TW200837310A - System for generating brown gas and uses thereof - Google Patents

Abstract

A system for the generation, storage and use of Brown gas comprising at least one Brown gas generator 116, in communication with an electricity supply 104 and water supply 102; at least one first storage chamber 122, in fluid communication with the generator, for storing the Brown gas generated from said generator 116; and Brown gas application means 146, 200, 300 in communication with said at least one first storage chamber, wherein said generator and first storage chamber are located proximate the Brown gas application means. For example, the Brown gas may be used for the production of hot water 146, for the production of chilled water 200 and as fuel in an incineration unit 300.

Description

200837310 IX. INSTRUCTIONS: I: TECHNICAL FIELD OF THE INVENTION The present invention relates to a system for generating Brownian gas and its use for different applications. L· BACKGROUND OF THE INVENTION Natural gas is commonly used in domestic and industrial applications. But the use of natural gas as a fuel to meet increasing demand, such as household and factory heating applications, is growing. Greenhouse emissions from natural gas combustion include carbon dioxide, sulfur dioxide, nitrous oxide and water vapor. In fact, natural gas combustion is considered to be one of the main environmental factors contributing to global warming. Other issues related to natural gas are: Compared to the global shortage of natural gas supply, the long-term economic feasibility and availability are problematic due to the increase in global demand. Another 15 problem is that not every country has its own natural gas source, so it is so serious that it depends on other countries to obtain natural gas. A comprehensive infrastructure network is also necessary to support the supply, storage and distribution of natural gas to end users. The pipelines and terminal networks exposed in the pre-existing area are not only expensive to establish and maintain, but also externally affecting such as natural disasters or terrorists: the price is weak. Filling the threats also ~ Instances One example is the way to incorporate this with the appropriate energy. Several alternative fuel sources have been suggested to replace natural gas. Solar energy is used to convert solar energy into usable energy. Another Brown gas, as described in US 4,081,656, is incorporated by reference. Brown gas is described as purely industrial welding and cutting. 200837310 ‘us 4, 〇81, 656 describes a method for producing oxygen and nitrogen from the electrolysis of water. The product, also known as Brownian gas, is characterized by a high calorific value of Brownian gas which can be reactively combusted with the selected metal to give off low levels of contamination. 5 The right-hand patent case describes the use of Brown gas. For example, still 6,761,558 describes a heating device for the Brown's aerothermal reaction, the contents of which are incorporated herein by reference. A description describes a method for capturing the heat of reactive combustion of Brown gas after the Brown gas has passed through the hexane liquid. 6, 443, 725 illustrates the method of circulating a heat of heat generated in a combustor to produce a single gas and burning brown gas, the contents of which are incorporated herein by reference. This = the previous description, we know that the art world needs a reliable and safe system for the use of the military and the health industry for a month, the system can cater to the increase in energy demand. Further, this shows a novel range of technologies having such advantages. 15 ^ If incineration is the most common method of destroying pathogens, viruses and toxic organisms found in most household wastes and industrial wastes. However, the incinerators are increasingly facing a number of problems. For example, incineration plants consume large amounts of fuel to burn waste. The fuel may include natural gas, acrylic or light fuel oil. The increase in global demand for natural gas and the short supply of natural gas in the world, traditional heating incineration has become an extremely expensive means of waste disposal. In order to mitigate the impact of the wood, _Chong (10) is located away from the crowd replenishment area, resulting in high transportation costs for long-distance transportation of waste, fuel and other sources of supply. Another problem is the dioxin and furan emissions caused by incomplete results during the incineration of household waste and industrial waste. This poses a serious threat to the health of the community. As a result, pressure from environmentalists has increased, and harsh regulations and regulations have been imposed on the abandonment of wastes that may cause dioxin and furan. High combustion temperature, over 12 〇 (TC, accompanied by high-disturbance mixing of waste (mixing 5 with forced air turbulence) and high residence time of flue gas for at least 2 seconds, can be effectively destroyed in the combustion chamber during incineration Dioxin and furan. Therefore, a way to ensure complete combustion of waste and reduce the formation of dioxin and furan during combustion is to modify the existing incineration process, substantially increase the temperature of the incinerator, and improve the combustion efficiency. However, the fuel consumption will increase. This results in an increase in operating costs of 10. Several alternative approaches have been suggested to achieve high combustion temperatures. One example is switching to a fluidized bed propane incinerator. Another example uses a thermal plasma incinerator that uses high energy, high strength plasma. Jets are used to destroy waste. However, these methods cannot be directly combined with existing incineration facilities. Another method is to use an alternative fuel source that is cheaper, has a higher calorific value, and has less impact on the environment. In another example, it is released into the air. Floating particulate matter and the release of flue gas are still a widespread problem. It is widely known that the release of such gases creates a significant environment and The risk of such substances may be generated by industrial processes, coal-fired and incineration plants from combustion waste (to name a few). From the results of these processes, if the emissions are not further processed, they are directly When discharged into the atmosphere, the composition of the emissions may be harmful to the environment. Controls and treatments for existing emissions and flue gases include the use of cyclones, electrostatic sinks (ESP), settling chambers, wet gas servers, And fabric filtration systems. However, to the greatest extent, these measures only help to reduce emissions and particulate matter in the pipelines of 200837310, as well as partial treatment of flue gas and emissions components. When the flue gas is discharged into the atmosphere, the flue gas of the effluent still contains harmful components that may be harmful to the environment. + σ Cyclone II has low total particle collection efficiency, especially for collection of particles less than 103⁄4 m. Although the electrostatic sinker is 'effective in handling emissions and flue gas, it is extremely expensive to install and maintain. It also requires a large installation space. In addition, during the gas release period The belt of the electrostatic sinker may generate ozone, which increases the environmental protection problem. It needs 10 15 20 » the human heart (4) electrostatic (four) device. The fabric system is also extremely mussel, when it exceeds about 29 (rc temperature Manipulating mineral fabrics or metal fabrics. In the case of accidentally generating a certain concentration of fire, there is also a risk of explosion. U is pure, and a solution ==: better need to be environmentally friendly and energy efficient means [Declaration Content 3 Summary of Invention According to a first aspect, the present invention provides a system for generating a gas comprising: f generating, storing and using a cloth - at least one Brown gas generator, the Brown water source being connected; /, generating a system and a power source and at least one first storage Room, and the Brown gas produced by the generator; and the 'for storage'

The Brown gas application device and the at least one first to the second of the generator and the first storage chamber position = pass 'nearly 5 hl Brown gas application 200837310 device.  It is to be understood that "adjacent" refers to the intended use of the present invention. For example, the use of the interior of a building requires that the definition of "adjacent" fall within the base of the building. Such as the factory room has a well-known furnace, The house has a ^ ^ 5 similar to an industrial air conditioner, Or adjacent to the outer casing of the building, Such as distribution boxes.  For different purposes, Such as for residential development. "Proximity" is included in the central location within the development of the home. This system can be compared and differentiated from conventional energy supplies such as main power, whereby power generation may be far removed from the residential development. in this way, In this case, It is a well-known infrastructure that generates and stores a well-known energy source that is located in a "far location" that requires a considerable amount of energy to be distributed. "Proximity" is defined as being within the available location. No substantial infrastructure is required until the final distribution is available for use. in this way, In the present invention, An advantage of the generator and the first storage chamber adjacent to the Brown gas application device is the increased system efficiency. This configuration relies on external energy sources. It also reduces the cost of setting up less infrastructure.  Comparing other forms of natural gas, Brown gas shows high calorific value and contaminant emissions are negligible. in this way, Brown gas is excellent for domestic and industrial use.  For example, the Brown gas produced can be used to provide a pipeline wheel for use in the following applications: 2 gas delivery, cooking and space heating; Or industrial heat treatment for the manufacturing process · laundry, Clean and hygienic, Hot water for washing; Manufacture of cooling water for space cooling; And provide decomposition of garbage, Fuel for incineration units of waste and other household waste or industrial waste.  In the second aspect, The invention provides a steel furnace for manufacturing hot water and a burner unit of 200883373, The boiler and burner unit contains:  • accept one of the first inlets for feed water;  - accepting a second inlet from the Brown gas of a Brown gas generator; And 5 - one of the hot water produced by the discharge,  According to yet another embodiment, The applicator includes at least one first chamber for producing hot water, The heat in which the hot water is heated is derived from the combustion of Brown gas. The Brown gas system is obtained from at least one first storage chamber. particular, The at least one first chamber can be a boiler and burner unit. At least one first room contains:  10 • for receiving one of the Brown gases by the at least one first storage chamber first into π;  - accepting one of the second inlets of water;  - a gas burner; And - one of the outlets for the hot water produced by the discharge,  15 wherein Brown gas from the first inlet is combustible by the gas burner, Thereby heating water from the second inlet; And wherein the heated water can be discharged from the outlet.  A second inlet for receiving water may be coupled to at least one heat exchanger outlet contained within the at least one Brown gas generator.  A second inlet for receiving water may also be connected to the outlet of at least one solar heat collector.  