JP2008292018A - Supercritical water biomass combustion boiler - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To continuously generate high-temperature and high-pressure combustion gas by using, as fuel, all types of biomass having a water content of approximately 90% or smaller regardless of shapes and forms, to generate supercritical water by the direct drive of a gas turbine for power generation or by heat exchange and use the supercritical water for the drive of a steam turbine for power generation, to simplify a device configuration, to collect and effectively use waste heat, to and achieve economy for a distributed power plant. <P>SOLUTION: This combustion boiler device uses a supercritical water oxidative reaction, uses an organic matter with a high water content such as biomass as fuel, and generates high-temperature and high-pressure combustion gas mainly composed of supercritical water. The combustion boiler device has divided operation elements such as "sealing-pressure intensification", "constant pressure-temperature rise", "combustion-temperature rise", "stable combustion" and "discharge-filling", and operates reactors of the respective operation elements. This operation can continuously generate a stable thermal output, eliminate the necessity of the continuous supply of solid fuel such as biomass to a high-temperature and high-pressure system, and achieve batch supply at an easily-supplied temperature and pressure. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

  The present invention includes a high water content biomass of about 85%, regardless of the type or form, and burns most unused biomass to directly generate high temperature and high pressure supercritical water and carbon dioxide. It relates to boilers, and is intended for use in distributed power plants that can respond to biomass generation locations according to the generation amount.

Mankind has used the biomass that grows around it as a heat energy source necessary for daily life such as heating, lighting, and cooking for many millions of years since its birth until the industrial revolution. However, since biomass generally has a high water content, when it is used as a fuel, wood having a low water content or relatively easy to dry and easy to transport, or processed charcoal has been used. In rural areas, dry straw, satoyama dead trees, fallen leaves, etc. discharged from agricultural pasture have been used. Devices for burning these are extremely small-scale devices such as soot and stoves, but various devices have been made to increase combustion efficiency and thermal efficiency with respect to air intake and flues.
On the other hand, since the industrial revolution, the use of energy as a power source has rapidly expanded from the invention of the steam engine. This was supported by finite fossil resources such as coal, oil, and natural gas buried on the earth, and the status of biomass, including heat sources, was almost lost. By supplying a large amount of fossil resources, it becomes possible for households to use energy, gas, kerosene, etc., which is based on a huge thermal power plant. Socially, airplanes, railroads and automobiles can be used. Transportation, transportation, etc. have been developed, various industrial machines have been invented, material mass production, large-scale land development, enormous food production, etc. have realized unprecedented material abundance and rapid population growth. .
However, this huge consumption of finite fossil resources not only leads to its depletion, but also contributes to global warming due to the release of a large amount of carbon dioxide to the atmosphere. We are facing a situation that needs to be reduced as quickly as possible. In order to solve such problems, the use of biomass as fuel, which has been carried out since ancient times, is the most effective and direct.

However, the burning of wood that has been used in the past is extremely limited due to its accumulation and quantity problems. For example, wood chips at a sawmill, power generation using combustion heat of waste materials, etc. can be considered, and some have been put into practical use, but the location is quite limited. On the other hand, attempts have been made to divert cultivated land and use fermented ethanol, vegetable oils and the like from sugars such as corn, straw and sugar as liquid fuels for internal combustion engines. The production of these liquid fuels is an application of the prior art, and there are few technical issues, but these biofuels have a big problem of competition with food, and a large amount of consumption exceeding the current harvest is expected As a result, food prices will not only rise and food importing countries are worried that there will be an absolute shortage of food in the future.
On the other hand, it is considered that unused biomass such as cellulose and lignin is gasified to produce hydrogen and carbon monoxide and used as synthetic gasoline by hydrogen energy and FT reaction. The former is regarded as an important technology as future energy by combining with the fuel cell. In the latter, the former gasification technology is still under development, but the latter FT reaction is a mass production technology that has been put to practical use using coal as a raw material. However, it is not always appropriate to handle biomass that is widely and thinly dispersed and that is composed of various forms and various components in a mass production and supply system similar to fossil resources. On the other hand, the annual carbon cycle by plants is said to be 90 billion carbon tons. In terms of quantity, biomass resources are enormous, and about 10% of the circulation amount replaces the currently consumed fossil resources. It will be possible.

The use of biomass as fuel has been practiced since ancient times, but its use does not exceed the range of cooking and heating. Currently, thermal power plants can be cited as the largest source of energy resources. Here, there is an ultra-large boiler that can generate 1 million kW of power using oil and coal as fuel. If the power generation efficiency is 40%, the necessary combustion heat in this boiler will be 2.5 million kW, and 200 tons of fossil resources with a calorific value of 45,000 kJ / kg will be burned per hour. If this is replaced with biomass, if the calorific value is about 1/3 of fossil resources, biomass of 600 tons / hr is required. Approximate the land area required to produce this quantity.
If the photosynthesis efficiency is now 2% and the solar energy received on the surface is 250W / m2, the fixed amount of biomass energy is 50kw / ha, and if converted in terms of cellulose production, 0.00286kg-cellulose / s / ha = 10.3kg Estimated biomass production of / hr / ha. If all the biomass that grows is used for boiler fuel, the area required to harvest 1 million kW of biomass will reach approximately 60,000 ha (600 km2), equivalent to the cultivated land area in Ehime Prefecture. As shown in this rough calculation, it can be seen that positioning biomass as an alternative fuel for current large-scale power generation is unrealistic just considering its collection. Moreover, since it is limited to biomass such as dry wood having a low water content in order to stably burn it with a conventional boiler device, a larger amount of land is actually required.

However, biomass energy production in cultivated land of 100 hectares can be as high as 5000 kW, and if 10% of it can be used in a distributed manner for power generation and thermal energy, the energy required for farming can be sufficiently supplied, There is no doubt that biomass is one of the important energy resources in the future. Even at present, measures to reduce carbon dioxide in thermal power plants are an urgent issue, and at most several percent of biomass co-firing in existing thermal power plants is also cited as an important measure. Also, in places where waste materials, wood chips, etc. are concentrated, it is becoming possible to locate power plants that use biomass as boiler fuel on the extension of existing technology.
If the plant configuration hardly changes regardless of the scale, the unit price of production decreases as the scale increases, and a huge power plant becomes advantageous. Therefore, conversion from limited fossil resources to biomass that grows in the surroundings and can be recycled has to improve the economics of small-scale distributed power plants and drastically change the equipment itself. Simplification by is very important. Fortunately, the reduction in the size of the power plant is not only a demerit due to equipment costs, but on a scale that is mainly for self-consumption without the purpose of comprehensive use of waste heat and power sales reaching about 60% during power generation, Transmission loss and transmission cost can be ignored. Even at this time, considering the rising oil prices and the need for global warming countermeasures, biomass power generation using existing technologies may be less economical than existing power grid purchases depending on location. Is becoming limited.

