 25c is a flow path for supplying air blown from the primary combustion fan 25a to the closed space 25d to the primary combustion region R2 inside the main body 21 from the closed space 25d.
As shown in FIG. 2, the air supply ports 25 c are provided at a plurality of locations in the vertical direction along the axis X in the primary combustion region R <b> 2 where the organic waste is partially combusted with the primary combustion air.

Further, as shown in FIG. 4A, the air supply ports 25c are provided in the main body 21 at equal intervals along the circumferential direction around the axis X (30 ° intervals in FIG. 4A). As shown in FIG. 4A, the air supply port 25 c is a linear flow path extending from the outer peripheral surface 21 e of the main body 21 toward the axis X.
In the example shown in FIG. 4A, the air supply ports 25c are arranged at intervals of 30 ° along the circumferential direction around the axis X. However, as other intervals (for example, 20 °, 45 °, etc.) Alternatively, they may be arranged at arbitrary intervals instead of at equal intervals.

  The primary air supply unit 25 shown in FIG. 2 has a heating unit (not shown) that heats the air blown from the primary combustion fan 25a. The air supply port 25c supplies the air heated by the heating unit to the air supply port 25c. Therefore, compared with the case where the air blown from the primary combustion fan 25a is not heated, the atmospheric temperature of the primary combustion region R2 can be maintained at a high temperature.

Next, the secondary air supply unit 26 will be described.
The secondary air supply unit 26 is a device that supplies secondary combustion air for burning the combustible gas contained in the combustion gas generated by the combustion of the organic waste in the primary combustion region R2 to the inside of the main body 21. is there. As shown in FIG. 2, the secondary air supply unit 26 is provided in the secondary combustion region R4, and supplies secondary combustion air toward the secondary combustion region R4. The secondary air supply unit 26 includes a secondary combustion fan 26a, a cover unit 26b, and an air supply port 26c.

  The secondary combustion fan 26a is a device that blows air (atmosphere) introduced from the outside, and includes an inverter motor (not shown) and a fan (not shown) driven by the inverter motor. The secondary combustion fan 26a can adjust the air volume to blow by controlling the rotation speed of the inverter motor.

The cover portion 26b is a member that forms a closed space 26d that introduces air blown from the secondary combustion fan 26a and supplies air to the air supply port 26c.
As shown in FIG. 4B (end view taken along the line B-B of the carbonization furnace 20 shown in FIG. 2), the cover portion 26 b is a closed space extending around the axis X between the outer peripheral surface 21 e of the main body portion 21. 26d is formed.

The air supply port 26c is a flow path for supplying air blown from the secondary combustion fan 26a to the closed space 26d to the secondary combustion region R4 inside the main body 21 from the closed space 26d.
As shown in FIG. 2, the air supply ports 26 c are provided at a plurality of locations in the vertical direction along the axis X in the secondary combustion region R <b> 4 where the combustible gas contained in the combustion gas is combusted by the secondary combustion air. ing.

Further, as shown in FIG. 4B, the air supply ports 26c are provided in the main body 21 at equal intervals along the circumferential direction around the axis X (30 ° intervals in FIG. 4B). As shown in FIG. 4B, the air supply port 26c is a linear flow path extending from the outer peripheral surface 21e of the main body 21 toward the axis X.
In the example shown in FIG. 4B, the air supply ports 26c are arranged at intervals of 30 ° along the circumferential direction around the axis X. However, as other intervals (for example, 20 °, 45 °, etc.) Alternatively, they may be arranged at arbitrary intervals instead of at equal intervals.

  The combustion gas discharge unit 27 is an exhaust port that discharges the combustion gas generated in the primary combustion region R2 and combusted with the combustible gas component in the secondary combustion region R4 to the combustion gas channel 200a. The combustion gas discharged to the combustion gas flow path 200a is supplied to the pyrolysis furnace 30 for use as a heat source for the pyrolysis reaction.

The temperature sensor 28 a is a sensor that detects the temperature of the combustion gas discharged from the combustion gas discharge unit 27. The temperature sensor 28 a transmits a temperature detection signal indicating the detected temperature to the carbonization furnace control unit 29.
As shown in FIG. 2, the temperature sensor 28a is arranged in a region close to the combustion gas flow path 200a in the secondary combustion region R4. Therefore, the combustion gas temperature Tg detected by the temperature sensor 28a is substantially the same as the temperature of the combustion gas discharged to the combustion gas flow path 200a.

The temperature sensor 28b is a sensor that detects the ambient temperature of the primary combustion region R2. The temperature sensor 28 b transmits a temperature detection signal indicating the detected temperature to the carbonization furnace control unit 29.
The temperature sensor 28c is a sensor that detects a carbide temperature Tc that is a temperature of carbide deposited on the lower end side of the gap 20a. The temperature sensor 28 b transmits a temperature detection signal indicating the detected carbide temperature Tc to the carbonization furnace control unit 29.

The level sensor 28d is a sensor that detects the amount of organic waste deposited in the gap 20a. In the primary combustion region R2, the level sensor 28d detects the amount of organic waste accumulated in the direction of the axis Y shown in FIG. 1 by obtaining an output signal corresponding to the amount of accumulation.
The level sensor 28d may be a reflective sensor that detects the amount of deposition by receiving reflection of emitted light, ultrasonic waves, or the like. Further, the level sensor 28d may be a transmission type sensor in which a receiving part for receiving emitted X-rays or the like is provided in the cylindrical part 22.

  As will be described later, the level sensor 28d detects that the amount of organic waste deposited in the gap 20a has decreased, such as when the introduction of new organic waste from the organic waste input unit 23 is stopped. Sensor. Therefore, the level sensor 28d detects the amount of deposition along the axis Y directed downward from the mounting position in the vertical direction. When the carbonization furnace control unit 29 outputs a detection signal indicating that the deposition amount Ao, which is the deposition amount of organic waste detected by the level sensor 28d, is 0, the deposition amount of the organic waste present in the gap 20a is predetermined. It is determined that the first deposition amount Ao1 has decreased.

  The ignition burner 20c is a device used to ignite organic waste when starting combustion of organic waste in the carbonization furnace 20. As shown in FIG. 2, the ignition burner 20c is provided on the lower end side of the gap 20a. In addition, as shown in FIG. 2, the ignition burners 20 c are arranged at two locations facing the axis X.

  The ignition burner 20c burns organic waste accumulated on the lower end side of the gap 20a by generating a flame using ignition fuel such as kerosene. The ignition burner 20c generates a flame when starting combustion of organic waste in the carbonization furnace 20 in accordance with a control command from the carbonization furnace control unit 29. Further, the ignition burner 20c stops the generation of flame at a predetermined timing in accordance with a control command from the carbonization furnace control unit 29.

  The carbonization furnace control unit 29 is a device that controls each part by receiving a detection signal indicating the state of each part from each part of the carbonization furnace 20 and transmitting a control signal to each part based on the detection signal. The carbonization furnace control unit 29 is a device that transmits a signal indicating the state of the carbonization furnace 20 to the control device 90 and controls the carbonization furnace 20 in response to a control signal transmitted from the control device 90.

  The carbonization furnace control unit 29 receives a temperature detection signal indicating the temperature detected by each of the temperature sensors 28a, 28b, and 28c, and a deposition amount detection signal indicating the deposition amount Ao of the organic waste detected by the level sensor 28d. . Further, the carbonization furnace control unit 29 transmits a control signal for controlling the blown amount of the primary combustion fan 25 a to the primary air supply unit 25. Further, the carbonization furnace control unit 29 transmits a control signal for controlling the blown amount of the secondary combustion fan 26 a to the secondary air supply unit 26. The carbonization furnace control unit 29 transmits a control signal to the ignition burner 20c to generate a flame when starting combustion of organic waste, and transmits a control signal at a predetermined timing to stop the generation of the flame. . Moreover, the carbonization furnace control unit 29 transmits a control signal for controlling the rotation speed of the turntable 24a to the drive motor 24e.

Next, a method for controlling the blown amount of the primary combustion fan 25a by the carbonization furnace control unit 29 will be described with reference to the flowchart of FIG.
The carbonization furnace control unit 29 controls the amount of air blown by the primary combustion fan 25a based on the atmospheric temperature of the primary combustion region R2 detected by the temperature sensor 28b. The amount of air blown by the primary combustion fan 25a coincides with the amount of primary combustion air supplied from the air supply port 25c to the primary combustion region R2 of the carbonization furnace 20. Therefore, the carbonization furnace control unit 29 can adjust the amount of primary combustion air blown to the primary combustion region R2 by controlling the amount of air blown by the primary combustion fan 25a. .