In front of the first entrance, At least one flash arrester can be provided. The flash arrester includes a volatile gas such as hydrogen, a device on the supply line of acetylene and other fuel gases, The flash fire suppressor is used to prevent the flame from being transmitted to the supply source. All the priests ^ 0 ^ Rolling stock tank or gas generator. For the purposes of the present invention, The flash fire suppression state may be installed in a plurality of ignition ignition portions of the Brown gas supply to be filled with the liquefied hydrocarbon gas as the at least one γ-containing γ ^ to further include a reactive metal component. E.g, Reactive metal components that can be used for at least _th" rides include, but are not limited to, any of the following: surface, Fine steel, Nickel-chromium alloy or other high temperature nickel alloy.  The reactive metal component can be in the form of a single curved shell or a hyperbolic shell. There are perforations on the surface of the housing to maximize the contact area between the metal component and the Brown gas flame. Recording - Chromium alloy can be in the form of a nickel route. Reactive metal components can be placed on the flame path of the flame to perform reactive combustion. Into the step - step to increase the flame temperature of the second chamber.  The system of the present invention further includes at least one second storage chamber, The second storage compartment is for storing hot water produced by the at least one first chamber. Such as 15 this, The at least one second storage chamber can be coupled to the at least one first chamber outlet. The hot water produced can be stored in the storage room for heating in the future space. Washing clothes, Clean and wash.  According to yet another embodiment, The applicator further comprises at least one second chamber for making cooling water. Special 20 but unit.  The at least one brother room may be absorbing cold. The at least one second chamber comprises:  Receiving a first inlet of an absorbent - receiving a second inlet of a refrigerant;  - receiving a third inlet of cooling water;  11 200837310 - Accepting one of the fourth entrances to warm water,  a first heat exchanger;  a second heat exchanger;  - one of the first outlets for discharging warm water; And 5 - one of the second outlets of the cooling water produced by the discharge,  The third inlet and the first outlet are connectable to the first heat exchanger. And the fourth inlet and the second outlet are connectable to the second heat exchanger.  The absorbent can be lithium bromide (LiBr), Ammonia (NH3) or other suitable absorbent, A desiccant or dehumidifying agent such as is apparent to those skilled in the art. Refrigerant 10 can be water. Other suitable refrigerants can also be used for the purposes of the present invention.  At least one second chamber can utilize heat to vaporize the refrigerant and the absorbent. To perform a cooling cycle, The heat is generated by a heat exchanger flowing from one of the hot waters of at least the second storage chamber. Or the heat generated by the combustion of the Brown gas directly from at least one of the first chambers.  15 due to the cooling cycle results, Water from the at least one second chamber is cooled. The manufactured cooling water can be stored in at least one third storage chamber. Cooling water can be used in a variety of applications. For example, for space cooling. particular, Cooling water from the at least one third storage chamber can flow into an air handling unit to provide space cooling. The air handling unit includes a heat exchange unit 20 with a blower.  According to yet another embodiment, The applicator of the present invention further comprises at least one third chamber of combustion waste. particular, The at least one third chamber is an incineration unit. The at least one third chamber comprises:  - burning a unit of combustion waste by burning Brown gas;  12 200837310 _ a connection for receiving waste to the combustion unit - a connection for receiving a second inlet from the at least one first storage chamber to one of the combustion units; And being connected to the outlet for discharging the flue gas produced by the combustion unit with one of the 5 combustion units.  The waste can be separated into solid waste and liquid waste. Waste can enter, A combustion unit is previously treated to reduce the water content of the waste.  , Feeding 10 15 The system according to the invention also comprises a heat exchanger for discharging flue gas having a lower temperature to the outlet. In addition, The system according to the present invention includes a _ a gas trap connected to an outlet connected to the thief unit, 俾 quenching the temperature of the flue gas emitted by the outlet, And/or remove particles and fly ash from the flue gas. The wet scrubber treats the gas stream to remove sub-micron or larger fly ash. The wet scrubber can have a series of high volume spray nozzles to provide rapid quenching of the flue gas discharged from the outlet. For example, The flue gas can be quenched to 200 ° C to 300 ° C. It can prevent the formation of dioxin and furans in the air. The outlet can also be connected to an air filtration system. There is an incinerator inside the system, which is excellent. Hazardous waste can be disposed of without delay. This avoids harmful emissions to the environment. Incinerators can also be assembled into waste to energy incinerators. The heat of combustion of the waste is thereby recovered for the production of water vapor or power generation.  2〇 According to the second aspect, The present invention provides a boiler and a burner unit for producing hot water. The boiler and burner unit comprises:  - accepting one of the first inlets of the feed water;  _ accepting one of the Brownian gas imports from a Brown gas generator; And 13 200837310 - one of the hot water exports from the discharge,  Where the Brown gas is burned to generate heat, This heat heats the feed water to make hot water.  The outlet for the hot water produced by the discharge can be connected to one of the 5 hot water storage tanks manufactured by the storage. The first inlet of the boiler and burner unit can be connected to: An outlet of the first heat exchanger of one of the Brown gas generators; At least one outlet of the solar heat collector, And/or the storage tank for storing the hot water produced.  In the third aspect, The present invention provides a system for recovering heat generated by combustion of a combustion material 10, contain:  - at least one Brown gas generator, It is connected to a power source and a water source;  - at least one first storage chamber for storing Brownian gas produced by the generator in fluid communication with the generator;  At least one combustion chamber for communicating the combustion material with the at least one first storage chamber 15; And - at least one heat culling chamber adapted to receive heat generated by the combustion chamber from the combustion chamber,  Wherein the generator and the first storage chamber are located adjacent to the combustion chamber and the thermal chamber.  20 In a fourth aspect, The present invention provides a method of recovering heat generated by combustion of a combustion material, The method consists of the following steps:  - a combustion material that is burned in the at least one combustion chamber by burning Brown gas; And - receiving the flue gas produced by the combustion chamber for recovering heat therein.  14 200837310 The at least one Brown gas generator utilizes electricity to hydrolyze into oxygen and hydrogen during electrolysis. At least one Brown gas generator can include an electrolysis chamber. A mixture of oxygen and hydrogen may be piped to the at least one first storage chamber. The at least one first storage chamber may contain a predetermined amount of liquefied 5 hydrocarbons, It can be used as a flame coolant. For example, The liquefied hydrocarbon may be selected from the group consisting of: Hexane, Heptane, Methanol, Ethanol, And their combinations.  Liquefied hydrocarbons can be kept at low temperatures. For example, it is maintained at a temperature below the boiling point of the hydrocarbon. Cooked artisans understand the proper storage temperature of the hydrocarbons applied, This storage temperature is common knowledge. For example, The temperature is from 20 ° C to 10 ° C. particular, The temperature 10 is 10 ° C to 20 ° C. particular, When the hydrocarbon used is hexane, The temperature is 20 °C. The liquefied hydrocarbon system acts as a catalyst to modify the flame temperature of the Brownian gas. particular, The liquefied hydrocarbon can be hexane.  According to yet another embodiment, The waste is burned in the at least one combustion chamber. The at least one combustion chamber uses Brown gas as a fuel. Brown gas 15 is obtained from the at least one first storage chamber. particular, The combustion chamber can be an incineration unit.  The combustion chamber can be a single-stage configuration or a multi-stage configuration. The at least one combustion chamber can include:  - burning a unit of combustion material by burning Brown gas;  - a first inlet for receiving a connection of the combustion material to the combustion unit;  20 - for receiving a connection of Brown gas from the at least one storage chamber to a second inlet of the combustion unit; And - for discharging the flue gas produced by the combustion unit to an outlet of the combustion unit.  The burning material can be waste, waste, Garbage and other household waste or 15 200837310 pen burners further comprise a pre-processing unit, Used to feed the combustion material to the combustion unit, The combustion material is pretreated. The combustion material can be separated into solid combustion materials and liquid combustion materials by a knife. The combustion materials can be sorted to remove recyclable non-combustible materials and hazardous combustion materials.  5 The combustion material can be pressed and/or dried to reduce the water content in the combustion material. 0 The combustion material is burned in the combustion unit. The combustion material is fed to the combustion unit by any suitable field. E.g, The combustion material can be fed into the combustion unit by gravity or mechanical means. The combustion unit may comprise a Brown gas burner 1 burner. A high temperature flame is projected into the combustion unit to burn the combustion material. The combustion unit also contains an additional entrance. 俾 Allow fresh air to be supplied to the combustion unit for a more complete combustion of the combustion material. The combustion unit can be lined with refractory material. To maintain the high temperature inside the combustion unit. The non-combustible material charred by the combusted combustion material may be collected in the combustion unit and removed by the combustion unit for disposal. Combustion materials after combustion and charred non-combustible materials can be further processed prior to disposal.  In addition to the combustion unit, The combustion chamber also contains a reoxidation chamber. Reoxidation until the flue gas is released into the atmosphere, A hot scrubber for flue gas produced in a combustion unit. For example, The flue gas produced by burning the combustion material in the combustion unit can be oxidized in the reoxidation chamber. Further clarification of flue gas or oxidizing flue gas becomes a form that is less harmful to the environment. The reoxidation chamber can also be operated using Brown gas. The reoxidation chamber therefore contains a Brown gas burner to heat the flue gas to the appropriate temperature. For example, The heating temperature of the flue gas may be the reduction reaction temperature of the flue gas component. This temperature can be 16 200837310 1〇〇〇°〇 to 2_. (: . In particular, the temperature can be 1_. (: To 1500. (: .  In order to further reduce the emission of nitrous oxide, The Brown gas burner in the reoxidation chamber can be burned using a mixture of pure oxygen and brown gas instead of using fresh air. The high nitrogen content in fresh air may react at high temperatures to form oxygenated nitrous oxides. Nitrous oxides may be harmful to the environment.  