In the conventional combustion technology, as described above, only the types of biomass that are extremely limited due to restrictions on the moisture content and the raw material form must be targeted. Fig. 1 shows the adiabatic flame temperature when cellulose is used as a biomass component and completely burned with a theoretical oxygen amount in pure oxygen under various moisture contents. If the spontaneous ignition temperature in the presence of oxygen is 350 ° C., the adiabatic flame temperature does not reach the spontaneous ignition temperature unless the water content is 0.833 or less under atmospheric pressure (0.1014 MPa). Of course, there is no existing atmospheric pressure boiler that stably burns at a relatively low temperature of about 500 to 700 ° C. Moreover, in order to sustain combustion stably, the adiabatic flame temperature is preferably equal to or higher than the steady combustion temperature, and if the combustion temperature is 1000 ° C., the moisture content of the biomass at this time is about 0.74, It can be seen that without development, it is difficult to stably burn most biomass raw.

On the other hand, when the combustion pressure is increased, the adiabatic flame temperature rises as shown in FIG. 1, and it can be seen that at 20 MPa or higher, the moisture content is about 0.9 or higher even when the water content is about 0.9. Moreover, combustion under such high pressure is known as supercritical water oxidation (SCWO), and it is well known that stable oxidation (combustion) of various organic substances is possible if the pyrophoric temperature is exceeded. Numerous papers and patents have been proposed as detoxification treatments for harmful organic substances such as water and dioxin, and some have been put into practical use. In addition, a wet oxidation method using an oxidation catalyst in a hydrothermal environment of about 250 ° C. for the decomposition treatment of sewage sludge has been proposed and its effectiveness has been confirmed. In addition, in many documents and patents, the recovery of the oxidation heat is also mentioned. For example, US Pat. No. 5,667,698 (Patent Document 1), US Pat. No. 7,186,345 (Patent Document 2), and literatures cited in those documents are cited.
However, its main purpose is only hazardous waste treatment, and heat recovery is only expected as a means for reducing treatment costs to increase competitiveness over other treatment methods. In other words, at present, there is no example in which supercritical water oxidation (SCWO) is specifically studied as a combustion method for a boiler dedicated device.

U.S. Pat.No. 5,667,698 U.S. Patent No. 7,186,345

The present invention covers all biomass generated in forests, wilderness, golf courses, farmland such as orchards and fields, freshwater and seawater (only unused biomass such as grain stems and pruned branches directly related to primary products) , Undergrowth, defoliation, weeds, and plants with high photosynthetic efficiency by cultivation during the rest period)
Or, it is related to a biomass boiler plant that uses biomass waste such as squeezed residue and extraction residue in beverages, food processing factories, etc., and combustible municipal waste such as garbage (including organic products such as plastic) as fuel. is there.
The main technical problems to be solved by the present invention are:
1) Any type of biomass up to 90% moisture content can be used as fuel, regardless of shape and form.
2) To generate high-temperature and high-pressure combustion gas continuously and directly drive the power generation gas turbine, or generate supercritical water by heat exchange and enable it to drive the power generation steam turbine. ,
3) Considering the simplification of equipment configuration, recovery of waste heat, and effective use, realizing economic efficiency for distributed power plants,
It is.

It is well known that various organic substances can be stably combusted by supercritical water oxidation (SCWO). The combustion conditions are generally that air or oxygen is used as the oxidizing agent in supercritical water at 400 to 650 ° C. and 20 to 30 MPa. In addition, most organic substances spontaneously undergo oxidation at a significant rate when the temperature exceeds 300 ° C. in the presence of oxygen.
The present invention applies the supercritical water oxidation reaction conditions to the combustion of biomass, adds the water contained in the biomass itself and water as necessary, and converts the supercritical water field at 350 to 650 ° C. and 20 to 30 MPa to such as biomass. Organic combustion boilers, such as biomass combustion boilers (combustion equipment) and combustion technology, which are produced stably with the combustion heat of organic matter and are continuously produced in high-temperature and high-pressure exhaust combustion fluid when supercritical water is the main component. is there. The combustion boiler has a plurality of SCWO reactors and a combustion chamber arranged at the subsequent stage. By sequentially cycling the plurality of SCWO reactors, a batch supply of biomass fuel at atmospheric pressure is performed. And a continuous output can be stably obtained.

The present invention provides the following.
[1] Applying supercritical water oxidation (SCWO) to generate high-temperature and high-pressure combustion fluids that contain at least biomass and use organic matter with a high water content as fuel and mainly contain supercritical water. A combustion boiler device characterized by being.
[2] At least two or more SCWO reactors and a combustion chamber for receiving a high-temperature and high-pressure combustion fluid mainly composed of supercritical water discharged from the SCWO reactor and generated by the organic SCWO. The combustion boiler device according to the above [1], wherein
[3] Operation of the combustion boiler apparatus is at least “sealing / pressure increase”, “constant pressure / temperature increase”, “combustion / temperature increase” or “constant pressure / combustion / temperature increase”, “steady combustion”, and “discharge / filling”. The operation element is divided into the operation elements, and the pipes and valve systems that enable each of the operations to be performed, continuously generating a stable heat output and continuously supplying a solid fuel such as biomass to a high-temperature, high-pressure system. The combustion boiler device according to the above [1] or [2], wherein supply is not required and batch supply is possible at a temperature and pressure that are easy to supply.
[4] A combustion chamber is provided at the rear stage of the reactor to join all the fluids flowing out from the SCWO reactor and completely burn unburned organic substances (organic substances mainly dissolved in hot water) contained in the flowing fluid. The combustion boiler device according to any one of the above [1] to [3], wherein the high-temperature and high-pressure fluid is continuously generated.
[5] A heat exchanger is provided downstream of the combustion chamber at the rear stage of the SCWO reactor, and high temperature / high pressure steam can be generated through the heat exchanger. The combustion boiler device according to any one of 1] to [4].
[6] A first combustion chamber and a second combustion chamber are provided as combustion chambers downstream of the SCWO reactor, and when the SCWO reactor performs “combustion / temperature increase” and “steady combustion” operations, A piping line for introducing the unburned product-containing exhaust fluid from the SCWO reactor in the operating state and the SCWO reactor in the “steady combustion” operating state into the first combustion chamber; The first combustion chamber is capable of combusting unburned matter and a part of the generated high-temperature / high-pressure fluid is used in the SCWO reactor in the “sealing / pressurizing” operation state and the SCWO reaction in the “constant pressure / temperature raising” operation state. And a piping line for introducing the remainder of the high-temperature / high-pressure fluid generated in the first combustion chamber into the second combustion chamber. The remainder of the high pressure fluid and the lower temperature than the self-combustion temperature discharged from the SCWO reactor in the “constant pressure / pressure increase” operation The exhaust fluid is mixed at the entrance of the second combustion chamber, heated to a temperature higher than the self-combustion temperature, and unburned fuel is completely burned to obtain a heat output as a high-temperature high-pressure fluid. The combustion boiler device according to any one of 1] to [5].
[7] The combustion boiler device according to any one of [1] to [6], further including a start-up heater for the combustion boiler device.
[8] After the steady combustion of the SCWO reactor is completed, water is injected into the high-temperature / high-pressure fluid remaining in the SCWO reactor, and a pipe line for reducing the pressure is used. Any of the above-mentioned [1] to [7], comprising a device for recovering thermal energy and, if necessary, a device for recovering combustion gas such as carbon dioxide remaining in the SCWO reactor. A combustion boiler device according to claim 1.
[9] SCWO reactor in which a heat insulating layer is provided on the inner surface of the reactor with ceramics having low thermal conductivity.