  The carbonization furnace control unit 29 performs primary combustion based on the atmospheric temperature in the primary combustion region R2 detected by the temperature sensor 28b so that the combustion state suitable for carbonizing the organic waste accumulated in the gap 20a is maintained. The amount of air blown by the fan 25a is controlled. Specifically, the carbonization furnace control unit 29 controls the amount of air blown by the primary combustion fan 25a so that the atmospheric temperature of the primary combustion region R2 is in the range of 900 ° C. or higher and 1200 ° C. or lower.

In the carbonization furnace 20 of the present embodiment, the carbonization furnace control unit 29 controls the amount of air blown from the primary combustion fan 25a so that the atmospheric temperature Ta in the primary combustion region R2 falls within the range of 900 ° C. or more and 1200 ° C. or less. Thus, the carbonization state of the organic substance is controlled so that the organic waste deposited on the upper layer side of the carbide scouring / cooling region R1 is maintained in a temperature range (predetermined temperature range) of 900 ° C. or higher and 1200 ° C. or lower. Below, 900 degreeC which is the minimum of the atmospheric temperature Ta of the primary combustion area | region R2 controlled by the carbonization furnace control part 29 is made into 1st atmospheric temperature Ta1, and 1200 degreeC which is the upper limit of the atmospheric temperature Ta of primary combustion area | region R2 Is the second ambient temperature Ta2.
Each process in the flowchart shown in FIG. 5 is a process performed when a calculation unit (not shown) included in the carbonization furnace control unit 29 executes a control program stored in a storage unit (not shown).

  Prior to the processing shown in the flowchart of FIG. 5, when the carbonization furnace control unit 29 starts combustion of the organic waste in the carbonization furnace 20, the organic waste is generated by the ignition burner 20 c and accumulated in the gap 20 a. Start burning. Thereafter, the carbonization furnace control unit 29 starts blowing external air (atmosphere) by the primary combustion fan 25a. The carbonization furnace control unit 29 controls the primary combustion fan 25a so that the air flow rate is constant until the atmospheric temperature Ta in the primary combustion region R2 detected by the temperature sensor 28b becomes equal to or higher than the first atmospheric temperature Ta1. After the atmospheric temperature Ta detected by the temperature sensor 28b becomes equal to or higher than the first atmospheric temperature Ta1, the processes shown in the flowchart of FIG. 5 are started.

  Note that the amount of primary combustion air blown by the primary combustion fan 25a until the ambient temperature Ta becomes equal to or higher than the first ambient temperature Ta1 completely burns the organic waste charged into the primary combustion region R2. It is the amount obtained by subtracting a certain amount from the amount necessary for this. This is to prevent the carbon yield (ratio of the weight of the organic waste to be charged and the weight of the carbon component contained in the resulting carbide) from being excessively combusted to reduce the carbon yield. is there.

In step S500, the carbonization furnace control unit 29 detects the ambient temperature Ta of the primary combustion region R2 by receiving the temperature detection signal transmitted from the temperature sensor 28b.
In step S501, the carbonization furnace control unit 29 determines whether or not the ambient temperature Ta detected by the temperature sensor 28b is lower than the first ambient temperature Ta1. When determining that the atmospheric temperature Ta is lower than the first atmospheric temperature Ta1, the carbonization furnace control unit 29 proceeds to step 502, and otherwise proceeds to step S503.

  In step S502, the carbonization furnace control unit 29 transmits a control signal for increasing the blowing amount of the primary combustion fan 25a to the primary combustion fan 25a. The primary combustion fan 25a increases the blown air volume in response to receiving the control signal from the carbonization furnace control unit 29. The carbonization furnace control unit 29 increases the amount of oxygen for burning the organic waste by increasing the amount of air blown from the primary combustion fan 25a, thereby raising the ambient temperature Ta.

  In step S503, the carbonization furnace control unit 29 determines whether or not the ambient temperature Ta detected by the temperature sensor 28b is higher than the second ambient temperature Ta2. When determining that the detected atmospheric temperature Ta is higher than the second atmospheric temperature Ta2, the carbonization furnace control unit 29 advances the process to step S504, and otherwise advances the process to step S501.

In step S504, the carbonization furnace control unit 29 transmits a control signal for reducing the blown amount of the primary combustion fan 25a to the primary combustion fan 25a. The primary combustion fan 25a reduces the blown air volume in response to receiving the control signal from the carbonization furnace control unit 29. The carbonization furnace control unit 29 reduces the amount of candy oxygen that burns organic waste by reducing the amount of air blown from the primary combustion fan 25a, thereby lowering the ambient temperature Ta.
When the process of the flowchart shown in FIG. 5 is completed, the carbonization furnace control unit 29 starts executing the process shown in FIG. 5 again.

  Thus, the carbonization furnace control unit 29 performs primary operation so that the atmospheric temperature Ta in the primary combustion region R2 is within the range of the first atmospheric temperature Ta1 (900 ° C.) or higher and the second atmospheric temperature Ta2 (1200 ° C.) or lower. The amount of air blown from the combustion fan 25a is controlled. Thereby, the carbonization furnace control unit 29 carbonizes the organic matter so that the organic waste deposited on the upper layer side of the carbide scouring / cooling region R1 is maintained in a temperature range (predetermined temperature range) of 900 ° C. or more and 1200 ° C. or less. Control the state.

  The carbonization furnace control unit 29 of the present embodiment repeatedly executes the process shown in FIG. 5 with a control period of 3 seconds so that the difference in the ambient temperature Ta detected in the continuous control period does not exceed 25 ° C. Can be controlled. The water gas generation system 100 of the present embodiment automatically controls the atmospheric temperature Ta by the carbonization furnace control unit 29, so that the organic waste deposited in the gap 20a is in a temperature range of 900 ° C. or higher and 1200 ° C. or lower (predetermined) Temperature range).

Next, a method for controlling the blowing amount of the secondary combustion fan 26a by the carbonization furnace control unit 29 will be described with reference to the flowchart of FIG.
The carbonization furnace control unit 29 controls the amount of air blown by the secondary combustion fan 26a based on the combustion gas temperature Tg detected by the temperature sensor 28a. The amount of air blown by the secondary combustion fan 26a matches the amount of air for secondary combustion supplied to the secondary combustion region R4 of the carbonization furnace 20 from the air supply port 26c. Therefore, the carbonization furnace control unit 29 can adjust the amount of secondary combustion air blown to the secondary combustion region R4 by controlling the amount of air blown by the secondary combustion fan 26a. .

Based on the combustion gas temperature Tg detected by the temperature sensor 28a so that the combustion state suitable for burning the combustible gas contained in the combustion gas in the secondary combustion region R4 is maintained. The amount of air blown by the next combustion fan 26a is controlled. Specifically, the carbonization furnace control unit 29 controls the amount of air blown by the secondary combustion fan 26a according to the flowchart shown in FIG.
Each process in the flowchart shown in FIG. 6 is a process performed when a calculation unit (not shown) included in the carbonization furnace control unit 29 executes a control program stored in a storage unit (not shown).

  Prior to the processing shown in the flowchart of FIG. 6, when the carbonization furnace control unit 29 starts combustion of the organic waste in the carbonization furnace 20, the organic waste is generated by the ignition burner 20 c and accumulated in the gap 20 a. Start burning. Thereafter, the carbonization furnace control unit 29 starts blowing external air (atmosphere) by the secondary combustion fan 26a. The carbonization furnace control unit 29 controls the secondary combustion fan 26a so that the air flow rate is constant until the combustion gas temperature Tg detected by the temperature sensor 28a becomes equal to or higher than the first combustion gas temperature Tg1. Each process shown in the flowchart of FIG. 6 is started after the combustion gas temperature Tg detected by the temperature sensor 28a becomes equal to or higher than the first combustion gas temperature Tg1.

  The amount of secondary combustion air blown by the secondary combustion fan 26a before the combustion gas temperature Tg becomes equal to or higher than the first combustion gas temperature Tg1 is assumed to exist in the secondary combustion region R4. It is an amount obtained by adding a certain surplus amount to the amount necessary to completely burn the fuel.