Reoxidize to the closable-grid square. The grid block can be set to directly contact the Brown gas flame in the reoxidation chamber to reach a high temperature. The grid cubes can be supported on a metal frame. The grid blocks can be made of any suitable material. E.g,  Grid squares can be surfaced, stainless steel, Made of nickel-chromium alloy or (iv) each alloy. The flue gas input by the 10 combustion unit allows it to pass through the heated glow grid. To perform a thermochemical reaction, It completely oxidizes the flue gas component of the flue gas, Such as carbon monoxide, Nitrous oxides and other particles. The treated flue gas can be used in other applications of the system of the present invention, It may be further processed before being discharged into the atmosphere.  15 In the multi-stage configuration of the combustion chamber, Such as a secondary combustion chamber, The combustion material can be burned in an insufficient air condition in the combustion unit. 俾 Manufacture of flue gas,  The flue gas contains carbon dioxide gas, water vapor, Carbon monoxide gas, Hydrogen and hydrocarbon compound gases. The flue gas is then directed through the conduit to the reoxidation chamber. The re-chemical chamber can supply sufficient air conditions and oxygen-rich conditions to further oxidize the various components of the flue gas.  In order to ensure that the flue gas produced is guided out of the combustion unit by means of a conduit,  The combustion unit and the reoxidation chamber are maintained at an appropriate negative pressure. E.g, The pressure is _50 Pa (Pa). The negative pressure can be maintained by installing a suction fan at the outlet of the combustion unit.  As explained above, Combustion of the combustion material in the combustion chamber, Making cigarettes 17 200837310 Road gas. The heat from the flue gas is used for other applications in the system. For example, The produced flue gas can be directed to at least one hot extraction chamber. Special, The at least one hot extraction chamber can be a boiler unit or a dryer.  The boiler unit can be used to make water vapor, The heat that is used to make the water vapor is derived from the flue gas that is directed to the boiler unit. Any suitable boiler unit can be used. The boiler unit can be designed. Therefore, the flue gas that does not exceed the predetermined temperature is included. The flue gas is allowed to flow at a predetermined minimum volume flow rate. In this case, The blower can be installed at the inlet of the boiler unit. To reduce the temperature of the flue gas that is turned in, And increase the volumetric flow rate of the incoming flue gas. For example, in 10 words, The boiler unit can be in the form of a metal tube counterflow heat exchanger boiler unit. The at least one hot extraction chamber can include:  - a water inlet;  • a flue gas inlet that receives the flue gas produced by the combustion unit;  - discharging the first outlet of one of the water vapors produced; And 15 - one of the second outlets for the flue gas,  Therefore, the water from the water inlet is heated by the flue gas from the flue gas inlet to generate water vapor. And wherein the water vapor is discharged from the first gas outlet, and the flue gas system is discharged from the second gas outlet. in this way, The flue gas inlet of the at least one hot chamber may be connected to the outlet 20 of the at least one combustion chamber.  The feed water entering the hot extraction chamber is available from one of the water sources inside the system. The feed water in the heat extraction chamber absorbs heat from the flue gas generated by the combustion chamber to form water vapor. The water vapor can be raised to the water vapor drum for further heating by boosting to produce super hot water vapor.  18 200837310 The feed water entering the 7/slow heat extraction chamber can be preheated in the combustion chamber. The water pipe can be heated at the top of the combustion chamber and along the wall. For example, At the end of the year, the heart comes from the heat of the flue gas produced by the combustion chamber or: Dew =: Hey. The feed water inside the pipe can be twisted by convection heat or 5 radiant heat. The volumetric flow rate of the feed water in the pipe can be controlled to The water is heated to about 赃 or the feed water heated by 卞° can then be sent to at least one heat and the chamber for the manufacture of water vapor. According to yet another embodiment, The system of the present invention further includes a power generating device in communication with the at least one first chamber. The power generation device! 〇 can contain:  - at least one steam turbine adapted to receive water vapor produced by the at least one first chamber;  • at least one generator for power generation in communication with the at least one water vapor turbine; And 15 - means for discharging electricity produced by the generator.  Water vapor from the at least one heat extraction chamber, such as a boiler unit, rotates the turbine, Manufacturing mechanical energy, Mechanical energy is converted into electrical energy by the at least one generator,  By t, And the electricity generated therein is discharged. Any suitable water steaming can be used. For example, The steam full wheel can be a single stage steam or a steam turbine. Water vapour or super hot water vapour is supplied to the water vapour = the turbine can be adjusted by the control system. For example, Water vapor is supplied to the water ... The air ball can be adjusted by changing the flow rate of the feed water turbine unit.  The generated electricity can be supplied to the at least one Brown gas generator for Brownian pain. And/or supply a power grid. Therefore, one of the advantages of the system of the present invention 19 200837310 is that electricity is generated by steam. Reduces reliance on external power supplies.  The system further includes a heat exchanger in communication with the at least one water vapor full wheel. particular, The heat exchanger can be a cooling unit. The heat exchanger can comprise:  5 - for receiving a water vapor inlet of one of the water vapors from the steam turbine; And - a water outlet,  Wherein the heat exchanger cools the water vapor received by the water vapor inlet, Thereby condensing water vapor to produce water; And the water system is discharged from the water outlet. The water discharged from the heat exchanger can be recycled inside the system. For example, The water discharged from the heat exchanger can be used as the feed water fed to the boiler unit.  A heat exchanger can also be in communication with the at least one heat extraction chamber. particular, When the steam turbine reaches its maximum capacity, The water vapor produced by the turbine unit can be directed to the heat exchanger to be cooled to water. in this way, The heat exchanger can include a second air inlet. When the steam turbine reaches its maximum capacity,  The second air inlet is adapted to receive water vapor produced by the at least one heat extraction chamber.  According to yet another embodiment, The at least one hot extraction chamber may comprise a drying device, Used to burn combustion materials in the combustion chamber, The burning material is dried.  For example, At least one of the heat extraction chambers may form part of a prior processing unit of the combustion chamber as previously described. particular, Before the combustion material is burned in the combustion unit, The dryer reduces the water content of the combustion material. The heat for drying the combustion material in the at least one heat extraction chamber may be derived from the flue gas discharged from the combustion chamber 20 200837310. So the flue gas from the job room can be guided to dry. The flue gas from the helium unit can also be directed to a dryer for drying the crucible (4). The dry field (4) is used in the combustion chamber to burn in the combustion chamber.  , , The outer sputum is contained before the flue gas is released into the atmosphere. The post-processing unit used to treat the flue gas. in this way, From the combustion chamber, Drying and / or steel furnace single 7 ° flue gas can be directed to the post-processing single it. Post-treatment = 70 can contain at least one reoxidation chamber, ― wet service gas ^, And/or a sudden cold 10 15 20 2 again, a chemical chamber such as the aforementioned reoxidation chamber, By the burning of Brown gas and the heat of the genus; The gas is used to treat the gas stream to remove sub-micron or larger gas ash. Device. Wet I gas turbines can have - (four) large-capacity water spray nozzles to mention Rapid quenching of the flue gas discharged from the gas outlet. E.g, Flue gas: : : : To 20 (rc to 30 (rc. This can be suppressed from re-formation in the atmosphere. The air outlet can also be connected to the -air transition system = the temperature of the flue gas discharged from the air outlet is reduced and/or the smoke is removed. Granules and fly ash in milk.  According to a second aspect, The present invention provides a method of burning heat generated, The branch comprises a lower combustion material fuel, a second combustion gas, and a fuel in at least one of the combustion chambers - a flue gas generated by the combustion chamber is used to recover the heat of the center. 1 Method 2 - Step package: The step of making water vapor in a steel furnace, The heat used by the money is derived from the flue milk produced by the combustion chamber. Water money can be secreted to connect with the power generator - water plug gas, Horse 21 200837310 Wheel 0 The method further comprises the step of drying the combustion material prior to combustion in the at least one combustion chamber, Therefore, the heat that dries the combustion material is derived from the flue gas produced by the combustion chamber.  5 In a fifth aspect, The present invention provides an assembly for treating a flue gas before it is discharged into the atmosphere. contain:  - at least one processing chamber for receiving and heating the flue gas;  - burning Brown gas to supply heat to the flue gas heating device; And - discharging part of the heated flue gas.  10 In a sixth aspect, The present invention provides a method of treating flue gas prior to discharge into the atmosphere, Contains the following steps:  Providing flue gas to the at least one processing chamber;  • Provide Brown gas to a Brown gas burner; And - heating the flue gas to a predetermined temperature by burning the brown gas.  15 The Brown gas burner can be a Brown gas burner. Any suitable broth burner can be used for the purposes of the present invention. The Brown gas burner can project a high temperature flame into the processing chamber to heat the flue gas. The processing chamber also contains a further air inlet. The fresh air is supplied to the processing chamber. The processing chamber can be supplied with sufficient air and oxygen conditions to further oxidize the flue gas components. The processing chamber can be tempered with a refractory liner to maintain the high temperature in the processing chamber. When the flue gas is heated, The flue gas can be oxidized in the treatment chamber. To further decompose or oxidize into a component that is less harmful to the environment. E.g, The flue gas can be heated to an appropriate temperature. The flue gas can be heated to the ignition point. The temperature at which the flue gas is heated can be higher than the temperature. particular, The flue gas can be heated to move. (3) The temperature of (4).  22 200837310 pieces, a medium force: Included in the at least one structure of at least one processing chamber, 5 10 15 20, plus 2^^, ^ County reading money flue gas steel 戟, Rod, Even a component contains a sieve,  particular, The component, Or a combination thereof. The member can be made of a suitable material.  At least one, Two 3 - grid square, The grid cube is covered in gold or gold. Grid squares can be imported, steel, Lock-road alloy,  Made of Brown in the room. The member can be placed in direct contact with the projection such as ===. Components can be carried on the branch _ smoke, First - & Look for the metal bracket. Entering the chamber allows it to pass through the heated components for higher heating efficiency. Executing the flue milk allows it to pass through the heated glow grid cubes. To gasify the sub-reaction and completely oxidize the flue gas component, Such as - carbon oxide,  Particles in other and other flue gases. Treated flue gas is available, , 匕k, Or proceed to discharge into the atmosphere and follow the steps.  