[10] Applying a supercritical water oxidation reaction (SCWO) to generate a high-temperature and high-pressure combustion fluid containing at least biomass and using organic matter with a high water content as a fuel and containing supercritical water as a main component, A method for obtaining and generating heat from an organic material, comprising completely burning unburned organic material contained in a fluid obtained from SCWO to generate a high-temperature and high-pressure fluid.
[11] Operating an SCWO reactor and an organic combustion boiler device having a combustion chamber located downstream thereof,
(1) Press-fit supercritical water into the SCWO reactor in a sealed state, and pressurize the SCWO reactor filled with the raw material to the combustion pressure (“sealed / pressurized”).
(2) Supercritical water is allowed to flow through the SCWO reactor, the temperature in the SCWO reactor is raised to the self-combustion temperature of the charged raw material under a constant pressure, and the supercritical water from the SCWO reactor is the main component. And let the hot water containing unburned organic matter flow out into the combustion chamber ("constant pressure / temperature rise"),
(3) Supply oxygen to the SCWO reactor, burn the charged raw material in the SCWO reactor under a constant pressure, and heat from the SCWO reactor mainly containing supercritical water and containing unburned organic matter. Causing water and carbon dioxide to flow into the combustion chamber (“constant pressure, combustion, temperature rise”) or supply oxygen to the SCWO reactor, and combust the charged material in the SCWO reactor, and from the SCWO reactor Causing hot water and carbon dioxide containing supercritical water and unburned organic matter to flow into a specific combustion chamber ("combustion / heating"),
(4) Cooling water is supplied to the SCWO reactor to maintain its combustion temperature so that combustion of the charged raw material in the SCWO reactor is maintained, and supercritical water is mainly supplied from the SCWO reactor. Causing hot water and carbon dioxide as components and containing unburned organic matter to flow into the combustion chamber ("steady combustion"),
(5) Cooling water is injected into the SCWO reactor, the temperature is lowered and lowered, and after reaching a predetermined temperature, the cooling water supply is stopped, and the hot water and carbon dioxide are discharged and recovered. After that, the organic raw material is supplied and charged into the SCWO reactor (“discharge / fill”)
It is attached to each of the operating elements of the above, generating stable heat output continuously, eliminating the need for continuous supply of solid fuel including biomass to high temperature and high pressure systems, batch supply at a temperature and pressure that is easy to supply The method for obtaining and generating heat from an organic material as described in [10] above, wherein
[12] An organic combustion boiler apparatus equipped with a plurality of SCWO reactors is operated to combine all fluids flowing out from the SCWO reactors, and unburned organic substances (organic substances mainly dissolved in hot water) contained in the outflowing fluid The method for obtaining and generating heat from organic matter according to [10] or [11] above, wherein a combustion chamber is provided in the latter stage of the reactor for complete combustion in a batch, and a high-temperature and high-pressure fluid is continuously generated .
[13] The heat from the organic matter according to any one of [10] to [12], wherein high-temperature and high-pressure steam is generated by a heat exchanger downstream of the combustion chamber downstream of the SCWO reactor. How to get out.
[14] Operating an organic combustion boiler apparatus having a first combustion chamber and a second combustion chamber as a combustion chamber downstream of the SCWO reactor, and operating the SCWO reactor in a “burning / heating” operating state and a “steady combustion” operating state The unburned matter-containing exhaust fluid from the SCWO reactor is introduced into the first combustion chamber, the unburned matter is combusted as necessary in the first combustion chamber, and a part of the generated high-temperature / high-pressure fluid is “sealed”・ Send to SCWO reactor in “pressurization” operation state and SCWO reactor in “constant pressure / temperature increase” operation state, while introducing the remainder of the high temperature and high pressure fluid generated in the first combustion chamber into the second combustion chamber This flow is mixed with the exhaust fluid at a temperature lower than the self-combustion temperature discharged from the SCWO reactor in the “constant pressure / pressure increase” operation state, and the temperature is raised to the self-combustion temperature or more at the second combustion chamber. It is characterized by completely burning unburned fuel and obtaining heat output as a high-temperature and high-pressure fluid. That generates the acquisition method of heat from organic matter according to any of the above [10] to [13].
[15] In the start-up of the organic combustion boiler apparatus, the SCWO reactor in the first “sealed / pressure-increasing” operation state is heated with a heater to increase the pressure to a predetermined pressure. [14] The method for obtaining and generating heat from the organic material according to any one of [14].
[16] After completing the “steady combustion” operation state of the SCWO reactor, water is injected into the high-temperature / high-pressure fluid remaining in the SCWO reactor, the pressure is reduced, and the resulting reduced-pressure high-temperature water is used. The thermal energy is recovered, and if necessary, the combustion gas such as carbon dioxide remaining in the SCWO reactor is recovered as described in any one of the above [10] to [15] A method for obtaining heat from organic substances.