  In step S600, the carbonization furnace control unit 29 receives the temperature detection signal transmitted from the temperature sensor 28a, thereby detecting the combustion gas temperature Tg that is the temperature of the combustion gas discharged from the combustion gas discharge unit 27.

  In step S601, the carbonization furnace control unit 29 determines whether or not the combustion gas temperature Tg detected by the temperature sensor 28a is lower than the first combustion gas temperature Tg1. When determining that the combustion gas temperature Tg is lower than the first combustion gas temperature Tg1, the carbonization furnace control unit 29 advances the process to step S602, and if not, advances the process to step S603.

In step S602, the carbonization furnace control unit 29 transmits a control signal for reducing the blown amount of the secondary combustion fan 26a to the secondary combustion fan 26a. The secondary combustion fan 26a reduces the blown air volume in response to receiving the control signal from the carbonization furnace control unit 29.
Here, when it is determined that the combustion gas temperature Tg is lower than the first combustion gas temperature Tg1, the blowing amount of the secondary combustion fan 26a is decreased for the following reason.

  The amount of secondary combustion air that the secondary air supply unit 26 supplies to the secondary combustion region R4 is a fixed amount rather than the amount that causes complete combustion of the combustible gas contained in the combustion gas present in the secondary combustion region R4. A large amount is preferable. That is, the excess air ratio in the secondary combustion region R4 is preferably set to a constant value larger than 1.0.

  However, the amount of combustible gas present in the secondary combustion region R4 generally varies depending on factors such as the properties of the organic waste and the combustion state of the organic waste in the primary combustion region R2. Therefore, if the amount of secondary combustion air supplied from the secondary air supply unit 26 to the secondary combustion region R4 is kept constant, an air amount suitable for complete combustion of the combustible gas cannot be maintained.

  When the amount of secondary combustion air is excessively large relative to the amount of complete combustion of the combustible gas, a large amount of surplus air that is not used for combusting the combustible gas is supplied to the secondary combustion region R4. It will be. Since the temperature of the air (atmosphere) blown by the secondary combustion fan 26a is lower than the atmospheric temperature in the secondary combustion region R4, the atmospheric temperature in the secondary combustion region R4 is lowered by a large amount of excess air.

If it does so, the combustion efficiency of the combustible gas in secondary combustion area | region R4 will deteriorate, and the combustion gas which contains much combustible gas will be discharged | emitted from the combustion gas discharge part 27. FIG. The combustible gas contains polymer hydrocarbons which are components that solidify to become tar. Therefore, if a large amount of components that solidify into combustible gas and become tar is contained, the carbonization furnace 20 and equipment installed downstream thereof may be damaged. For this reason, it is desirable that a large amount of components that solidify into the combustion gas and become tar are not included, and damage to the carbonization furnace 20 and equipment installed downstream thereof is desirably suppressed.
Therefore, when the carbonization furnace control unit 29 determines that the combustion gas temperature Tg is lower than the first combustion gas temperature Tg1, the secondary combustion is performed in order to reduce the amount of surplus air supplied to the secondary combustion region R4. The air volume of the fan 26a is reduced.

  In step S603, the carbonization furnace control unit 29 determines whether or not the combustion gas temperature Tg detected by the temperature sensor 28a is higher than the second combustion gas temperature Tg2. The carbonization furnace control unit 29 proceeds to step S604 if it is determined that the detected combustion gas temperature Tg is higher than the second combustion gas temperature Tg2, and otherwise proceeds to step S601.

In step S604, the carbonization furnace control unit 29 transmits a control signal for increasing the blowing amount of the secondary combustion fan 26a to the secondary combustion fan 26a. The secondary combustion fan 26a increases the blown air volume in response to receiving the control signal from the carbonization furnace control unit 29.
When the process of the flowchart shown in FIG. 6 is completed, the carbonization furnace control unit 29 starts executing the process shown in FIG. 6 again.
Here, when it is determined that the combustion gas temperature Tg is higher than the second combustion gas temperature Tg2, the blowing amount of the secondary combustion fan 26a is increased for the following reason.

  When operating the carbonization furnace 20 without setting an upper limit on the combustion gas temperature Tg, the assumed maximum combustion gas temperature is assumed, and the carbonization furnace 20 and the combustion are maintained so that sufficient heat resistance is maintained even at the combustion gas temperature. It is necessary to design the gas flow path 200a. In this case, it is necessary to manufacture the carbonization furnace 20 or the like using an expensive member having high heat resistance, and the manufacturing cost of the carbonization furnace 20 or the like increases. In order not to increase the manufacturing cost of the carbonization furnace 20 or the like, it is preferable that the combustion gas temperature Tg be equal to or lower than a predetermined upper limit temperature.

  Therefore, the carbonization furnace control unit 29 increases the blowing amount of the secondary combustion fan 26a when it is determined that the combustion gas temperature Tg is higher than the second combustion gas temperature Tg2. As described above, when a large amount of surplus air is supplied to the secondary combustion region R4 by increasing the amount of air blown from the secondary combustion fan 26a, the atmospheric temperature in the secondary combustion region R4 is lowered.

As described above, the carbonization furnace control unit 29 controls the amount of air blown by the secondary combustion fan 26a based on the combustion gas temperature Tg detected by the temperature sensor 28a, so that the combustion gas temperature Tg is the first. It is made to become more than combustion gas temperature Tg1 and below 2nd combustion gas temperature Tg2.
Here, as the first combustion gas temperature Tg1 and the second combustion gas temperature Tg2, for example, the first combustion gas temperature Tg1 can be set to 900 ° C., and the second combustion gas temperature Tg2 can be set to 1300 ° C.

  The reason why the first combustion gas temperature Tg1 is set to 900 ° C. is that most of the polymer hydrocarbons can be removed from the combustion gas by maintaining the temperature of the secondary combustion region R4 at 900 ° C. or higher. . The polymer hydrocarbon is a component that solidifies into a tar in the combustible gas contained in the combustion gas. Therefore, by removing most of the polymer hydrocarbon from the combustion gas, damage to the carbonization furnace 20 and equipment installed downstream thereof can be suppressed.

Further, as the first combustion gas temperature Tg1 and the second combustion gas temperature Tg2, for example, the first combustion gas temperature Tg1 may be set to 1000 ° C., and the second combustion gas temperature Tg2 may be set to 1200 ° C.
Further, for example, both the first combustion gas temperature Tg1 and the second combustion gas temperature Tg2 may be set to 1100 ° C. In this case, the carbonization furnace control unit 29 decreases the blowing amount when the combustion gas temperature Tg is lower than the first combustion gas temperature Tg1, and increases the blowing amount when the combustion gas temperature Tg is higher than the second combustion gas temperature Tg2. The secondary combustion fan 26a is controlled so as to cause this to occur.

Next, a method for controlling the rotational speed of the turntable 24a by the carbonization furnace control unit 29 will be described with reference to the flowchart of FIG.
Each process in the flowchart shown in FIG. 7 is a process performed when a calculation unit (not shown) included in the carbonization furnace control unit 29 executes a control program stored in a storage unit (not shown).

  In the flowchart shown in FIG. 7, the carbonization furnace control unit 29 controls the discharge amount of the carbide discharged by the carbide discharge unit 24. In the present embodiment, the amount of carbide discharged by the carbide discharge unit 24 is controlled so that the organic waste input from the organic waste input unit 23 accumulates in the gap 20a over a predetermined time. This is because other components other than the carbon component contained in the organic waste are sufficiently removed by thermal decomposition by heating or the like. If the time for which the organic waste is deposited in the gap 20a is short, other components other than the carbon component cannot be sufficiently removed, and the resulting carbide content is reduced.

In addition, if the time for which the organic waste is accumulated in the gap 20a is long, a part of the carbon component is completely burned, and the carbon yield of the carbide obtained from the organic waste as a raw material is lowered. The predetermined time for depositing the organic waste in the gap 20a varies depending on the type and state of the organic waste, the environmental temperature of the carbonization furnace 20, and the like. For example, the predetermined time is 30 minutes or more and 50 minutes or less. Is preferred. More preferably, it is an arbitrary time of 35 minutes or more and 45 minutes or less.
The amount of carbide discharged by the carbide discharge unit 24 is controlled from the carbide discharge unit 24 as the organic waste input from the organic waste input unit 23 to the gap 20a is stopped. This is to prevent the temperature of the discharged carbide from rising.