One or more processing chambers may be included in the assembly.  , , One — ^ _ __丨 ,  Handle ~ stick or eight treatments to have two treatment chambers. There are multiple points to the point where the residence time of the heated flue gas increases. This results in complete oxidation of the flue gas components. When there are more than one processing room, At the same time, the financial system is connected in series. Let the gas pass through the two processing rooms.  The flue gas heated by the spoon can be used for other purposes. in this way, The assembly is further a room for the military. The heat pulse chamber is adapted to receive heated flue gas from the at least one processing chamber. particular, The hot no room contains _ early yuan. Further system, The thief taking room contains a steam steam furnace unit.  23 200837310 The heat extraction chamber contains a boiler unit for the manufacture of steam. Thus, the heat of the manufacture of water vapor is derived from the heated flue gas directed from the at least one processing chamber to the boiler unit. Any suitable boiler unit can be used. E.g,  The boiler unit can be in the form of a metal tube or plate type counterflow heat exchanger boiler unit. The hot extraction room contains:  a water inlet;  - a water vapor outlet; And - a flue gas outlet,  The heat is not configured to allow the flue gas to heat the water to produce water vapor. Special 10, The water from the water inlet is heated by the flue gas from the at least one processing unit. Thereby producing water vapor; And wherein the water vapor and the flue gas system are discharged from the water vapor outlet and the flue gas outlet respectively.  The feed water fed into the boiler unit can be obtained from a water supply source. The feed water in the boiler unit absorbs the heat 15 of the flue gas produced by the at least one processing chamber to form water vapor. The water vapor rises to the water vapor drum, To further produce super hot water vapor by heating under pressure. The feed water fed to the boiler unit can be preheated. E.g, The feed water pipe can travel on the roof of the at least one processing chamber and along the wall surface. Exposing the tubes to heat from the flue gas fed to the processing chambers, Or exposed to heat inside the treatment chamber. Feeding inside the pipe 20 Water can be heated by convection heat and radiant heat. The volumetric flow rate of the feed water inside the tube can be controlled so that the water is heated to about 90 ° C or below. The heated feed water pump is then sent to the boiler unit for the manufacture of water vapor.  According to yet another embodiment, The system of the present invention further includes a power generating device in communication with the at least one first chamber. The power generating device 24 200837310 can include:  - at least one water vapor turbine adapted to receive water vapor generated by the hot chamber;  - at least one generator for power generation in communication with the at least one steam turbine; And - means for discharging electricity produced by the generator.  10 15 The steam from the special steel furnace unit of the heat and the room is turned to the full wheel. Manufacturing mechanical energy, Mechanical energy is converted into electrical energy by the at least one generator, Use this to generate electricity, And the electricity generated therein is discharged. Any suitable water vapor full wheel can be used. For example, The water I (four) wheel can be a single stage steam turbine or . Record the field or super hot water vapor supply to the steam full wheel: Borrow - control system adjustment. For example, The water vapor is supplied to the steam vortex 2 by changing the flow rate of the feed water flow W unit. The resulting confession is used to generate Brownian gas. And / give a force grid. Therefore, the system of the present invention is superior (4): Electricity, Reduces reliance on external power supplies.  ,  The exchange i step consists of communicating with the at least one steam thirst wheel to teach and benefit. particular, Hot swap write ... contains · & It is ^^ early 7^. The heat exchanger can receive water from the steam turbine and one of the first air inlets of the steam.  Wherein the heat exchanger water system is discharged by water.  Condensing water vapor to produce water; And wherein the water discharged from the heat exchanger can be looped inside the assembly 25 200837310. For example, water discharged from a heat exchanger can be used as feed water for the boiler unit. in this way, The water outlet of the heat exchanger can be coupled to the water inlet of the hot chamber.  The heat exchanger can also be in communication with the heat extraction chamber. Especially when the steam turbine reaches 5 to the maximum capacity, The water vapor generated by the steel furnace unit of the heat-free chamber can be guided to a heat exchanger to be cooled into water. in this way, The heat exchanger can include a second air inlet. When the steam turbine reaches its maximum capacity, The second air inlet is adapted to receive water vapor generated by the hot chamber.  The assembly of the present invention also includes a post-processing unit, The flue gas is further processed before the flue gas is discharged into the atmosphere. E.g, The aftertreatment unit can be a scrubber assembly. The scrubber assembly may include a flue gas scrubber. The scrubber assembly is adapted to receive the flue gas from the flue gas outlet of the heated flue gas and/or the flue gas outlet of the hot fetch chamber. particular, Flue gas : The gas device is a scrubber.  Any suitable scrubber can be used. E.g, The scrubber can be a wet scrubber,  15 thin waist pipe scrubber, Ejector plate scrubber or spray tower scrubber. The flue gas scrubber unit contains a gravity settling chamber and a mechanical collector.  Importantly, The flue gas scrubber moves the particles from the flue gas to the liquid stream. To reduce the amount of particles in the flue gas. So before the flue gas is released into the atmosphere, Reduce the particulate matter content in the flue gas. The flue gas scrubbing 20 unit removes particulate matter having an average diameter of about 3 microns or more. The flue gas scrubber can collect particulate matter and gaseous pollutants simultaneously from the flue gas. The gas can be removed by absorption or by chemical reaction. E.g, In the scrubber, The particulate loaded flue gas is forced to contact liquid droplets or liquid flakes on the fill material or liquid jets from a plate. Wet scrubber in pellets 26 200837310 The ability to remove particles from a gas stream is determined by the following variables:  - particle size, That is, the aerodynamic diameter;  - particle velocity; And / or - droplets, Sheet or spray speed.  5 (4) The listening device includes a front W or a final filter.  To step in and remove the particulate matter inside the flue gas. E.g, It can be installed upstream of the gas processor. It is intended to capture ageing materials with a larger average diameter. The gas eliminator itself can also remove such larger particulate matter. Remove larger particles before the gas flows through the gas distributor. Allow the gas purifier to fall more: And 2 10 is effective to concentrate on particulate matter having a smaller average diameter. The final filter can be installed downstream of the gas depressor. The finalizer is intended to capture particles that have not been removed during the duty cycle.  By removing sub-micron or larger fly ash from the gas stream, The wet gas processor can handle the gas flow. In addition to removing particulate matter from the gas stream, the wet gas service 15 It can also quickly quench the flue gas. E.g, Wet gas servers can have a series of high water spray nozzles to provide rapid quenching of the flue gas.  The scrubber assembly step includes means for cooling the flue gas before it is vented to the atmosphere. Any suitable flue gas cooling device can be used. For example, a flue gas cooling device is a quench. The flue gas cooling unit cools the flue gas to a temperature below 30 (TC). The advantage of cooling the flue gas before it is released into the atmosphere is, It can prevent the formation of Dioxin and the biting in the atmosphere. The cooling unit can be connected to the air filter system. To further remove particulates and fly ash from the flue gas.  According to the second aspect, The present invention provides a method for controlling flue gas before being discharged into the atmosphere 27 200837310, Contains the following steps:  Providing flue gas to the at least one processing chamber;  - providing Brown gas to a Brown gas burner; And - heating the flue gas to a predetermined temperature by burning the brown gas.  5 the heating step is included in the presence of at least one component for achieving higher heating efficiency, Heat the flue gas. The predetermined temperature can be higher than 700 °C. The Brown gas burner can be a Brown gas burner.  According to a particular embodiment, Flue gas is supplied to three processing chambers, The flue gas passes through three individual processing chambers in sequence. particular, The method consists of the following steps:  10 _ flue gas is supplied to a first processing chamber;  - By burning Brown gas, Heating the flue gas in the first processing chamber to a first predetermined temperature;  - directing the heated flue gas from the first processing chamber to the second processing chamber;  15 - by burning Brown gas, Heating the flue gas in the second processing chamber to a second predetermined temperature;  - directing the heated flue gas from the second processing chamber to the third processing chamber; And - by burning Brown gas, The flue gas in the third processing chamber is heated to a third predetermined temperature.  E.g, The first predetermined temperature can be about 800 °C. The second predetermined temperature can be about 1000 °C. The third predetermined temperature can be greater than 1200 °C. In particular, the third predetermined temperature may be about 1600 °C.  The method further includes the step of producing water vapor in the hot extraction chamber,  28 200837310 wherein the heat of the manufacture of water vapor is derived from heated flue gas. The produced steam can be fed to at least one water vapor turbine in communication with the generator for power generation.  The method further includes the step of further processing the heated flue gas. E.g, The method consists of the following steps:  - flue gas heated by scrubbing in a flue gas scrubber; And/or - cooling the heated flue gas in a flue gas cooling device.  The flue gas can be cooled to an appropriate temperature. For example, the flue gas can be cooled to a temperature below 300 °C.  10 Brief Description of the Drawings The present invention will be further described with reference to the accompanying drawings. The drawings illustrate possible configurations of the invention. Other configurations of the present invention are also possible, The specification details of the figures are in no way intended to limit the invention.  Figure 1 is a schematic illustration of a system in accordance with one embodiment of the present invention.  Figure 2 is a still further embodiment of the present invention, A schematic of an absorption chiller.  Figure 3 is a still further embodiment of the present invention, An indication of an incineration unit.  Figure 4 is a still further embodiment of the present invention, A localization that directs Brown gas and 20 hot water and cooling water to a multi-storey building. Schematic diagram of the storage and delivery system.  Figure 5 is a still further embodiment of the present invention, A schematic diagram of a system.  Figure 6 is a view showing still another embodiment of the present invention, A schematic diagram of a system utilizing heat from a flue gas produced by burning 29 200837310.  Figure 7 is a still further embodiment of the present invention, A schematic diagram of a system utilizing heat from a flue gas produced by a combustion chamber.  Figure 8 is a still further embodiment of the present invention, An illustration of the assembly 咅 5 figure.