In the present invention, it has succeeded in fueling biomass with a high water content using the SCWO reaction, and by adopting batch raw material supply, biomass of various forms and shapes can be used as raw materials. By using a plurality of reactors corresponding to each operation, stable and continuous output is possible, and the structure of the apparatus can be simplified, and the apparatus cost in a small-scale distributed biomass combustion boiler is greatly increased. Contributes to reduction.
The biomass boiler plant of the present invention and its operation technology continuously generate high-temperature and high-pressure combustion gas that can use any type of biomass up to about 90% moisture as fuel, regardless of shape and form, and generate electricity. It is possible to directly drive a gas turbine for industrial use or generate supercritical water by heat exchange and use it to drive a steam turbine for power generation, simplify the system configuration, and also recover and effectively use waste heat. Yes, it can also be economical for distributed power plants.
Other objects, features, excellence and aspects of the present invention will be apparent to those skilled in the art from the following description. However, it is understood that the description of the present specification, including the following description and the description of specific examples and the like, show preferred embodiments of the present invention and are presented only for explanation. I want. Various changes and / or modifications (or modifications) within the spirit and scope of the present invention disclosed herein will occur to those skilled in the art based on the following description and knowledge from other parts of the present specification. Will be readily apparent. All patent documents and references cited herein are cited for illustrative purposes and are not to be construed as a part of this specification. is there.

Biomass is the expression of the amount of organisms that exist in a space at a specific point in time as a quantity of material, but when used as an industrial resource, biomass is not a fossil resource, but a living organism. It refers to industrial resources originating from material constituent materials. In the present specification, “biomass” may mean a biologically derived organic resource excluding fossil resources. Biomass may mean carbon neutral or a renewable resource. Biomass includes, for example, livestock waste from agriculture, forestry and fisheries (including livestock manure), wood (including waste materials), firewood, resource crops (plants such as corn, sugarcane, rice, wheat) and waste (waste) (Including vegetable oils), waste generated from the food industry, and waste (including black liquor) generated in the paper pulp manufacturing process. In the present invention, all biomass generated in forests, wilderness, golf courses, farmland such as orchards and fields, freshwater and seawater (only unused biomass such as grain stems and pruned branches directly related to primary products) , Undergrowth, fallen leaves, weeds, and plants with high photosynthesis efficiency during cultivation, etc.), biomass waste such as squeezed residue and extraction residue in beverages, food processing plants, etc. Combustible municipal waste such as organic products may also be used as fuel.
The organic matter such as biomass used in the present invention may have a high water content. Examples of the water content include 0.950 or more, 0.925 or more, and 0.9 or more. Further, the water content may be 0.875 or more, 0.85 or more, and further 0.833 or more. Organic substances such as biomass that can be used in the present invention may contain those having such a moisture content, and some or all of them may include those having such a moisture content.

Conventional SCWO operations are mainly for liquids that can be supplied by high-pressure pumps, etc., or solid-liquid slurries, and the SCWO reactor (SCWO reactor) is treated with processed material, water (or supercritical water, or water as needed. A continuous reaction operation in which fuel) and oxygen or air are continuously introduced is common. In addition, for the treatment of solids contaminated with harmful substances, avoid pretreatment as complicated as possible for safety, charge the solids into the SCWO reactor batchwise, and then supercritical water and air (or oxygen ) Is circulated and burned for half-batch operation.
As a boiler for a power plant, it is desirable to operate continuously so that a stable output can be obtained. However, there is no general-purpose, inexpensive and highly reliable apparatus and method for supplying solids having various forms to a high-pressure system. Although it is possible to pulverize raw materials to such an extent that existing slurry pumps can be used for many biomasses, various pulverization methods are required depending on the form of the raw materials. There is no inexpensive and versatile method for continuous supply of biomass to a high-pressure system, such as requiring special equipment and enormous energy requirements.

The following aspects are provided in the technology of the present invention.
(1) A combustion boiler device that uses supercritical water oxidation to generate high-temperature, high-pressure combustion fluids that contain supercritical water as the main component, using high-water content organic matter such as biomass as fuel.
(2) The operation of the biomass combustion boiler device described in (1) is described below as “sealing / pressurizing”,
It is divided into operating elements such as “constant pressure / temperature rise”, “combustion / temperature rise”, “steady combustion”, “discharge / filling”, etc., and stable heat output is continuously generated, A system configuration and operation method that eliminates the need for continuous supply of solid fuel such as biomass and enables batch supply at an easy temperature and pressure.
(3) A combustion chamber in which all the fluids flowing out from the SCWO reactor are merged and unburned organic substances (organic substances mainly dissolved in hot water) contained in the flowing fluid are completely burned is provided at the rear stage of the reactor. A device that continuously generates high-temperature and high-pressure fluid and its operation method.
(4) Equipment configuration and operation method when a heat exchanger is installed in the downstream of the combustion chamber at the rear stage to generate high temperature / high pressure steam (see FIGS. 2 and 3).
(5) The latter combustion chamber is divided into two so that the intended flow path is configured, and the discharge fluid of “combustion / temperature rise” and “steady combustion” operation that can set any pressure is introduced. Unburned material is combusted as needed in one combustion chamber, and part of the generated high-temperature / high-pressure fluid is used for “sealing / pressure-increasing” and “constant-pressure / temperature-raising” operations, and the rest is introduced into the second combustion chamber. Is done. This flow and the fluid discharged at a lower temperature than the self-combustion temperature discharged by the “constant pressure / pressure-increase” operation are mixed at the entrance of the second combustion chamber, the temperature is raised above the self-combustion temperature, and unburned fuel is completely combusted in the second combustion chamber. Apparatus and operation method for obtaining heat output as a high-temperature and high-pressure fluid.
(6) The heater configuration and operation method required for the startup of the equipment described in (5).
(7) A device that injects water into the high-temperature and high-pressure fluid remaining in the SCWO reactor after completion of steady combustion, recovers heat as high-temperature water at the same time as pressure reduction, and collects combustion gases such as carbon dioxide if necessary Configuration and how to operate it.
(8) An SCWO reactor in which a heat insulating layer is provided on the inner surface of the reactor with ceramics having a low thermal conductivity in order to improve the operability and thermal efficiency of the unsteady supercritical water oxidation reaction.