When the amount of organic waste deposited in the gap 20a is gradually reduced, the carbide refining / cooling region R1 for extinguishing the carbide gradually becomes narrower. In this case, if the rotation speed of the turntable 24a is maintained constant, the carbide is discharged from the lower end of the gap 20a in a state where the carbide is not sufficiently cooled. This is because the carbide that has been carbonized in the primary combustion region R2 to a high temperature is not sufficiently cooled in the carbide refining / cooling region R1.
Then, the carbonization furnace control part 29 adjusts the temperature of the carbide | carbonized_material which the carbide | carbonized_material discharge part 24 discharge | emits by controlling the discharge | emission amount of the carbide | carbonized_material which the carbide | carbonized_material discharge part 24 discharge | emits.

In the present embodiment, the carbonization furnace control unit 29 adjusts the temperature of the carbide discharged by the carbide discharge unit 24 using both the temperature sensor 28c and the level sensor 28d. The former is a sensor that directly detects the temperature of the carbide, and the latter is a sensor that indirectly detects a state in which the temperature of the carbide is high from the amount of deposited carbide.
Hereinafter, each step of the flowchart of FIG. 7 will be described.

In step S700, the carbonization furnace control unit 29 receives the temperature detection signal transmitted from the temperature sensor 28c, thereby detecting the carbide temperature Tc, which is the temperature of the carbide deposited on the lower end side of the gap 20a.
In step S701, the carbonization furnace control unit 29 receives the accumulation amount detection signal transmitted from the level sensor 28d, thereby detecting the accumulation amount Ao that is the accumulation amount of the organic waste accumulated in the gap 20a.

In step S702, the carbonization furnace control unit 29 determines whether or not the carbide temperature Tc detected by the temperature sensor 28c is equal to or higher than the first carbide temperature Tc1. When determining that the detected carbide temperature Tc is equal to or higher than the first carbide temperature Tc1, the carbonization furnace control unit 29 advances the process to step S703, and otherwise advances the process to step S704.
Here, as 1st carbide | carbonized_material temperature Tc1, arbitrary temperature of the range of 250 degreeC or more and 300 degrees C or less can be set, for example.

In step S703, the carbonization furnace control unit 29 controls the drive unit 24b to rotate the rotation speed of the turntable 24a at the second rotation speed Rs2. The second rotation speed Rs2 is lower than the first rotation speed Rs1 described later.
Here, the first rotation speed Rs1 is a speed for discharging the amount of carbide necessary for the carbonization furnace 20 to maintain the normal operation state from the carbide discharge portion 24. In step S703, the rotation speed of the turntable 24a is set to the first speed so that the temperature of the carbide discharged by the carbide discharge unit 24 decreases when the carbide temperature Tc detected by the temperature sensor 28c becomes equal to or higher than the first carbide temperature Tc1. The second rotation speed Rs2 is lower than the rotation speed Rs1. By reducing the rotation speed of the turntable 24a, the time for which the carbide stays in the carbide refining / cooling region R1 becomes longer, and accordingly, the temperature of the carbide discharged by the carbide discharge portion 24 decreases.

  In step S704, the carbonization furnace control unit 29 determines whether or not the deposition amount Ao detected by the level sensor 28d is equal to or less than the first deposition amount Ao1. When determining that the detected deposition amount Ao is equal to or less than the first deposition amount Ao1, the carbonization furnace control unit 29 proceeds to step S705, and if not, proceeds to step S706.

  In step S705, the carbonization furnace control unit 29 controls the drive unit 24b to rotate the rotation speed of the turntable 24a at the second rotation speed Rs2. The second rotation speed Rs2 is lower than the first rotation speed Rs1 described later. In step S705, the rotation speed of the turntable 24a is set to the first speed so that the temperature of the carbide discharged by the carbide discharge unit 24 decreases when the accumulation amount Ao detected by the level sensor 28d becomes equal to or less than the first accumulation amount Ao1. The second rotation speed Rs2 is lower than the rotation speed Rs1.

  In step S706, the carbonization furnace control unit 29 controls the drive unit 24b to rotate the rotation speed of the turntable 24a at the first rotation speed Rs1. As described above, the first rotation speed Rs1 is a speed for discharging the amount of carbide necessary for the carbonization furnace 20 to maintain the normal operation state from the carbide discharge section 24. Since the carbide temperature Tc is lower than the first carbide temperature Tc1 and the deposition amount Ao is larger than the first deposition amount Ao1 in step S906, the carbonization furnace control unit 29 has an amount necessary for maintaining the operation state. The drive unit 24b is controlled to discharge the carbide from the carbide discharge unit 24.

  When the process of the flowchart shown in FIG. 7 is completed, the carbonization furnace control unit 29 starts executing the process shown in FIG. 7 again. In this way, the carbonization furnace control unit 29 is configured so that the drive unit 24b rotates the turntable 24a based on the carbide temperature Tc detected by the temperature sensor 28c and the organic waste accumulation amount Ao detected by the level sensor 28d. To control.

In the flowchart shown in FIG. 7 described above, the rotation speed of the turntable 24a is switched in two steps depending on whether or not the carbide temperature Tc detected by the temperature sensor 28c is equal to or higher than the first carbide temperature Tc1. Other embodiments may be used.
For example, the rotational speed of the turntable 24a may be switched in two or more stages according to the carbide temperature Tc. Further, for example, the rotational speed of the turntable 24a may be controlled so as to be a speed inversely proportional to the carbide temperature Tc detected by the temperature sensor 28c without switching the rotational speed of the turntable 24a stepwise.

Further, in the flowchart shown in FIG. 7, the rotational speed of the turntable 24a is switched in two steps depending on whether or not the accumulation amount Ao detected by the level sensor 28d is equal to or greater than the first accumulation amount Ao1. However, other embodiments may be used.
For example, the rotation speed of the turntable 24a may be switched in a plurality of stages of two or more stages according to the accumulation amount Ao. Further, for example, the rotational speed of the turntable 24a may be controlled so as to be a speed proportional to the accumulation amount Ao detected by the level sensor 28d without switching the rotational speed of the turntable 24a stepwise.

In the flowchart shown in FIG. 7, the rotational speed of the turntable 24a is controlled using both the carbide temperature Tc detected by the temperature sensor 28c and the accumulation amount Ao detected by the level sensor 28d. Other embodiments may be used.
For example, the rotational speed of the turntable 24a may be controlled using either the carbide temperature Tc detected by the temperature sensor 28c or the deposition amount Ao detected by the level sensor 28d.

As described above, the carbonization furnace control unit 29 of the present embodiment is such that the carbide temperature Tc detected by the temperature sensor 28c is lower than the first carbide temperature Tc1 (for example, any temperature in the range of 250 ° C. or higher and 300 ° C.). The rotational speed of the turntable 24a is controlled.
Thereby, the organic waste deposited in the temperature range of 900 ° C. or more and 1200 ° C. or less on the upper layer side of the carbide scouring / cooling region R1 by controlling the amount of air blown by the primary combustion fan 25a for a predetermined time (for example, 30 minutes or more) And deposits in the gap 20a over a period of 50 minutes or less, and then is discharged from the carbide discharge portion 24.
In addition, the organic waste having a temperature lower than the first carbide temperature Tc1 at the position of the temperature sensor 28c is gradually cooled in the gap 20a below the temperature sensor 28c, and the carbide discharge section 24 at normal temperature (for example, 25 ° C.). Discharged from.

  The carbonization furnace control unit 29 of the present embodiment repeatedly executes the process shown in FIG. 7 with a control period of 3 seconds so that the difference in the carbide temperature Tc detected in the continuous control period does not exceed 25 ° C. Can be controlled. In the water gas generation system 100 of the present embodiment, by performing automatic control of the carbide temperature Tc by the carbonization furnace control unit 29, the organic waste has a gap 20a over a time period (predetermined time) of 30 minutes to 50 minutes. Can be deposited.

Next, the pyrolysis furnace 30 of this embodiment will be described in detail.
FIG. 8 is a longitudinal sectional view of the pyrolysis furnace 30 shown in FIG. In FIG. 8, the axis Z indicates the vertical direction (gravity direction) orthogonal to the installation surface (not shown) on which the pyrolysis furnace 30 is installed.