[poor way; DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Figure 1 shows a portion of a separation system in accordance with one embodiment of the present invention. In particular, the invention shows the generation of Brownian gas and the use of Brownian gas in a boiler and burner unit 10 in a separate system. Brown gas is produced in the Brown gas generator 116, One form of the Brown gas generator 116 is illustrated in U.S. Patent No. 4, 081, No. 656. Generator 116 includes an electrolysis chamber. A power source i〇4 is connected to a control panel 1〇6, The panel monitors and controls operating parameters, The power supply to the generator 116 is monitored and controlled via a power line 114, such as by monitoring and controlling. Also 15 Set a water supply source 1〇2. The water supply source 102 can be in the form of a water storage tank. Water from the water supply source 102 passes through a reverse osmosis (RO) water filter, The RO water after the transition is stored in the RO tank 110. The water from the R0 tank 11 is fed into the generator 116 by a pump 112.  result, The generator 116 takes in RO water and electricity to dissociate 20 oxygen and hydrogen during the electrolysis process. The resulting mixed gas of oxygen and hydrogen is pumped through line 121 to a Brown gas storage tank 122. Generator 116 further includes a heat exchanger 118. The immediate by-product of the electrolysis process is the heat derived from the hydrolysis to its constituents. The heat exchanger 118 is cooled by water. The water system is supplied to the heat exchanger 118 through the line 152 from the water supply source 1〇2. Subsequently, The preheated water manifold 30 200837310 The road 154 flows out of the heat exchanger 118.  The Brown gas storage tank 122 is partially filled with liquefied hydrocarbons. In this case, the liquefied hydrocarbon is hexane 124. A hexane storage tank 126 is also provided. The burned m from the burned storage tank m is pumped into the Brown gas storage tank 14 by the pump (2). The mixture of oxygen and hydrogen is mixed with the (tetra) gas to form a Brownian gas 120° Brown gas storage tank 122. The step is assembled with a width of 128.  Control panel 106 also monitors and controls other operational parameters, For example, the water of the ruler is supplied to the generator 116 by the RO water tank 11 The appearance 124 is supplied to the gas pressure of the inside of the Brown gas storage tank 122 generator 116 and the Brown gas storage tank 122, Producing an operating temperature of 10, 116 And the flow rate of the mixture of oxygen and gas from the generator 116.  Brown gas 120 from Brown gas storage tank 122 can be supplied directly to the end user via line network 130. The line can be fitted with at least one check valve 132 to ensure that the flow of gas is only in one direction. The pipeline 13 further includes a pressure regulator 133, a control valve 134, And a flash fire suppressor 136. In addition to the direct supply of Brown Gas 120 to the end user, Brown gas 12 〇 can also be supplied to a furnace to the burner unit 146 for the production of hot water.  particular, Brown gas 120 is supplied to burner 148 of burner unit 146 via line 138. The line 138 includes a check valve 140, a pressure regulator 14ι, a 20 control valve 142, And a flash fire suppressor 144. The burner 148 is equipped with a gas ignition device, Flame and flame style control device, Standard for gas detectors Industrial gas burners. The burner 148 is operated on the Brown gas 120. The burner 148 has a motor driven blower, The gas supply solenoid valve and a gas nozzle. The burners 148 are assembled to produce a flame of up to 1 Torr (TC temperature. Burner 31 200837310 148 Projects the flame into the pin furnace.  The boiler 150 has a cylindrical structure. There is space inside to cover the water pipe bundle (not shown). The feed is to be supplied to a pin furnace for heating to produce hot water feed water. In addition, Inside the boiler 150, a layer of reactive metal elements, The layer 5 metal element is placed on the path of the flame burning Brown gas 12 〇 to perform reactive combustion. Help to further increase the flame temperature. The hot gas produced by the combustion of the Brown gas 120 in the burner 148 contacts the water tube bundle, As a result, the feed water inside the water pipe is heated. In order to maintain the heat of combustion as much as possible, The boiler 150 is externally coated with a layer of insulating material. The heat from the burner 148 burning the hard gas 120 is used to heat the feed water for the steel furnace 150. Hot water is produced by the cockroach.  The feed water to the feed steel furnace 150 comes from three sources. the first, Water supply source 102 is used as makeup water. The water is pumped into the furnace by pump 158 along line 156. second, The preheated water is passed through the line 154 discharged from the heat exchanger 118 in the Brown gas generator 116. third, As the preheated water in the line 157 discharged from at least one of the solar energy collectors 159. The at least one solar heat collector 159 takes in water from the water supply source 〇2, The preheated water is discharged via line 157 to the boiler and burner unit 146. particular, From the pipeline 154, 156. The water of 157 and 157 are combined and pumped into boiler and burner unit 146 by pump 158. The hot water produced by boiler 150 can be used for space heating, Hygienic use and washing use. The hot water produced by boiler 150 is used for space heating 'sanitary and washing applications, The hot water may be mixed with water from the water supply source 102 via a blender valve to a temperature of from about 50 ° C to 70 ° C (depending on the application). The hot water produced can be stored in a hot water storage tank.  32 200837310 Figure 2 shows yet another unit included in the system of the present invention. particular,  Figure 2 shows the configuration of the absorption chiller 200. The absorption chiller 200 manufactures cooling water, Cooling water can be used for space cooling purposes. The absorption chiller 2〇〇 is divided into four sections: Condenser 202, Generator 204, Gasifier 206, And absorber 5 208. The absorption chiller 200 operates based on a thermochemical procedure that approximates the vacuum gasification of the refrigerant to absorb heat from the surrounding jade.  The gasifier 206 section and the absorber 208 section are maintained near vacuum conditions. particular, The conditions for the gasifier 206 are as follows: The gasifier 206 is maintained in a vacuum state to perform gasification at a lower temperature. E.g, The pressure can be 1 kPa.  10 The temperature can be about 4 °C. The absorption chiller 200 is heated by the heat exchanger 205 flowing hot water from the hot water tank 201. In addition, To supplement the heat, The absorption chiller 200 can be disposed adjacent to the burner 148 of the boiler and burner unit 146. Lithium bromide (LiBr) 210, i.e., absorbent and water 212, i.e., refrigerant feeds the generator section 2〇4 of the absorption chiller 200. The heat generated by the hot water produced by the boiler and burner unit 146, Or the water content of the LiBr solution 210 generated in the generator section 204 by the heat generated by the combustion of the Brown gas 120 by the burner 148. The refrigerant vapor in the form of water vapor 214 is recycled to the condenser section 202, The latent heat is released to the cooling water 242 in one of the heat exchangers 216 in the condenser section 202. In the program, The water vapor 214 is condensed back to the refrigerant water 212.  2〇 The refrigerant water 212 flows through the line 218, Line 218 includes an expansion valve 220 to form a refrigerant spray 222 in the gasifier section 206. Water from the refrigerant spray 222 is sprayed onto the cooling water pipe bundle 224 in the gasifier section 206. The portion of water from spray 222 is absorbed by the concentrated LiBr 230 of absorber section 208. And a portion is collected by the gasifier section 206 at 223, The condenser section 202 is circulated back through the line 218 by means of the gang 33 200837310. Refrigerant spray 222 The temperature of the water temperature is low, Therefore, the water of the refrigerant spray 222 is absorbed by the warm water 246 in the cooling water pipe 224 and vaporized (vaporized under vacuum). result, The cooling water is discharged by the cooling water pipe 224. The refrigerant vapor produced in this process is absorbed by the concentrated LiBr 2 〇 3 of the absorber section 208. Such rapid absorption of refrigerant vapor, Forming a vacuum state in the gasifier 206, The reason is that the gasifier 2〇6 is interconnected with the absorber 208. particular, A pump (not shown) is coupled to gasifier 206 and absorber 208. The pump creates a high vacuum of less than ί%% atmospheric pressure. The concentrated LiBr is produced in the generator section 2〇4. When the water content in the LiBr solution 10 is vaporized in the generator section 204, A concentrated lithium bromide is formed.  Concentrated lithium bromide flows through line 226 to absorber section 208, Line 226 includes an expansion valve 228 to form brominated clock spray 230. The lithium bromide from the brominated clock spray 230 is collected at the bottom of the absorber section 208. When combined with refrigerant vapor from gasifier 206, Forming a dilute lithium bromide solution pool 232, The refrigerant vapor 15 gas is recycled back to the lithium bromide pool 210 of the generator section 204 by the pump 236. Lithium bromide spray 230 sprays lithium bromide into one of heat exchangers 215 in absorber section 208. The heat exchanger 215 has a cooling water 240 having a temperature of about 25 ° C and is fed to the heat exchanger by the cooling water tower 250. At the same time, the slightly high temperature water 242 is discharged by the heat exchanger 215. And fed into the heat exchanger 216 in the condenser section 202.  20 results, After the condenser section 202 absorbs heat from the refrigerant vapor 214,  The high temperature water 244 is discharged by the heat exchanger 216. And the cooling water tower 250 is fed.  The cooling water 248 produced in the gasifier section 206 is piped to a storage tank. Or directly to the end user for each purpose, Such as space cooling applications. E.g, Cooling water 248 can be passed to air conditioning units in various homes 34 200837310 (heat exchangers with blowers) to provide space cooling applications.  