In a typical embodiment, the organic (eg, biomass) combustion boiler (or combustion boiler plant or combustion boiler system) of the present invention comprises two or more SCWO reactors and a combustion chamber downstream (downstream). It is a feature. The combustion boiler includes at least SCWO reactors, which are described below, “sealing / pressure increase”, “constant pressure / temperature increase”, “constant pressure / combustion / temperature increase” or “combustion / temperature increase”, “steady combustion”, and It can be subjected to an operation selected from the group consisting of “discharge / fill”. Preferably, one SCWO reactor is connected to an SCWO reactor, which is “sealed / pressurized” → “constant pressure / temperature rise” → “constant pressure”. · It is characterized by being configured to be able to be subjected to an operation cycle consisting of “combustion / temperature rise” or “combustion / temperature rise” → “steady combustion” → “discharge / filling”, and therefore the operation The piping system valve (valve) and the fluid delivery pump provided in the combustion boiler are configured to be controllable. Thus, the combustion boiler includes an oxygen introduction piping system (which may include valves, piping (conduit), pumps, and in some cases flow meters, control devices, etc.), high-temperature high-pressure steam (from the combustion chamber to the SCWO reactor). Cooling to piping system (valve, piping (conduit), optionally pump, optionally flow meter, controller etc.), combustion chamber and / or SCWO reactor for introducing supercritical water) Piping system for introducing water (valve, piping (conduit), pump, and in some cases may include a flow meter, control device, etc.), effluent fluid from SCWO reactor is downstream (downstream) combustion chamber Piping system (valve, piping (conduit), optionally pump, optionally including a flow meter, control device, etc.), drain piping system for discharging hot water for heat recovery from SCWO reactor (Valve, piping (conduit ), Optionally a pump, optionally including a flow meter, controller, etc.), optionally a steam accumulator, turbine, drain piping system for discharging hot water from the turbine (valve, piping (conduit), optional) A pump, which may include a flow meter, a control device, etc.), a gas-liquid separator, a drain piping system (valve, piping (conduit), optionally a pump, optionally a flow rate) A meter, a control device, etc. may be included, and in some cases it is preferred.
The combustion boiler includes, for example, at least five SCWO reactors, and can be operated so that each SCWO reactor takes each operation state during steady operation. In another embodiment, it is configured on the premise that it is operated to reduce the number of reactors, for example, having at least four SCWO reactors, or having at least three SCWO reactors. May be. The combustion boiler may have a combustion chamber divided into a plurality of parts, for example, a combustion chamber having a first combustion chamber and a second combustion chamber, and / or removable for start-up. A simple heating device (heater) may be provided. A plurality of the heaters may be provided, or the heater may be provided permanently in one of the combustion chambers. When the heater is attached to the combustion chamber, for example, it is preferable that the heater is provided in the combustion chamber that receives hot water containing unburned organic matter from the SCWO reactor in the combustion chamber at the rear stage of the SCWO reactor. It is.

Specific examples (that is, examples) are given below to specifically describe the present invention, but these examples are merely provided for the purpose of describing the present invention and for reference to specific embodiments thereof. is there. These exemplifications are for explaining specific specific embodiments of the present invention, but are not intended to limit or limit the scope of the invention disclosed in the present application. In the present invention, it should be understood that various embodiments based on the idea of the present specification are possible.
All examples were performed or can be performed using standard techniques, except as otherwise described in detail, and are well known and routine to those skilled in the art.
In one specific embodiment of the present invention, a plurality of SCWO reactors as shown in FIG. 2 are sequentially cycled to enable batch supply of biomass fuel at atmospheric pressure and continuous output. A boiler plant that stably obtains the above is provided.
FIG. 2 corresponds to five operations and shows the case where five reactors are used. (It is not always necessary to assign one or more reactors to each operation, and consecutive operations may be merged according to the operation time. For example, “discharge / filling” and “sealing / pressurization” operations are changed to “discharge / filling / sealing / pressure-raising” operations, and “constant pressure / combustion / temperature rise” and “steady combustion” operations are set to “combustion / temperature rise”. • The number of reactors can be reduced if the “steady combustion” operation is synchronized with other operations.
All reactors are in an equivalent relationship, the oxygen introduction line shown in (A), the high-temperature high-pressure steam (supercritical water) introduction line shown in (B), and the cooling water introduction shown in (C). A line, a line for guiding the effluent fluid from the reactor shown in (D) to the subsequent combustion chamber, and a drain line (E) for discharging hot water for heat recovery shown in brown are connected.
Each thick line indicates a distribution state, a thin line indicates a stop state, and a valve indicates an open state and a gray state is closed. Each operation will be described in order from the state of the left end of FIG. 2 where the filling of the biomass fuel at room temperature and atmospheric pressure is completed.

  First, the operation that starts immediately after filling the raw material is called “sealing / pressurizing operation”. As shown in FIG. 2, the valves of the supercritical water introduction line are opened, the other valves are closed, and the supercritical water is sealed. To increase the combustion pressure (shown in FIG. 2 as a “closed pressure increase” reactor). Thus, subjecting the SCWO reactor to a “sealing / pressurizing” operation means pressurizing supercritical water into the SCWO reactor in a sealed state, and boosting the SCWO reactor filled with the raw material to the combustion pressure. . This operation ends when the pressure in the reactor reaches a predetermined combustion pressure, and the process proceeds to the next “constant pressure / temperature increase operation”.

This “constant pressure / temperature raising operation” shows the state of the second reactor from the left in FIG. 2, with the supercritical water introduction line and the valve of the line connecting the reactor and the combustion chamber being open, By circulating water in the reactor, the temperature in the reactor is raised to the self-combustion temperature under a constant pressure (shown as a “constant pressure rise” reactor in FIG. 2). At this time, hot water flows out according to the inflow amount of supercritical water and the thermal expansion due to the temperature rise. Most of the solid biomass is held in the reactor by a mesh provided at the reactor outlet. On the other hand, many of the biomass components composed of hemicellulose, cellulose and lignin insoluble in water at room temperature, as well as sugar, are included. Dissolve in hot water. Therefore, although the quantitative relationship varies depending on the type of biomass, the biomass component that has reached the dissolution temperature during this operation is dissolved and discharged. Thus, when the SCWO reactor is subjected to a "constant pressure / temperature increase" operation, supercritical water is circulated through the SCWO reactor, and the temperature in the SCWO reactor is increased to the self-combustion temperature of the charged raw material under a constant pressure. And hot water containing supercritical water as a main component and containing unburned organic matter is discharged from the SCWO reactor to the combustion chamber. This “constant pressure / temperature raising operation” is terminated when the self-combustion temperature is reached, and the process proceeds to the next “constant pressure / combustion / temperature raising operation”.

This “constant pressure / combustion / heating operation” shows the state of the third reactor from the left in FIG. 2, and closes the supercritical water introduction valve and opens the oxygen supply valve to burn the biomass in the reactor. (Shown as a “constant pressure combustion temperature rise” reactor in FIG. 2). The temperature in the reactor rises due to the heat of combustion, and this operation ends when a predetermined steady combustion temperature is reached. During this operation, hot water and carbon dioxide, in which the biomass components are partially dissolved, flow out corresponding to the thermal expansion due to the combustion reaction and the temperature rise. Thus, subjecting the SCWO reactor to a “constant pressure / combustion / temperature raising” operation means that oxygen is supplied to the SCWO reactor, the charged raw material in the SCWO reactor is combusted under constant pressure, and the SCWO reaction is performed. This means that hot water and carbon dioxide containing supercritical water as a main component and containing unburned organic substances are discharged from the vessel to the combustion chamber. After this operation is completed, the routine proceeds to “steady combustion operation”.