  As shown in FIG. 8, the pyrolysis furnace 30 of the present embodiment includes a main body 31, a reaction tube 32, a reaction tube head 33 (supply unit), a water gas outlet nozzle 34 (water gas outlet), Combustion gas supply part 35 (heating gas supply part), combustion gas discharge part 36 (heating gas discharge part), gland packing 37 (first seal part), gland packing 38 (second seal part), And a gland packing 39 (third seal portion).

The main body 31 is a member formed in a substantially cylindrical shape extending along the axis Z. The main body 31 forms a space for accommodating the reaction tube 32 therein.
The main body 31 is attached to a metal (for example, iron) housing 31a that forms the exterior of the pyrolysis furnace 30, a heat insulating material 31b that is attached to the inner peripheral surface of the housing 31a, and an inner peripheral surface of the heat insulating material 31b. And a heat-resistant material 31c.

The upper surface of the substantially cylindrical main body 31 is composed of an upper plate 31d that is annular in plan view, and the bottom surface of the main body 31 is composed of a bottom plate 31e that is annular in plan view.
Further, an upper end flange portion 31g (first flange portion) is provided at the upper end of the side surface 31f of the main body portion 31, and a lower end flange 31i (second flange portion) is provided at the lower end of the side surface 31f of the main body portion 31. ing.

The upper plate 31d and the upper end flange portion 31g are a fastening bolt 31h (fastening member) in a state where a gasket (fourth seal portion) (not shown) is sandwiched between the upper plate 31d and the upper end flange portion 31g at a plurality of positions around the axis Z. ).
Similarly, the bottom plate 31e and the lower end flange 31i are a fastening bolt 31j (fastening member) in a state where a gasket (fifth seal portion) (not shown) is sandwiched between the bottom plate 31e and the lower end flange 31i at a plurality of locations around the axis Z. It is concluded by

The reaction tube 32 is a mechanism formed in a substantially cylindrical shape extending along the axis Z. The reaction tube 32 has an outer peripheral surface 32 d that forms a combustion gas flow path 30 a for allowing a combustion gas (heating gas) to flow between the inner peripheral surface of the main body 31.
The reaction tube 32 includes a center pipe 32a (tubular member), an upper end flange 32b (third flange portion), a plurality of first inclined plates 32f, a plurality of second inclined plates 32g, and a plurality of holding rods 32h (holding portions). ).

As shown in FIG. 8, the upper end flange 32b of the reaction tube 32 and the end of the center pipe 32a on the upper end flange 32b side protrude upward from the upper plate 31d (upper surface) of the main body 31.
The lower end 32 c of the reaction tube 32 protrudes downward from the bottom plate 31 e (bottom surface) of the main body 31.

The center pipe 32a is a member formed in a cylindrical shape extending along the axis Z. Inside the center pipe 32a is housed a thermal decomposition promotion mechanism including a plurality of first inclined plates 32f, a plurality of second inclined plates 32g, and a plurality of holding rods 32h (holding portions).
The thermal decomposition promotion mechanism promotes the thermal decomposition reaction of the carbide and superheated steam (gasification agent) by guiding the carbide stepwise from the upper end side to the lower end side of the center pipe 32a and retaining the carbide in the reaction tube 32. It is a mechanism to make.

As shown in FIG. 8, the plurality of first inclined plates 32f and the plurality of second inclined plates 32g are held by four holding rods (not shown) at a plurality of locations along the axis Z. Further, the first inclined plates 32f and the second inclined plates 32g are alternately arranged along the axis Z.
The upper ends of the four holding rods are attached to the lower surface of the lower end flange 33 a of the reaction tube head 33. By releasing the fastening between the upper end flange 32b of the reaction tube 32 and the lower end flange 33a of the reaction tube head 33, the thermal decomposition promoting mechanism can be removed (detached) upward from the center pipe 32a.

As shown in FIG. 8, the first inclined surface formed by the first inclined plate 32f is inclined so as to guide the carbide falling from the second opening 32j downward, and the second inclined plate 32g forms the second inclined surface. The inclined surface is inclined so as to guide the carbide falling from the first opening 32i downward.
In this manner, the thermal decomposition promoting mechanism guides the carbide stepwise from the upper end side to the lower end side of the center pipe 32a using the first inclined plates 32f and the second inclined plates 32g that are alternately arranged along the axis Z. be able to.

The inclination angle of the first inclined surface and the second inclined surface with respect to the plane orthogonal to the axis Z can be arbitrarily set according to the properties of the carbide, but in order to reliably move the carbide along the inclined surface, the carbide It is preferable that the angle be equal to or greater than the angle of repose. On the other hand, if the inclination angle is too large, the residence time of the carbide in the reaction tube 32 is shortened, and the thermal decomposition reaction is not sufficiently promoted.
Therefore, it is particularly preferable that the inclination angle of the first inclined surface and the second inclined surface with respect to the plane orthogonal to the axis Z is determined to be equal to or greater than the repose angle of the carbide in the range of 20 ° to 60 °.

The reaction tube head 33 is attached to the reaction tube 32 and supplies carbide and superheated steam (gasification agent) to the inside of the reaction tube 32 to generate water gas inside the reaction tube 32.
The reaction tube head 33 includes a lower end flange 33a (fourth flange) attached to the reaction tube 32, an upper end flange 33b attached to the carbide supply passage 101, and a flow path (not shown) through which superheated steam is supplied from the steam superheater 81. ) And a side flange 33c attached thereto.

  The lower end flange 33a of the reaction tube head 33 and the upper end flange 32b of the reaction tube 32 are fastened by fastening bolts 33d with a gasket (sixth seal portion) (not shown) sandwiched between them at a plurality of locations around the axis Z. ing.

The water gas outlet nozzle 34 is a substantially cylindrical member attached to the lower end portion 32 c of the reaction tube 32. The water gas outlet nozzle 34 is used to reduce the temperature of the water gas generated by the pyrolysis reaction of the carbide in the reaction tube 32, the unreacted part of the carbide, the ash, and the like through the water gas supply path 102. Lead to.
In addition, the unreacted carbide guided from the water gas outlet nozzle 34 to the temperature reducer 40 is washed with superheated steam (water vapor) to remove components other than the carbon component. Therefore, the carbide guided to the temperature reducer 40 is a carbide having a high carbon content in which other components other than the carbon component are favorably removed.

The combustion gas supply unit 35 is an opening that is provided above the main body 31 and supplies the combustion gas guided from the combustion gas channel 200a to the combustion gas channel 30a.
The combustion gas discharge unit 36 is an opening that is provided below the main body 31 and discharges the combustion gas from the combustion gas channel 30a to the combustion gas channel 200b.
The combustion gas supplied from the combustion gas supply part 35 to the combustion gas flow path 30a flows from the upper end side to the lower end side of the center pipe 32a while heating the outer peripheral surface 32d of the center pipe 32a, and is discharged from the combustion gas discharge part 36. Is done.

  The gland packing 37 is a member that blocks the combustion gas in the combustion gas passage 30a from flowing out from the upper plate 31d of the main body 31 to the outside. The gland packing 37 is an annular member that is provided in contact with the lower surface of the upper plate 31 d of the main body 31 and has an inner peripheral surface 37 d that contacts the outer peripheral surface 32 d of the reaction tube 32.

  The gland packing 37 is configured in a state where the ceramic board 37a, the ceramic board 37b, and the ceramic fiber 37c are in close contact with each other. By using the ceramic fiber 37c, which is a fibrous material that can be deformed relatively easily, the sealing performance at the portion in contact with the heat insulating material 31b and the heat resistant material 31c is enhanced.

  The gland packing 38 is a member that blocks the combustion gas in the combustion gas passage 30a from flowing out from the bottom plate 31e of the main body 31 to the outside. The gland packing 38 is an annular member that is provided in contact with the upper surface of the bottom plate 31 e of the main body 31 and has an inner peripheral surface 38 d that contacts the outer peripheral surface 32 d of the reaction tube 32.

The gland packing 38 is configured in a state in which the ceramic board 38a, the ceramic board 38b, and the ceramic fiber 38c are in close contact with each other. By using the ceramic fiber 38c, which is a fibrous material that can be deformed relatively easily, the sealing performance at the portion in contact with the heat insulating material 31b and the heat resistant material 31c is enhanced.
The gland packing 39 is a member that blocks outflow of water gas from the mounting position at the mounting position of the lower end portion 32 c of the reaction tube 32 and the water gas outlet nozzle 34.