The system of the present invention also includes an incineration unit. The detailed configuration of the incineration unit is not shown in Figure 3. particular, The incineration unit 3 uses the cloth _12() produced by the Brown gas generator U6 as _. The incineration unit lion is oxidized to household waste and industrial waste at the location of the system. The incineration unit 3 is based on Brownian 12 得 operation from a Brown gas storage tank. Brown gas 12() is transported from storage tank 122 to a combustion chamber 312 and a reoxidation chamber 314 via line network 302.  The official road network 302 step-by-step - pressure regulator, a check valve 303 at the outlet of the storage tank 122, The multi-head valve 3〇6 splits the Brownian gas stream into the combustion chamber 312 and the reoxidation chamber 314. The pressure regulator 3〇4 controls and maintains a uniform air outlet pressure of 12 〇 in the official network 302. The combustion chamber 312 and the reoxidation chamber 314 are each equipped with a Brown gas burner 313 and 315.  Brown gas burners 313 and 315 are equipped with a gas ignition device, Flame and flame style control device, Standard industrial gas burner for flame detection devices. Cloth 15 gas burners 313 and 315 are based on Brown gas 120 operation. Also has a motor drive fan, A gas supply solenoid valve and a gas nozzle. Burners 313 and 315 are combined to produce a flame at a temperature of up to 15 ° C in combustion chamber 312 and reoxidation chamber 314. A flash arrester 308 and 31 and a control valve 3〇5 and 3〇7 are also provided at the respective intake ports of the combustion chamber 312 and the reoxidation chamber 314.  20 The incineration unit 30A also includes pre-processing units 316 and 318. The pre-processing unit 316 is used for pre-processing of solid waste. The pre-processing unit 318 is used for pre-treatment of liquid waste. The pre-processing unit 316 includes a collection unit 320, A classifier 322 and a dryer 324. The collecting unit 32 collects solid waste, The classifier 322 classifies the waste. Solid waste can also be removed by visual means by means of manual classification. gravel, Metal and other huge items. The water content of the waste is reduced in the dryer 324, In the dryer 324, The waste is heated. The waste is heated by the bundle. There is water vapor in the tube bundle. The tube bundle is used to heat the tube bundle. The waste is thus heated. The waste from the dryer 324 is then fed to the combustion chamber 312. Similarly, For pretreatment of liquid waste, The pre-processing unit 318 is configured to collect one of the collected liquid wastes, 326, One of the sludge removal filters 328 is removed from the liquid waste, And a gasifier 330 that removes water content from the sludge. Filter 328 can be any suitable filter. For example, the filter can be a fabric filter or a membrane filter. In addition,  10 Filter presses or centrifugal filters can also be used. The liquid waste pre-treatment procedure may include solid_water separation to filter out of the raw water. The slag can be collected in a gasifier to remove water. The filtered raw water can then be chemically treated and then discharged to the drainage system. The treated waste is then fed to the combustion chamber.  The combustion chamber 312 is heated to a temperature of up to 15 〇〇 15 c by the combustion of Brownian gas 12 ,. This temperature is at the flash point of most solid waste. Once the combustion chamber 312 is burned by the waste material and the Brown gas 120 to about 1 Torr (rc temperature, The Brown Gas Burner 313 stops operating. Only when the temperature of the combustion chamber 312 drops below iooo °c, The Brown gas burner 313 is re-ignited. The interior of the combustion chamber 312 also has a heat exchanger 338. The heat exchanger 338 can expand heat recovery.  20 for example, The circulating water contained in the tube bundle of the heat exchanger 338 absorbs the heat of combustion by the combustion chamber 312 and releases the heat from the waste dryer 324. In the waste dryer 324, This heat can be used to remove moisture from the solid waste. The incineration unit 3〇〇 also includes a circulation system. The feed water is supplied to the heat exchanger in the incineration unit.  The circulation system includes a multi-head valve 348, 350, 352, - water vapor settling tank 344,  36 200837310 A pump 346, And the pipeline network 342.  • The flue gas 332 produced by the waste burning at the age of 312 is fed to the re-emulsification chamber 314, By further oxidizing organic materials and other harmful substances, the King's knife will dissolve any waste remaining in the flue rolling 332.  5 #emulsified to 314 is a combustion of flue gas 332 and maintained at a temperature of 1 Torr or more by supplemental combustion of Brown gas (10) by burner 315. The reoxidation chamber 314 is equipped with means for supplying fresh air to allow the flue gas 332 to undergo oxy-combustion. The reoxidation chamber is heated by the burner 315 to a temperature of about (10) Torr. The temperature is a component of the flue gas such as carbon monoxide (c〇), Chlorine (four), And the self-ignition temperature of A-burn 10 (CH4). Once the combustion of the flue gas 332 and the addition of the Brown gas 12 ,, When the reoxidation chamber 314 reaches a temperature of about i〇〇〇°c, The burner 315 is stopped. When the temperature of the reoxidation chamber 314 drops below 100 (rc, Burner 315 begins to burn Brown gas 120. The reoxidation chamber 314 is further provided with a grid block 311'. The grid block 311 is supported on one of the metal 15 brackets inside the reoxidation chamber 314. The highly permeable perforated grid block 311 can be made of platinum, steel, Made of nickel _ chrome or other nickel alloy. The bubble of the grid block 311 can be any suitable shape. Such as a square, Triangle or polygon. The grid block 3 can be composed of an interwoven multilayer structure to maximize contact with the input flue gas 332, And maximizing exposure to the Brown gas flame produced by the burner 315.  The flow directions of the Brown gas flames produced by the flue gas 332 and the burner 315 with respect to the grid block 311 are perpendicular to each other or parallel to each other. The grid block 311 is arranged in line with the Brown gas flame produced by the burner 315. The flue gas 332 from the combustion chamber 312 is guided through the grid block 311 by the guide channel. When the grid block 311 is directly exposed to the flue gas flame produced by the burner 315,  37 200837310 Grid block 311 produces glow, A temperature at which it can react with the incoming flue gas 332 is reached. In this program, Flue gas components such as carbon monoxide (c〇), Hydrogen (3⁄4), And other gaseous hydrocarbon compounds are oxidized into a form that is less harmful to the environment,  Such as carbon dioxide (C〇2), Water and other less harmful gases.  5 The flue gas 335 from the reoxidation chamber 314 passes through a chamber 334 containing a wet gastor 336. It is then discharged into the atmosphere as an exhaust gas 34. The wet scrubber 336 treats the resulting flue gas 335 to remove fly ash of sub-micron or larger. The wet scrubber 336 has a series of high volume water spray nozzles. To provide rapid flue gas cooling to about 200X: To 30 (TC temperature, Then released as exhaust gas 34〇, To curb the formation of dioxins and furans in the atmosphere. The feed water fed to the wet scrubber 336 is derived from the water supply source 102. The exhaust gas 34 释放 released by the chamber 334 can be connected to an air filter system.  Fig. 4 shows a configuration example of each unit of the aforementioned system. particular,  Figure 4 shows no such as Brown gas generator 116, Pin furnace and burner unit,  How to use 15 absorption chiller 200 and incineration unit 3 用于 for a separate system, , First to produce Brown gas, Store Brown gas, And the delivery of Brown gas for various purposes in multi-story buildings.  Figure 5 shows a system substantially separated from one of the embodiments of the present invention. particular, Figure 5 shows the use of Brown gas 20 and Brown gas in a combustion chamber of a separate system. Brown gas is produced in the Brown gas generation system 1113, Wherein the Brown gas generation system 1113 comprises a Brown gas generator 1114, a hot parent converter 1116, And a Brown gas storage tank 1122. The special Braun gas is produced in the Brown gas generator 1114, A form of Brown gas generator U14 has been described in the US Patent No. No. 656. Generator 38 200837310 1114 includes an electrolysis chamber. The power source 11〇4 is connected to a control panel 11〇6, Control panel 1106 monitors and controls operating parameters, A power supply generator 1114 such as a power supply line 1112. A water supply source 1102 is also provided. The water supply source 1102 can be in the form of a water storage tank. The water system from the water supply source 11〇 passes through a reverse osmosis (R0) water filter 1108 using 5 pumps 111〇. The filtered ruler is fed into the electrolysis chamber of the water generator 1114.  As a result, the generator 1114 takes in water and electricity. Come from the electrolysis process to dissociate oxygen and hydrogen. The resulting mixture of oxygen and hydrogen is directed through line 1121 to Brown gas storage tank 1122. The Brown gas generation system 1113 further includes a heat exchanger 1116. The immediate by-product of the electrolysis process is the heat obtained by hydrolysis into its constituents. Heat exchanger 1116 is cooled by water. The cold water from the cooling water tower 1118 is circulated to the heat exchanger 1116 ° via the line in, then Warming is led out of heat exchanger 1116 by line 1119.  Return to the cooling tower 1Π8.  15 Brown gas storage tank 1122 is partially filled with liquefied hydrocarbons. In this case, The liquefied hydrocarbon is hexane 1124. A hexane storage tank 1126 is also provided. The hexane 1124 from the hexane storage tank 1126 is pumped into the Brown gas storage tank 1122 by means of a pump (not shown). A mixture of oxygen and hydrogen is mixed with hexane vapor to form Brown gas 112. The Brown gas storage tank 1122 is further provided with a bleed valve u28. The relief valve is a valve, Set to a certain pressure level to prevent the pressure of the container or system from becoming unsafe.  