This “steady combustion operation” shows the state of the second reactor from the right in FIG. 2 and is shared with the cooling water line (in this figure, the boiler water line to maintain the combustion temperature. May be actuated) (shown as a “steady combustion” reactor in FIG. 2). In this operation, hot water and carbon dioxide, in which part of the biomass components are dissolved, flow out according to the combustion reaction. Thus, subjecting the SCWO reactor to a “steady combustion” operation means that cooling water is supplied to the SCWO reactor so as to maintain its combustion temperature so that combustion of the charged raw material in the SCWO reactor is maintained. And means that hot water and carbon dioxide containing supercritical water as a main component and containing unburned organic substances are discharged from the SCWO reactor into the combustion chamber. This operation ends when all the biomass is burned, and proceeds to the next “discharge / fill operation”.

This “discharge / fill operation” shows the state of the rightmost reactor in FIG. 2, all except the cooling water introduction valve are closed, the cooling water is injected, the temperature is lowered to the recovered hot water temperature, and the pressure is lowered simultaneously (FIG. 2). Is shown as a “discharge-fill” reactor). When the predetermined temperature is reached, the cooling water valve is closed, the drain valve (E line) is opened, and the gas pressure mainly composed of carbon dioxide is used to discharge and collect hot water and carbon dioxide. When the raw material filling pressure (usually atmospheric pressure) is reached, the biomass raw material is filled from a raw material supply nozzle (not shown in the figure, but premised on the supply of biomass at the level of ground grinding). Thus, when the SCWO reactor is subjected to the “discharge / fill” operation, the cooling water is press-fitted into the SCWO reactor, the temperature is lowered, the temperature is lowered to a predetermined temperature, and then the cooling water supply is stopped. It means that carbon dioxide is discharged and recovered, and then the raw material filling pressure is set, and then the organic raw material is supplied and charged into the SCWO reactor. More specifically, cooling water is injected into the SCWO reactor. Then, the temperature is lowered to the recovered hot water temperature, and the pressure is lowered at the same time. After the predetermined temperature is reached, the supply of cooling water is stopped, the hot water and carbon dioxide are discharged and recovered, and then the raw material filling pressure (usually atmospheric pressure) ), The biomass raw material is supplied and the SCWO reactor is charged.
At the end of this operation, one cycle (five operations) is completed simultaneously in each reactor, and all the reactors sequentially move to the next operation, and the above operations are repeated.

The effluent fluid from the reactor of the three operations of “constant pressure / temperature rise”, “constant pressure / combustion / temperature rise”, and “steady combustion” merges as shown in FIG. Mix and completely burn out spilled biomass. Cooling water is introduced as necessary so as not to exceed the steady combustion temperature.
In FIG. 2, heat exchange is performed with high-temperature and high-pressure combustion gas to generate supercritical water, which is used as a power source for the power plant. Some are used as supercritical water for “sealing / pressurizing” and “constant pressure / heating” operations. The heat exchanged combustion fluid is guided to a gas-liquid separator and separated into high-pressure carbon dioxide and waste water.

Next, FIG. 3 shows an example of the simulation of the boiler plant shown in FIG.
When five reactors are used, the “discharge / fill operation” is treated as offline for the entire combustion operation, and the time for one reactor to finish the remaining four operations is treated as one cycle.
FIG. 3 shows a simulation result when 100 kg of biomass is burned under the calculation conditions shown in the figure on the basis of absolutely dryness per hour. Each reactor will process 166.7 kg of raw material with a moisture content of 85% (absolutely dry standard biomass 25 kg) in one hour, excluding the “discharge / fill operation”. Although the reactor is different every quarter cycle in the whole operation, the same operation is repeated, so the operation speed is set so that each operation is completed in 15 minutes. The operation speed of “sealing / pressurization” and “constant pressure / temperature rise” is controlled by supercritical water introduction speed, and the speed of “constant pressure / combustion / temperature rise” and “steady combustion” operations are controlled by oxygen introduction speed. The amount of supercritical water and oxygen introduced is divided equally over time.
The operation speed of “discharge / fill” is controlled by the introduction speed of the cooling water, but it is not necessary to synchronize with other operation time, and it can be processed within 15 minutes. Although the time lapse of each operation is omitted, an example of each operation, a mixing zone and a combustion zone in a subsequent biomass combustion boiler, and a general mass balance and energy balance is shown. A net output of 474 kW is obtained based on 25 ° C and atmospheric pressure.

In the above, supercritical water (high temperature / high pressure steam) is generated by heat exchange with high-temperature and high-pressure combustion gas, and a part of the supercritical water is used for raising the temperature of the raw material. Since the boiler inherently directly generates high-temperature and high-pressure combustion exhaust fluid, it may be used directly for driving the expansion turbine.
According to this configuration, energy loss due to heat exchange can be omitted, and the heat exchanger that is the heart of the boiler is not necessary, so that the apparatus cost can be reduced.
In addition, for the use of supercritical water in the “sealing / pressure increase” and “constant pressure / temperature increase” operations, a dedicated boiler can be provided as ancillary equipment.

In another embodiment of the present invention, as shown in FIG. 4, the downstream combustion chamber of the SCWO reactor is divided into two, and the first combustion chamber is operated with “constant pressure / combustion / temperature rise” and “steady combustion” operations. Is set to be larger than the pressure in the second combustion chamber. As shown in FIG. 4, the high-temperature exhaust fluid in the first combustion chamber is used as a driving heat source for the “sealing / pressure-increasing” and “constant pressure / temperature-raising” operations. Introduced into the combustion chamber.
When the SCWO reactor is in a “constant pressure / combustion / temperature rise” and “steady combustion” operation, an arbitrary pressure can be set. Therefore, this operation is hereinafter referred to as “combustion / temperature rise” and “steady combustion” operations.
The discharged fluid below the self-combustion temperature is mixed with the high-temperature fluid from the second combustion chamber at the entrance of the second combustion chamber, the temperature is raised above the self-combustion temperature, and the outflow dissolved biomass is completely combusted in the second combustion chamber. In this plant, an incidental heat source is not required during steady operation, and the cost of the apparatus can be reduced.
In a preferred embodiment of the present plant configuration, a device for raising the temperature of the raw material to the self-combustion temperature at the start-up is applied. The device is as follows.