Next, the pyrolysis furnace 30, the temperature reducer 40, the cyclone 50, the steam generator 80, the steam superheater 81, and peripheral devices thereof according to this embodiment will be described in detail with reference to FIG. 9.
As shown in FIG. 9, the carbide supply path 101 includes a screw conveyor 101a, a clinker removing device 101b, a belt conveyor 101c, a magnetic separator 101d, a screw conveyor 101e, and a screw conveyor 101f.

  The screw conveyor 101 a is a device that conveys the carbide discharged from the carbonization furnace 20. The screw conveyor 101a accommodates a screw in a linearly extending cylindrical body. The screw conveyor 101a conveys the carbide along the extending direction of the cylinder by rotating the screw inside the cylinder by the driving force of the motor.

The clinker removing device 101b is a device that removes clinker having a particle size of a certain size or more from the carbide discharged from the screw conveyor 101a by a net or the like. The carbide from which the clinker is removed is conveyed to the magnetic separator 101d by the belt conveyor 101c.
The magnetic separator 101d is a device that removes iron scraps such as nails contained in carbide with a magnet. The carbide from which the iron scrap has been removed is supplied to the screw conveyor 101e.

  Each of the screw conveyor 101e and the screw conveyor 101f is a device that conveys carbides. The screw conveyor 101f supplies the carbide to the nitrogen replacement unit 30b included in the pyrolysis furnace 30. In addition, since the structure of the screw conveyor 101e and the screw conveyor 101f is the same as that of the screw conveyor 101a, description is abbreviate | omitted.

  The screw conveyor 101e and the screw conveyor 101f carry the carbide to the upper side of the pyrolysis furnace 30 because the carbide is supplied from above the pyrolysis furnace 30 and in the reaction tube 32 of the pyrolysis furnace 30 by its own weight. This is to allow carbide to pass through. By passing the reaction tube 32 of the pyrolysis furnace 30 through the dead weight of the carbide, the entire region from the upper end to the lower end of the reaction tube 32 can be used as a region for promoting the pyrolysis reaction. Further, since the carbide is passed through the reaction tube 32 by its own weight, no special power for moving the carbide is required.

  Carbide is transported in two stages, screw conveyor 101e and screw conveyor 101f, because each screw conveyor requires an expensive motor with a large driving force by reducing the power required to rotate the screw. This is to avoid the above.

The nitrogen replacement device 30b is a device that constitutes the pyrolysis furnace 30, and is a device for replacing oxygen contained in air supplied from the screw conveyor 101f together with carbides with inert nitrogen gas.
The nitrogen purger 30b is disposed on the upper side connected to the screw conveyor 101f and the lower side connected to the reaction tube head 33, and is an electric control valve (for example, a ball valve) whose open / close state is controlled by the control device 90. ).

  The control device 90 supplies carbide to the inside of the nitrogen purger 30b by opening the upper control valve and closing the lower control valve. When the amount of carbide supplied to the inside of the nitrogen purger 30b reaches a certain amount, the control device 90 stops the transportation of the carbide by the screw conveyor 101f and closes the control valve above the nitrogen purger 30b. .

  Nitrogen gas is always supplied to the nitrogen replacer 30b from a device that generates nitrogen gas, such as an air separation device. Therefore, when a certain amount of time has elapsed with the control valves above and below the nitrogen purger 30b closed, the air supplied to the nitrogen purger 30b together with the carbides is discharged to the outside and the interior is replaced with nitrogen gas. It becomes a state.

After the inside of the nitrogen purger 30b has been replaced with nitrogen gas, the control device 90 switches the control valve below the nitrogen purger 30b to the open state to transfer the carbide from the nitrogen purger 30b to the reaction tube head 33. Supply.
After supplying carbide to the reaction tube head 33 from the nitrogen purger 30b, the controller 90 closes the control valve below the nitrogen purger 30b. Further, the control device 90 then opens the control valve above the nitrogen purger 30b and supplies new carbide into the nitrogen purger 30b.

  As described above, the control device 90 controls the opening and closing of the control valves above and below the nitrogen purger 30b, so that the gas supplied to the reaction tube head 33 together with the carbide is nitrogen gas. This nitrogen gas is an inert gas that does not react with the water gas generated in the reaction tube 32. Therefore, it is possible to suppress the air containing oxygen together with the carbide from being supplied to the reaction tube 32 and causing the reaction between oxygen and the water gas to reduce the yield of the water gas.

The char recovery device 41 includes a nitrogen purger 41a and a char recovery unit 41b.
The nitrogen replacer 41a is a device for replacing the water gas supplied from the temperature reducer 40 together with the unreacted portion of the carbide with inert nitrogen gas.
The char recovery unit 41b is an apparatus that recovers an unreacted portion of the carbide and supplies the unreacted component to a nitrogen purger 30b from a supply path (not shown).
The nitrogen purger 41a is disposed on the upper side connected to the temperature reducer 40 and the lower side connected to the char recovery unit 41b, and is an electric control valve (for example, a ball) whose opening / closing state is controlled by the control device 90. Valve).

  The control device 90 supplies unreacted carbide to the inside of the nitrogen purger 41a by opening the upper control valve and closing the lower control valve. When the unreacted amount of the carbide supplied into the nitrogen purger 41a reaches a certain amount, the control device 90 closes the control valve above the nitrogen purger 41a.

  Nitrogen gas is always supplied to the nitrogen purger 41a from a device that generates nitrogen gas such as an air separation device. Therefore, when the upper and lower control valves of the nitrogen purger 41a are closed and a certain time elapses, the water gas supplied into the nitrogen purger 41a together with the unreacted portion of the carbide is discharged to the outside, and the interior is filled with nitrogen. The gas is replaced. The water gas discharged from the nitrogen purger 41a is supplied to the flare stack 71.

After the inside of the nitrogen purger 41a is replaced with nitrogen gas, the control device 90 switches the control valve below the nitrogen purger 41a to the open state, and the carbide is transferred from the nitrogen purger 41a to the char recovery unit 41b. The unreacted portion is supplied.
After supplying the unreacted portion of the carbide from the nitrogen purger 41a to the char recovery unit 41b, the control device 90 closes the control valve below the nitrogen purger 41a. In addition, the control device 90 then opens the control valve above the nitrogen purger 41a and supplies new unreacted carbon carbide into the nitrogen purger 41a.

  As described above, the control device 90 controls the opening and closing of the control valves above and below the nitrogen purger 41a, so that the water gas supplied to the char recovery unit 41b together with the unreacted carbide is supplied to the char recovery unit 41b. It is prevented from being supplied.

The residue collection device 51 includes a nitrogen purger 51a and a residue collection unit 51b.
The nitrogen purger 51a is a device for replacing the water gas supplied from the cyclone 50 together with unreacted carbides and residues with inert nitrogen gas.
The residue collection unit 51b is a device that collects unreacted carbide and residue discharged from the nitrogen purger 51a.

  The nitrogen purger 51a is disposed on each of an upper side connected to the cyclone 50 and a lower side connected to the residue recovery unit 51b, and an electric control valve (for example, a ball valve) whose open / close state is controlled by the control device 90. Have Nitrogen gas is always supplied to the nitrogen replacer 51a from a device that generates nitrogen gas such as an air separation device.

  The control device 90 controls the control valve of the nitrogen purger 51a in the same manner as the control valve of the nitrogen purger 41a, and prevents water gas from being supplied to the residue recovery unit 51b. . The method by which the control device 90 controls the control valve of the nitrogen purger 51a is the same as the method by which the control device 90 controls the control valve of the nitrogen purger 41a, and thus the description thereof is omitted.

The steam generator 80 includes a steam generation unit 80a and a steam circulation tank 80b.
The steam generation unit 80a includes a heat transfer tube (not shown) that circulates water that exchanges heat with the combustion gas, and a jacket (not shown) that is provided in a cylindrical body that is formed so as to cover the heat transfer tube. Abbreviation). Water is supplied to the heat transfer tube and the jacket from the steam circulation tank 80b.

The steam circulation tank 80b is supplied with water from the water supply device 82 and supplies water to the heat transfer tube and the jacket of the steam generation unit 80a. The hot water heated by the jacket and the steam generated by heating the heat transfer tube with the combustion gas are respectively collected in the steam circulation tank 80b.
The steam circulation tank 80b supplies the steam (saturated steam) supplied from the heat transfer tube of the steam generating unit 80a to the steam superheater 81.