Brown gas 1120 from Brown gas storage tank 1122 is supplied directly to combustion chamber 1142 via line network 1130. The pipeline network is equipped with at least one check valve 1132, To ensure that the flow of the Brown gas 112 只 is only in the direction of - 39 200837310. The pipe network 1130 further includes at least one pressure regulator (four), At least one control valve 1136, And at least one flash arrester 1138. The pressure regulator is a device for controlling and maintaining the gas pressure of the outlet gas corresponding to the pipeline. The flash fire suppressor is a device that prevents "flashback" from the external fire through the open coaxial port.  In particular, the Brown gas is supplied to the combustion chamber by at least one burner 114G via the pipeline network 113. The burner i i 4 is equipped with a gas ignition device, Flame shape and style control device, Standard industrial gas burner for flame detection devices. The burner U40 is based on Brown gas 112〇 operation. And has a motor drive blower, The gas supplies electromagnetic I and gas nozzles. The burner ray is combined to produce a flame with a temperature higher than 120 generations. The burner is located on the side of the combustion chamber m2 and projects the flame into the interior of the combustion chamber 1142. When the waste is burned inside the combustion chamber 1142, Produce flue gas. The heat from the flue gas can be used to generate electricity, Details are detailed later.  15 20 Figure 6 shows the configuration of the system of the present invention, The heat from the flue gas produced by the combustion chamber H42 is used for a variety of additional purposes. Figure 6 shows. The burning heart will use the Brown gas (10) generated by the Brown gas generation system 1113 as a fuel to burn the combustion material. Job materials can be scrap, Including household pure red industry waste.  Brown gas from Brown's gas to produce secret 1113 is as previously mentioned in &  The pipeline network (10) is shown in the drawing and is passed to the combustion unit 1142a. The pressure in the combustion unit regulator 1134 is controlled in the line network 113 适合 to use the 1142a-to-export Brown gas pressure. E.g, The gas pressure can be about the water pressure (i.e., 2738 Pa).  40 200837310 The inner wall gasket of the combustion unit lM2a is made of fossil fuel material. To include combustion heat inside the combustion unit 1142a, And the structure of the combustion unit U42a is protected. E.g, Refractory materials include hard, heat resistant materials that work in an acidic environment. Examples of fire resistant materials include, but are not limited to, aluminum oxide, Tantalum carbide, Clay, brick, And 5 矽 oxygen. The gap injection pressurized air is supplied to the combustion unit 1M2a via a perforation of the side or bottom of the combustion unit. Compressed air is used to promote the turbulent mixing of the waste, The waste will be burned with air in the combustion unit 1142a. The gap injection compressed air helps to prevent clogging of the supply of compressed air to the perforations of the combustion unit U42a. The dry solid waste is separated from the ash by a grid (not shown) at the bottom of the combustion unit 1142a. The bottom ash 1201 from the combustion of the waste in the combustion unit 1142a is passed through the combustion unit 1142& The bottom hopper (not shown) is collected for disposal.  The flue gas 1202 is produced as a result of the combustion of the waste in the combustion unit 1142a. A plurality of flue gases 12〇2 are directed by the combustion unit U42a to a water-steamed 15-gas boiler 1204. The water is pumped to the steam pin furnace 1204 by the pump 1212. In the steam boiler 1204, Water circulates inside the tube 1206, The tubes are externally heated by the flue gas 1202 that is directed to the steam boiler 1204 by the combustion unit 1142a. For example, the flue gas can be 9〇〇t: . When the water-filled tube 12〇6 contained in the steam boiler 1204 is exposed to the high-temperature flue gas 12〇2,  20 the temperature of the water in the tube 1206 rises, Due to the thermosiphon effect, The hot water rises to the water vapor drum 1208 in the steam steel furnace 1204. The hot water in the steam drum 1208 is further heated by the flue gas 1202 to produce water vapor 1214. The water vapor 1214 is separated from the top of the water vapor drum 1208. Ultra-hot water vapor can be produced by heating in a super heater (not shown) as needed. The flue gas 1202 is then directed through the 200837310 channel 1228a to the post-processing unit 123A to process the flue gas 1202. It is then discharged η% of the human exhaust gas. The post-processing unit is detailed later.  Water money 1214 or super hot water vapor is then used to drive the steam full wheel 1216. For example, the super hot water vapor may be 39 (rc or more. The water vapor leaking wheel (2) 65 can be a single-stage steam steamer or a multi-stage steam steamer. The steam turbine (4) is connected to the generator coffee for power generation by the shaft Π18. The water vapor (2) 4 feeds the steam turbine 1216 at a high pressure of about [mu]3 (2. 3 x 〇 6 Pa). Water vapor full wheel 1216 spin, The spindle 1218 is also caused to spin. As a result, the magnet contained in the generator 1220 is also rotated since the spindle (10) is self-contained. The magnet has a wire coil 10 coils. When the magnet inside the generator 1220 rotates, Current is generated in the metal wire. Generator 1220 converts mechanical energy into electrical energy. The power generated by the generator 122 is then transmitted to a series of electrical devices for voltage and current regulation. The Brown gas generation system 1113 is used to generate Brown gas 112〇, Or transmitted to the power grid inside the system, It is the power supply 11〇4 of the system.  15 Water vapor 1214 or super hot water vapor passing through the steam turbine 1216 is then passed to the heat exchanger I222 via the channel. The water vapor 1214 is cooled in the heat exchanger 1222 to be condensed into water. The condensed water is then pumped back to the pipe 1206 of the water vapour furnace 1204 by the pump 1212. Used to produce water vapor 1214 from the heat of the flue gas 1202. The feed water flowing into the heat exchanger 1222 for cooling the water vapor 1214 or 20 super hot water vapor from the steam turbine 216 is obtained from the water supply source 1102 by the pipe network 1224. Heat exchanger 1222 also cools excess superheated water vapor or excess water vapor 1214. When the steam turbine 12i6 reaches its maximum capacity, When it is no longer possible to ingest any larger amounts of water vapor 1214 or super hot water vapor, Water vapor 1214 is considered to be in excess. When this happens, Excess water 42 200837310 Vapor 1214 or excess super hot water vapor is directed to heat exchanger 1222 via bypass tube 1226. As explained above, Excess water vapor 1214 and excess super hot water vapor are cooled in heat exchanger 1222 and condensed into water. The water is then sent back to the tube 1206 of the steam boiler 1204 by the pump 1212. The water vapor 1214 is produced by the endothermic heat of the flue gas 5120.  The combustion chamber 1142 also includes a pre-processing unit 1242. particular, The pre-processing unit 1242 is used for pre-treatment of solid waste. The pre-processing unit 1242 includes a dryer. The waste water is fed into the combustion unit H42a for combustion to reduce the water content of the waste. The waste is heated by a tube bundle 1243 10 inside the dryer. The tube bundle 1243 has a tube through which the flue gas 1202 passes through the tube bundle. Heating waste from the outside. particular, The tube of tube bundle 1243 is highly thermally conductive. A plurality of flue gases 1202 from the combustion unit 1142a are directed to the tube bundle 1243 via channels 1229. The flue gas 1202 from the steam boiler 1204 is also directed through the channel 1228a to the tube bundle 1243. The flue gas 1202 15 passing through the tube bundle 1243 is then directed to the aftertreatment unit 1230 via the channel 丨244. The flue gas 1202' is then discharged into the atmosphere to become the exhaust gas 1236. The post-processing unit 123 is described later in detail.  The flue gas 1202 from the steam boiler 1204 and the pre-processing unit 1242 passes through the channels 1228 & And 1244 is directed to post processing unit 20 1230. The aftertreatment unit 1230 includes a wet scrubber 1232 and a quencher 1234. The flue gas 1202 from the steam boiler 12〇4 and the pre-treatment unit 1242 is washed down into the wet scrubber 1232. The wet scrubber 1232 can be a chemical wet stripper, For example, the chemical used in the chemical wet scrubber may be an aqueous slurry formed by hydrogenation of about or sodium hydroxide. The wet scrubber 1232 can be a plurality of interconnected enclosures having 43 200837310. Each chamber is formed by a perforated plate to slow the passage of the flue gas 1202 through the wet scrubber 1232. The wet scrubber 1232 processes the flue gas 1202 to remove sub-micron or larger fly ash, Dust and particles. The wet scrubber 1232 has a series of still-pressure fluid spray nozzles. E.g, The fluid is an experimental solution,  5 such as sodium hydroxide or calcium hydroxide. The alkaline solution neutralizes the flue gas 1202 which may be acidic. The alkaline solution is also washed to remove fly ash and large particles in the flue gas 12〇2.  After the flue gas 1202 passes through the wet scrubber 1232, The semi-treated flue rolling 1202 is washed down into the quencher 1234 for rapid quenching. The quencher 1234 1 has a series of high volume water spray nozzles to provide rapid quenching of the flue gas 1202 to a temperature of between about 200 ° C and 300 ° C. Then the flue gas 12〇2 is released into the exhaust gas 1236. To curb the formation of dioxin and furans in the atmosphere. Quenching also reduces the odor of the semi-treated flue gas. The feed water fed to the quencher 1234 is derived from the water supply and demand source 11〇2. The water from the supply and demand source 15 Η 02 is pumped to the quencher 1234 via the pipeline network 1238. The fluid containing fly ash and large particles collected at the bottom of the post-processing unit 123 can pass through the filtration system. The spray nozzle of the wet scrubber 1232 is then circulated back by the pump 1233. At fixed time intervals, The fluid at the bottom of the aftertreatment unit 123A can be discharged to the processing unit 124A, I am here to accept the Chemistry Division. The chemically treated fluid can be recycled back to the wet scrubber 1232, Or it can be placed in a drainage system.  