As shown in FIG. 5, heaters H-1 and H-2 are used at start-up.
Charge raw materials into reactors IV. Attach heater H-1 to reactor I, add water if necessary, and adjust water volume. The H-1 heater is preferably a cartridge type and should be used only during start-up operations and removed during the next filling of raw materials. An appropriate amount of water is also added to the first combustion chamber. H-1
Then, the heater H-2 attached to the first combustion chamber is turned on, and the “sealing / pressurizing operation” of the reactor I is started. At this time, the valve is opened between the reactor I and the first combustion chamber and is in a conductive state. When the predetermined pressure is reached, the process proceeds to OP-2 in FIG.
In OP-2, the discharged fluid is introduced into the first combustion chamber while the reactor I is in the “constant pressure / temperature raising operation” state.
The reactor II is in a “sealing / pressurizing operation” state. The driving heat sources for these operations are H-1 and H-2 heaters. OP-2 ends when Reactor I reaches the self-combustion temperature and Reactor II reaches the predetermined pressure, and proceeds to OP-3.

In OP-3, reactor I shifts to “combustion / temperature increase operation”, reactor II shifts to “constant pressure / temperature increase operation”, and reactor III shifts to “sealing / pressure increase operation”. When the SCWO reactor is subjected to a "burning / heating" operation, oxygen is supplied to the SCWO reactor, the charged raw material in the SCWO reactor is burned, and supercritical water is mainly used from the SCWO reactor. It means that hot water and carbon dioxide containing components and unburned organic substances are discharged to the first combustion chamber. The driving of these operations is the combustion heat in the reactor I and the first combustion chamber. H-1 and H-2 are not used in principle thereafter, but H-2 is used as necessary. The fluid discharged from the reactor II is sent to the second combustion chamber. At this time, the second combustion chamber corresponds to the “sealing / pressurizing operation”. When the reactor I reaches the steady combustion temperature and the reactors II and III reach the predetermined conditions, the process proceeds to OP-4.
Since all operations appear at this point, the valve of the line connecting the first combustion chamber and the second combustion chamber is opened, the second combustion chamber is heated to a temperature higher than the self-combustion temperature, the combustion operation is started, and the plant becomes independent. Driving begins. Reactor I is disconnected from the line, introduced with cooling water, recovered with hot water and carbon dioxide, and restored to the initial state through a “discharge / fill operation” of filling the raw materials. At this time, remove the H-1 heater.
Thereafter, by repeating this operation, the routine shifts to a periodic steady operation.

In the present specification, “oxygen” may be selected from those known in the art as oxidants, or selected from those known as oxygen sources, for example, ozone. Liquid or gaseous oxygen, hydrogen peroxide, air, compressed air, oxygen-enriched air, mixtures thereof, etc., preferably air, compressed air, oxygen-enriched air, A mixture etc. are mentioned.
The apparatus and operation method of the present invention are described above, and the present invention achieves the conversion of biomass with high water content by adopting SCWO reaction, and the raw material of biomass in various forms and shapes by adopting batch raw material supply By using multiple reactors corresponding to each operation, stable and continuous output is possible, and the system structure is simplified as much as possible, making it an indispensable device for small-scale distributed biomass combustion boilers. It was shown that it contributes to cost reduction.

The technology of the present invention is not limited to any type or form, including biomass with a high water content of about 85%. It enables high-pressure biomass boilers and is useful for use in distributed power plants that can respond to the amount of biomass generated depending on the amount generated.
The present invention covers all biomass generated in forests, wilderness, golf courses, farmland such as orchards and fields, freshwater and seawater (only unused biomass such as grain stems and pruned branches directly related to primary products) , Undergrowth, defoliation, weeds, and plants with high photosynthetic efficiency by cultivation during the rest period)
Biomass boiler plant that uses flammable municipal waste such as biomass waste such as squeezed residue and extraction residue in beverages and food processing factories, and garbage (including organic products such as plastics) as fuel Is realized.
It will be apparent that the invention may be practiced otherwise than as particularly described in the foregoing description and examples. Many modifications and variations of the present invention are possible in light of the above teachings, and thus are within the scope of the claims appended hereto.

It is a graph which shows the relationship between the moisture content and the adiabatic flame temperature when the raw material having various moisture contents is completely burned with the theoretical oxygen amount in pure oxygen. Curves are shown for combustion pressures of 0.1014 MPa (atmospheric pressure), 10 MPa, 20 MPa, 25 MPa, and 30 MPa. Raw material: cellulose, initial temperature: 25 ° C., oxidizing agent: pure oxygen, excess oxygen ratio: adiabatic flame temperature under conditions of 0.0. 1 shows a supercritical water biomass fired boiler plant with five reactors and combustion chambers corresponding to five operations according to the present invention. When supercritical water is generated. An example of the material and energy balance of the boiler plant of FIG. 2 is shown. 1 shows a supercritical water biomass fired boiler plant with five reactors and two combustion chambers corresponding to five operations according to the present invention. When high-pressure steam is not generated. FIG. 5 shows the startup situation of the boiler plant in FIG. 4. Reactor I is in the operational state of OP-1, and both heaters H-1 and H-2 are on. FIG. 5 shows the startup situation of the boiler plant in FIG. 4. The operation states following Fig. 5 are to be operated in the order of upper left figure (OP-2), upper right figure (OP-3), lower left figure (OP-4), upper right figure (OP-5). Show.

Claims (16)