Next, the dryer 10 of this embodiment is demonstrated in detail using FIG.
The dryer 10 is a dryer of a type called a rotary kiln, and includes a combustion gas introduction unit 10b, a rotating body 10c, and a discharge unit 10d.
The combustion gas introduction part 10b introduces the combustion gas supplied from the combustion gas flow path 200d into the dryer 10 and introduces the introduced combustion gas into the rotary body 10c.

The rotating body 10c is a cylindrical member formed in a direction extending along the axis W, and rotates about the axis W by being given rotational power by a drive motor.
Moreover, organic waste is supplied into the inside of the rotary body 10c from the raw material supply path 11a. The organic waste supplied to the inside of the rotating body 10c is guided toward the discharge unit 10d while being dried by the combustion gas guided from the combustion gas introduction unit 10b.
The organic waste is directly heated by the combustion gas while being stirred by the rotation of the rotating body 10c, and is conveyed by the flow of the combustion gas from one end to the other end of the rotating body 10c.

The discharge unit 10d collects the organic waste dried while being conveyed by the rotating body 10c and supplies it to the raw material supply path 10a. The organic waste supplied to the raw material supply path 10 a is supplied to the carbonization furnace 20 via the hopper 12.
Further, the discharge unit 10d supplies the combustion gas introduced from the combustion gas introduction unit 10b through the inside of the rotating body 10c to the combustion gas channel 200e. The combustion gas supplied to the combustion gas flow path 200e is supplied to the exhaust gas cooling and cleaning device 13.

Next, the characteristics of the carbide obtained in the carbonization furnace 20 of the present embodiment and the carbide obtained in the char recovery device 41 and the residue recovery device 51 will be described.
When wood waste containing 15% by weight of water was used as organic waste supplied from the hopper 12, 15 to 25% by weight of carbide was obtained in the carbonization furnace 20 with respect to the organic waste. The water gas generation system 100 is continuously operated, and the carbides discharged from the carbonization furnace 20 are collected about every 6 hours to obtain a total of 16 samples of carbides. An organic element analyzer (MT-5 manufactured by Yanaco Analytical Industries, Ltd.) ). As a result, the average carbon content of the carbide was 91.5%, and the standard deviation was 1.5%. The measured specific surface area of the carbide with a specific surface area measuring device (Quantachrome Co. ^Nova-4200e), to give the results of 300m ² / g~400m 2 / g. Moreover, when ash (other components other than carbide) contained in organic waste was analyzed with a fluorescent X-ray analyzer (PW2400 manufactured by Philips), it was found that about 52 weight percent of Ca was contained in the entire ash. The result was obtained.

Further, when the wood waste material containing 15% by weight of water is used as the organic waste supplied from the hopper 12, the char recovery device 41 and the residue recovery device 51 are added up to about 2 with respect to the organic waste. -3 wt% unreacted carbide was obtained. The water gas generation system 100 is continuously operated, and the carbides discharged from the char recovery device 41 and the residue recovery device 51 are collected about every 6 hours to obtain a total of 16 samples of carbides. The analysis was conducted with MT-5) manufactured by the company. As a result, the average carbon content of the carbide was 92.1%, and the standard deviation was 1.4%. The measured specific surface area of the carbide with a specific surface area measuring device (Quantachrome Co. ^Nova-4200e), to give the results of 300m ² / g~400m 2 / g. Moreover, when ash (other components other than carbide) contained in organic waste was analyzed with a fluorescent X-ray analyzer (PW2400 manufactured by Philips), it was found that about 52 weight percent of Ca was contained in the entire ash. The result was obtained.

  Thus, according to the water gas generation system 100 of the present embodiment, 15 to 25% by weight of carbide can be obtained with respect to the organic waste, and the carbon content of the carbide is about 92%. Therefore, according to the water gas generation system 100 of the present embodiment, the carbonization furnace 20, the char recovery device 41, and the residue recovery device 51 can obtain a carbide with a high carbon yield and have a very high carbon content. Can be obtained.

Further, according to the water gas generation system 100 of the present ^embodiment, it is possible to obtain a large carbide having a specific surface area of 300m ² / g~400m 2 / g. The carbide having a large specific surface area is useful as a humidity control agent or an adsorbent (activated carbon). FIG. 11 shows an image obtained by imaging the carbide obtained by the water gas generation system 100 of the present embodiment with a scanning electron microscope, and shows a structure having a large specific surface area. A scale is shown in the lower right of FIG. 11, and one scale is 100 μm.

It should be noted that the carbon content of the carbides obtained by the char recovery device 41 and the residue recovery device 51 (average value of 92.1 than the carbon content of the carbides obtained by the carbonization furnace 20 (average value of 91.5%). %) Is higher. This is because the carbide obtained by the char recovery device 41 and the residue recovery device 51 is washed with superheated steam (water vapor) in the pyrolysis furnace 30 and other components other than the carbon component are well removed.
In addition, the carbide produced by the water gas generation system 100 of the present embodiment can be effectively used for other uses than the above-described humidity control agent and adsorbent. For example, it can also be used as a soil conditioner, a charcoal agent, a snow melting agent, and an abrasive.

The operation and effects of the present embodiment described above will be described.
According to the water gas generation system 100 of the present embodiment, organic waste is discharged from the organic waste charging unit 23 into the gap 20 a formed between the inner peripheral surface of the main body 21 of the carbonization furnace 20 and the outer peripheral surface of the cylindrical portion 22. In the normal operation state of the carbonization furnace 20, the organic waste thrown from the organic waste throwing portion 23 is accumulated from the lower side to the upper side of the gap 20a along the axis X. The organic waste on the upper layer side of the gap 20a is partially burned by the primary combustion air supplied from the primary air supply unit 25 and guided to the lower layer side of the gap 20a.

  The organic waste on the lower layer side of the gap 20a is blocked by the organic waste on the upper layer side, and the lower layer side of the gap 20a becomes a carbide smelting / cooling region R1 in which solid content containing a large amount of carbon components is refined and cooled. In the carbide refining / cooling region R1, the solid content containing a large amount of carbon components is refined while being further carbonized in a state where the oxygen concentration is low, and is gradually extinguished as it approaches the lower end of the gap 20a. Thereby, the temperature of the carbide | carbonized_material discharged | emitted from the lower end of the gap | interval 20a can be made low.

  Further, according to the water gas generation system 100 of the present embodiment, the carbonization state of the organic waste is controlled so that the organic waste is maintained in a predetermined temperature range at the gap 20a. For this reason, the organic waste becomes a high temperature and most of the carbon components are completely burned, or the organic waste becomes a low temperature in the gap and other components other than the carbon component cannot be sufficiently removed. Can be suppressed. Here, for example, the predetermined temperature range is preferably 900 ° C. or more and 1200 ° C. or less, and more preferably 1000 ° C. or more and 1100 ° C. or less.

Further, according to the water gas generation system 100 of the present embodiment, control is performed so that organic waste is deposited in the gap 20a over a predetermined time. Therefore, it is possible to suppress the problem that the time for the organic waste to accumulate in the gap 20a is shortened and other components other than the carbon component cannot be sufficiently removed from the organic waste. Here, the predetermined time is preferably in the range of, for example, 30 minutes or more and 50 minutes or less.
Thus, according to the water gas generation system 100 of the present embodiment, it is possible to produce a carbide from which other components other than the carbon component are sufficiently removed while suppressing a decrease in the carbon component contained in the organic waste. it can.

The water gas generation system 100 of the present embodiment includes a pyrolysis furnace 30 that generates a water gas by causing a pyrolysis reaction between the carbide discharged from the carbide discharge unit 24 and superheated steam, and a carbide discharged from the pyrolysis furnace 30. And a char collection device 41 and a residue collection device 51.
By doing in this way, unreacted carbide | carbonized_material can be collect | recovered, carrying out the pyrolysis reaction of the carbide | carbonized_material with high carbon content, and superheated steam in the thermal decomposition furnace 30, and producing | generating water gas. This unreacted carbide is one obtained by washing with superheated steam to remove other components than the carbon component. Therefore, it is possible to obtain a carbide having a high carbon content in which other components other than the carbon component are well removed.