Applying supercritical water oxidation (SCWO) to generate high-temperature and high-pressure combustion fluids that contain at least biomass and use organic substances with a high water content as fuel and mainly contain supercritical water. A featured combustion boiler device. It comprises at least two or more SCWO reactors and a combustion chamber for receiving a high-temperature and high-pressure combustion fluid mainly composed of supercritical water discharged from the SCWO reactor and generated by the organic SCWO. The combustion boiler device according to claim 1. The operation of the combustion boiler apparatus is at least “sealing / pressure increase”, “constant pressure / temperature increase”, “combustion / temperature increase” or “constant pressure / combustion / temperature increase”, “steady combustion”, and “discharge / fill” operations. It is divided into elements and equipped with piping and valve systems that enable each of these operations to generate stable heat output continuously and eliminate the need for continuous supply of solid fuel such as biomass to high temperature and high pressure systems The combustion boiler apparatus according to claim 1 or 2, wherein batch supply is possible at a temperature and pressure that are easy to supply. A combustion chamber is provided at the rear stage of the reactor to combine all the fluids flowing out from the SCWO reactor and complete combustion of unburned organic substances (mainly organic substances dissolved in hot water) contained in the flowing fluid. The combustion boiler apparatus according to any one of claims 1 to 3, wherein the high-pressure fluid is continuously generated. A heat exchanger is provided downstream of the combustion chamber at the rear stage of the SCWO reactor, and high-temperature and high-pressure steam can be generated through the heat exchanger. A combustion boiler device according to any one of the above. When the SCWO reactor is provided with a first combustion chamber and a second combustion chamber as the subsequent combustion chamber of the SCWO reactor, and the SCWO reactor is in the “combustion / temperature rise” and “steady combustion” operation, A piping line for introducing the unburned product-containing exhaust fluid from the SCWO reactor and the SCWO reactor in the “steady combustion” operation state into the first combustion chamber, and receiving the unburned product-containing exhaust fluid. One combustion chamber is capable of burning unburned material, and a part of the generated high-temperature / high-pressure fluid is sent to the SCWO reactor in the “sealing / pressure-increasing” operation state and the SCWO reactor in the “constant pressure / temperature-increasing” operation state. And a piping line for introducing the remainder of the high-temperature / high-pressure fluid generated in the first combustion chamber into the second combustion chamber. Exhaust flow lower than the self-combustion temperature discharged from the remainder and the SCWO reactor in the "constant pressure / pressure increase" operating state The body is mixed at the entrance of the second combustion chamber, heated to a temperature higher than the self-combustion temperature, and unburned fuel is completely burned to obtain heat output as a high-temperature and high-pressure fluid. The combustion boiler apparatus as described in any one of -5. The combustion boiler device according to any one of claims 1 to 6, further comprising a start-up heater for the combustion boiler device. After completion of steady combustion in the SCWO reactor, water is injected into the high-temperature / high-pressure fluid remaining in the SCWO reactor, and has a piping line for reducing the pressure. Combustion according to any one of claims 1 to 7, further comprising a device for recovering combustion gas such as carbon dioxide remaining in the SCWO reactor, if necessary. Boiler equipment. SCWO reactor with a heat insulating layer on the inner surface of the reactor made of ceramics with low thermal conductivity. Supercritical water oxidation (SCWO) is applied to generate high-temperature and high-pressure combustion fluids that contain at least biomass and use organic matter with a high water content as fuel and mainly contain supercritical water. A method for generating and acquiring heat from the organic material, wherein unburned organic material contained in the fluid is completely burned to generate a high-temperature and high-pressure fluid. Operating an SCWO reactor and an organic combustion boiler device having a combustion chamber located downstream thereof, the SCWO reactor
(1) Press-fit supercritical water into the SCWO reactor in a sealed state, and pressurize the SCWO reactor filled with the raw material to the combustion pressure (“sealed / pressurized”).
(2) The supercritical water is allowed to flow through the SCWO reactor, the temperature inside the SCWO reactor is raised to the self-combustion temperature of the charged raw material under a constant pressure, and the supercritical water is mainly contained from the SCWO reactor. And let the hot water containing unburned organic matter flow out into the combustion chamber ("constant pressure / temperature rise"),
(3) Supply oxygen to the SCWO reactor, burn the charged raw material in the SCWO reactor under a constant pressure, and heat from the SCWO reactor mainly containing supercritical water and containing unburned organic matter. Causing water and carbon dioxide to flow into the combustion chamber (“constant pressure, combustion, temperature rise”) or supply oxygen to the SCWO reactor, and combust the charged material in the SCWO reactor, and from the SCWO reactor Causing hot water and carbon dioxide containing supercritical water and unburned organic matter to flow into a specific combustion chamber ("combustion / heating"),
(4) Cooling water is supplied to the SCWO reactor to maintain its combustion temperature so that combustion of the charged raw material in the SCWO reactor is maintained, and supercritical water is mainly supplied from the SCWO reactor. Causing hot water and carbon dioxide as components and containing unburned organic matter to flow into the combustion chamber ("steady combustion"),
(5) Cooling water is injected into the SCWO reactor, the temperature is lowered and lowered, and after reaching a predetermined temperature, the cooling water supply is stopped, and the hot water and carbon dioxide are discharged and recovered. After that, the organic raw material is supplied and charged into the SCWO reactor (“discharge / fill”)
It is attached to each of the operating elements of the above, generating stable heat output continuously, eliminating the need for continuous supply of solid fuel including biomass to high temperature and high pressure systems, batch supply at a temperature and pressure that is easy to supply The method for obtaining and generating heat from an organic substance according to claim 10, wherein Operate an organic combustion boiler device equipped with a plurality of SCWO reactors, merge all fluids flowing out from the SCWO reactors, and batch unburned organic matter (organic matter mainly dissolved in hot water) contained in the effluent fluid The method for obtaining and generating heat from an organic substance according to claim 10 or 11, wherein a combustion chamber for complete combustion is provided at the rear stage of the reactor, and a high-temperature and high-pressure fluid is continuously generated. The method for generating and acquiring heat from an organic substance according to any one of claims 10 to 12, wherein high-temperature and high-pressure steam is generated by a heat exchanger downstream of the combustion chamber downstream of the SCWO reactor. Operate an organic combustion boiler device that has a first combustion chamber and a second combustion chamber as the combustion chamber at the rear stage of the SCWO reactor, and operate the SCWO reactor in the “burning / heating” operation state and the SCWO reaction in the “steady combustion” operation state. The exhaust fluid containing unburned material from the vessel is introduced into the first combustion chamber, the unburned material is combusted as necessary in the first combustion chamber, and a part of the generated high-temperature / high-pressure fluid is “sealed / pressurized”. This is sent to the SCWO reactor in the operating state and the SCWO reactor in the “constant pressure / temperature rising” operating state, while the remainder of the high temperature / high pressure fluid generated in the first combustion chamber is introduced into the second combustion chamber. And the exhaust fluid at a temperature lower than the self-combustion temperature discharged from the SCWO reactor in the “constant pressure / pressure increase” operating state are mixed at the entrance of the second combustion chamber, and the temperature is raised to the self-combustion temperature or higher. The fuel is burned completely, and heat output is obtained as a high-temperature and high-pressure fluid. Generation acquisition method of heat from organic matter according to any one of claim 10-13. The SCWO reactor in the first "sealing and pressure-increasing" operation state is heated with a heater to increase the pressure to a predetermined pressure in the case of start-up of the organic combustion boiler device.
The generation | occurrence | production acquisition method of the heat | fever from the organic substance as described in any one of -14. After completing the “steady combustion” operation state of the SCWO reactor, water is injected into the high-temperature / high-pressure fluid remaining in the SCWO reactor, the pressure is reduced, and heat is obtained using the resulting reduced-pressure hot water. Energy is recovered, and combustion gas such as carbon dioxide remaining in the SCWO reactor is recovered as necessary, and heat generation from organic matter according to any one of claims 10 to 15 Acquisition method.

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