Second Embodiment
Next, the carbide manufacturing system 300 of 2nd Embodiment of this invention is demonstrated with reference to drawings.
The carbide manufacturing system 300 of the present embodiment is a modification of the water gas generation system 100 of the first embodiment. The carbide manufacturing system 300 of the present embodiment is assumed to be the same as the water gas generation system 100 of the first embodiment unless otherwise described below.

The water gas generation system 100 of the first embodiment generates water gas by causing the carbide obtained in the carbonization furnace 20 to undergo thermal decomposition reaction with superheated steam in the pyrolysis furnace 30, and produces water gas as a main product. Thus, carbide was produced as a by-product.
On the other hand, the carbide manufacturing system 300 of this embodiment is not equipped with a pyrolysis furnace, and manufactures a carbide as a main product.

  As shown in FIG. 12, the carbide production system 300 of the present embodiment includes a dryer 10, a hopper 11, a hopper 12, an exhaust gas cooling and cleaning device 13, a carbonization furnace (carbide production apparatus) 20, and a carbonization furnace 20. A carbide recovery device 310 that recovers the carbide produced in the above, a steam generator (heat exchanging unit) 320 that generates steam by performing heat exchange between the combustion gas discharged from the carbonization furnace 20 and water (heat medium), and The steam turbine 330 driven by the steam generated by the steam generator 320, the power generation equipment 340 for obtaining power generation output by a generator connected to the turbine shaft (not shown) of the steam turbine 330, and each part of the carbide manufacturing system 300 And a control device 350 for controlling.

  The power generation facility 340 can supply power so that the generated power output is used in each part of the carbide manufacturing system 300. Further, the power generation facility 340 can supply a power generation output that is excessive in the carbide manufacturing system 300 to a power system (not shown). Note that the steam generated by the steam generator 320 and used as the rotational power of the turbine shaft of the steam turbine 330 is reconstituted by a condenser (not shown) and then supplied again to the steam generator 320 as a heat medium. The

In the carbide manufacturing system 300 shown in FIG. 12, the combustion gas produced | generated by the carbonization furnace 20 distribute | circulates as follows by the combustion gas flow path which consists of combustion gas flow paths 300a, 300b, 300c.
The combustion gas generated by the carbonization furnace 20 is supplied to the steam generator 320 through the combustion gas passage 300a. The combustion gas discharged from the steam generator 320 is supplied to the dryer 10 through the combustion gas channel 300b. The combustion gas discharged from the dryer 10 is supplied to the exhaust gas cooling and cleaning device 13 through the combustion gas channel 300c. The combustion gas detoxified by the exhaust gas cooling and cleaning device 13 is discharged into the atmosphere by the exhaust gas cooling and cleaning device 13.

According to the carbide production system 300 of the present embodiment, since the entire amount of carbide produced in the carbonization furnace 20 is recovered by the carbide recovery device 310, a carbide having an extremely high carbon content can be obtained as a main product.
In addition, according to the carbide manufacturing system 300 of the present embodiment, steam is generated by heat exchange of the high-temperature (for example, 1000 ° C. to 1200 ° C.) combustion gas generated in the carbonization furnace 20 with water, and a steam turbine. 330 can be operated and recovered as power for the power generation equipment 340. Further, the combustion gas having a relatively high temperature (for example, 500 ° C. to 600 ° C.) that has passed through the steam generator 320 can be used for drying organic waste in the dryer 10, and the heat of the combustion gas can be further effectively used.

[Other Embodiments]
The present invention is not limited to the above-described embodiment, and can be changed as appropriate without departing from the scope of the invention.

10 Dryer (drying section)
20 Carbonization furnace 20a Gap 21 Body part 22 Cylindrical part 23 Organic waste input part 24 Carbide discharge part 25 Primary air supply part (air supply part)
26 Secondary air supply unit (second air supply unit)
27 Combustion gas discharge part 28a Temperature sensor 28b Temperature sensor (first temperature detection part)
28c Temperature sensor (second temperature detector)
28d Level sensor (deposition amount detector)
29 Carbonization furnace control unit (control unit)
30 Pyrolysis furnace (Pyrolysis part)
40 Desuperheater 41 Char recovery device (Carbide recovery unit)
51 Residue recovery unit (Carbide recovery unit)
90 Control device 100 Water gas generation system 300 Carbide production system 310 Carbide recovery device R1 Carbide refining / cooling region R2 Primary combustion region R3 Raw material input region R4 Secondary combustion region W, X, Y, Z axes

Claims (11)

A main body formed in a cylindrical shape extending along the axis;
A cylindrical portion having an outer peripheral surface which is formed in a cylindrical shape extending along the axis and forms a gap for carbonizing organic matter between the inner peripheral surface of the main body portion;
An organic substance input unit for introducing the organic substance into the gap;
An air supply unit for supplying combustion air for partially burning the organic matter deposited in the gap;
A carbide discharge portion for discharging carbide obtained by carbonizing the organic matter from the gap;
A carbide manufacturing apparatus comprising: a control unit that controls a carbonization state of the organic substance so that the organic substance is maintained in a predetermined temperature range in the gap and the organic substance is deposited in the gap over a predetermined time. The control unit is
Controlling the supply amount of the combustion air supplied by the air supply unit so that the organic matter is maintained in the predetermined temperature range in the gap;
The carbide manufacturing apparatus according to claim 1, wherein the carbide discharge amount discharged by the carbide discharge unit is controlled so that the organic matter is accumulated in the gap over the predetermined time. A first temperature detector that detects an ambient temperature of a fuel region in which the organic matter is partially burned by the combustion air;
A second temperature detector for detecting the temperature of the organic matter deposited in the gap,
The control unit is
Controlling the supply amount of the combustion air supplied by the air supply unit according to the temperature detected by the first temperature detection unit;
The carbide manufacturing apparatus of Claim 2 which controls the discharge | emission amount of the said carbide | carbonized_material which the said carbide | carbonized_material discharge part discharge | releases according to the temperature which the said 2nd temperature detection part detects.   The said predetermined temperature range is a range of 900 degreeC or more and 1200 degrees C or less, The carbide manufacturing apparatus as described in any one of Claims 1-3.   The said predetermined time is 30 minutes or more and 50 minutes or less, The carbide manufacturing apparatus as described in any one of Claims 1-4. A thermal decomposition unit that generates a water gas by performing a thermal decomposition reaction between the carbide discharged from the carbide discharge unit and water vapor;
The carbide manufacturing apparatus according to any one of claims 1 to 5, further comprising a carbide recovery unit that recovers the carbide discharged from the thermal decomposition unit. An outer periphery that forms a gap between the main body formed in a cylindrical shape extending along the axis and the inner peripheral surface of the main body and formed in a cylindrical shape extending along the axis. A carbide manufacturing method using a carbide manufacturing apparatus including a cylindrical portion having a surface,
An organic substance charging step of charging the organic substance into the gap;
An air supply step of supplying combustion air to the gap and partially burning the organic matter deposited in the gap;
A carbide discharging step of discharging the carbonized organic matter from the gap;
And a control step of controlling a carbonization state of the organic substance so that the organic substance is maintained in a predetermined temperature range in the gap and the organic substance is deposited in the gap over a predetermined time. The control step is
Controlling the amount of combustion air supplied by the air supply step so that the organic matter is maintained in the predetermined temperature range;
The carbide manufacturing method according to claim 7, wherein an amount of the carbide discharged in the carbide discharging step is controlled so that the organic material is deposited in the gap over the predetermined time. A first temperature detection step of detecting an ambient temperature of a fuel region in which the organic matter is partially burned by the combustion air;
A second temperature detection step of detecting the temperature of the organic matter deposited in the gap,
The control step is
Controlling the supply amount of the combustion air supplied by the air supply step according to the temperature detected by the first temperature detection step;
The carbide manufacturing method according to claim 8, wherein an amount of the carbide discharged by the carbide discharging step is controlled according to a temperature detected by the second temperature detecting step. The carbide manufacturing apparatus according to any one of claims 1 to 5,
A heat exchanging section for exchanging heat between the combustion gas discharged from the carbide producing apparatus and the heat medium;
A carbide production system comprising: a power generation unit that generates power by obtaining power from the heat medium heated by the heat exchange unit.   The carbide manufacturing system according to claim 10, further comprising a drying unit that dries the organic matter input from the organic material input unit by the combustion gas heat-exchanged by the heat exchange unit.