Optionally, The exhaust gas 1236 released by the quencher 1234 can be coupled to an air transition system. Accept further processing, It is then discharged into the atmosphere. Waste gas 1236 also contains saturated steam. Therefore, a gasifier can be installed at the air outlet of the quencher 44 200837310 1234. To remove the saturated water vapor in the exhaust gas 1236, In order to prevent the formation of plumes in the atmosphere. As for another option, The treated flue gas 1202 can also pass through a gas filtration system. It is then vented to the atmosphere to remove submicron sized particles.  A further configuration of the system of the present invention is wherein the heat from the flue gas produced by the combustion chamber 114 2 is used for each purpose, The system configuration is shown in Figure 7. The system of Figure 6 is substantially identical to the system of Figure 7. The exception is the combustion chamber 1142. The combustion chamber 1142 shown in Fig. 7 includes a secondary combustion chamber. Special, The combustion chamber 1142 of Fig. 7 includes a combustion unit 1142a and a reoxidation chamber 10 1302. The reoxidation chamber 1302 can be a thermal reoxidation chamber. Like the combustion unit 1142a, The reoxidation chamber 13〇2 also utilizes the Brown gas 1120 generated by the Brown gas generation system 1113 as fuel. in this way, The Brown gas 112 is led to the reoxidation chamber 13〇2 by the Brown gas generation system 1113 via the pipeline network 113〇. Piping network 1130 includes a multi-head valve 1303, To split the Brown gas into the 15 combustion unit and the reoxidation chamber 13 () 2 . Pipeline network 1 (10) further includes a check valve 1304, Pressure regulator 1306, Control valve 13〇8 and flash arrester 1310. The pressure regulator 13〇6 controls and maintains a consistent Brownian pressure in the pipeline network.  The reoxidation chamber 1302 is equipped with a Brown gas burner 1312. The Brown gas burner 1312 is equipped with a gas ignition device, Flame shape and style control device and: A standard industrial gas burner for the device. The Brown Gas Burner (3) 2 is based on Brownian 112 〇 operation. Also has a motor drive blower, A gas supply solenoid valve and a gas nozzle are provided. The Brown gas burner (10) can be assembled to produce a temperature above 12 〇〇t in the reoxidation chamber 1302: Flame. particular, Reoxygenation 45 200837310 The chemical chamber 1302 is maintained at a temperature of about 1 〇〇 (rc). The temperature is a flue gas component such as carbon monoxide (CO), Hydrogen (HO, And the reduction temperature of decane (Ch4).  At the beginning of the incineration (combustion) process, The Brown gas burners 114A and 1312, respectively, of the combustion unit 1142a and the reoxidation chamber 51302 burn Brown gas 1120 to heat the furnace space inside the combustion unit 1142a and the reoxidation chamber 1302. Brown Gas 1120 & The L-rate and combustion time are controlled to the combustion unit 1142& The preset temperature is reached. Typically, In the absence of waste, The combustion unit 1142a can reach temperatures in excess of 1000 C. In the process of incineration, The dry waste is constantly fed to the combustion unit U42a to be burned. At a steady rate, Constantly supplying waste, The combustion unit 1142a can reach temperatures in excess of 1200 °C. During the combustion process, Manufactured with carbon monoxide, Gaseous hydrocarbon compounds and flue gases of nitrogen oxides (Ν〇χ). The resulting flue gas 1202 is carried to a reoxidation chamber 1302 for further processing. The reoxidation chamber 1302 can be an elongated structure. To allow a residence time of at least 2 seconds 15 to allow the flue gas 1202 to completely burn. In addition, The reoxidation chamber 13〇2 may be composed of two or more small furnaces having similar or different interconnections. A more complete treatment of the flue gas 1202 is achieved by extending the exposure of the flue gas 1202 to the processing time.  The reoxidation chamber 1302 is equipped with a grid block 1313 supported on a gold 20 frame inside the reoxidation chamber 13A2. Highly permeable perforated grid block ι313 can be made of platinum, steel, Made of nickel-chromium alloy or nickel alloy. The grid block 1313 positively reacts with the Brown gas flame generated by the Brown gas burner 1312. The high temperature is reached inside the reoxidation chamber 1302. The voids of grid block 1313 can have any suitable shape, Such as a square, Triangle or polygon. particular, Grid 46 200837310 Block 1313 can be constructed as a multilayer structure of interconnects, To maximize the contact with the incoming cloth 1120 and maximize exposure to the Brown gas flame produced by the Brown Gas Burner 312.  The flue gas stream and the Brown gas flame generated by the Brown gas burner 1312 are oriented perpendicular to each other or parallel to each other with respect to the grid block 1313.  Grid block 1313 is positioned to align with the blast of flame generated by Brown gas burner 1312. The flue gas 1202 from the combustion unit 1142a passes through the grid block 1313. When the grid block 1313 is exposed to the Brown gas flame generated by the Brown gas burner 1312, Grid block 1313 glows and reaches a temperature at which 10 can react with the input flue gas 1202. In the program, Flue gas components such as CO, Η: , And other gaseous hydrocarbon compounds are oxidized into a form that is less harmful to the environment, Such as carbon dioxide (C02), Water and other less harmful gases. Especially before the oxygen reacts further with the hydrogen in the brown gas 1120, The nitrogen-containing flue gas 1202 is reduced to the elemental composition of nitrogen and oxygen. This produces nitrogen and water vapor.  As described in Figure 6 above, Part of the flue gas 1314 from the reoxidation chamber 13〇2 is directed to the steam boiler 12〇4 for making steam (or super hot water vapor) to drive the steam thirst wheel 1216 and the generator 1220 to generate electricity. . Part of the flue gas 1314 from the reoxidation chamber 1302 is also directed 20 through the channel 1315 to the tube bundle 1243 to dry the waste material in the pretreatment unit 1242.  Throughout the incineration process, Both the combustion unit 1142a and the reoxidation chamber 13〇2 are maintained at a negative pressure to ensure the formation of a flue gas 12〇2 flow from the combustion unit 1142a and the reoxidation chamber 13〇2 to the steam boiler 1204 and the pretreatment unit 1242. Proper ventilation. For example, The pressure is about _5 〇pa. The negative pressure on the combustion unit n42a 47 200837310 and reoxidation to 1302 can be transmitted through the smoke discharge end of the combustion unit n42a (in the case of Figure 6). The flue gas discharge end of the reoxidation chamber 1302 is installed (in the case of the secret shown in Fig. 7), Or set up & The exhaust fan at the vent end of the post-processing unit 123G is achieved.  5 Figure 8 shows a general assembly of one embodiment of the present invention. particular, Figure 8 shows the treatment of the flue gas emitted by the flue gas vent. The flue gas is then released into the atmosphere. The flue gas 2103 from the flue gas ejector 2102 is directed to the first process chamber 21〇4. The flue gas vent 21 〇 2 can be any system that emits flue gas. E.g, The flue gas ejector 21〇2 can be an incineration unit, Coal kiln and so on. Flue gas 2103 is rich in carbon monoxide, Gaseous hydrocarbon compounds and nitrogen oxides (NOx). The flue gas 21〇3 typically has a temperature of 300 ° C or higher. In the first processing chamber 21〇4, The flue gas 2103 is further heated.  E.g, The flue gas 2103 is further heated to about 8 〇〇 C in the first processing chamber 21〇4. The heated flue gas 21〇3 is then directed into the second processing chamber 21〇6 for further heat treatment. E.g, The flue gas can be heated to a temperature of about 1000 C in the second processing chamber 2106. The heated flue gas 2103 is introduced into the third processing chamber 21〇8 by the second processing chamber 2106. Want to be heated above 12〇0. (: Temperature. particular, The temperature in the third processing chamber 2108 is approximately 1600 °C.  The flue gas 2103 is in the first processing chamber 21〇4, The second processing chamber 21〇6 and the twenty-third processing chamber 2108 are heated by burning Brown gas. Brown gas can be produced in the Brown gas generator. A form of Brown gas generator is described in US Patent No. 4, 081, No. 656. Brown gas can be directly supplied to the processing chamber 21〇4 by a Brown gas storage tank 2110 via the pipeline network 2112. 2106 and 2108. The Brown gas storage tank 2110 can be equipped with a bleed valve 2111. The relief valve is a valve, The valve set 48 200837310 is intended to be opened at a certain pressure level to prevent the pressure of the container or system from becoming unsafe. The pipeline network 2112 can be equipped with at least one check valve 2114.  The official road network 2112 can further include a multi-head valve 2116 to split the Brownian airflow into the various processing chambers 2104, 2106 and 2108. For example, Brownian airflow can be split,  5 let Brown gas through the pipeline network 2118, 2120 and 2122 are respectively supplied to the first processing chamber 2104, The second processing chamber 2106 and the third processing chamber 2108. Each pipeline network 2118, 2120 and 2122 respectively comprise at least one pressure regulator 2124,  2132, 2140, At least one control valve 2126, 2134, 2142, And at least one flash arrester 2128, 2136, 2144. The pressure regulator is a device for controlling and maintaining the gas pressure of the uniform outlet gas to a pipeline; The flash fire suppressor is a device that prevents the external fire from "flashing back" through the open safety pipe interface. Pressure regulator 2124, 2132, And 2140 are controlled and maintained in the pipeline network 2118, Suitable for processing room 2104 in 2120 and 2122, The consistent air outlet Browning pressure of 2106 and 2108. E.g, The gas pressure is about 11 吋 water pressure (also 15 is about 2738 Pa).  particular, Brown gas is supplied to the processing chamber 2104, 2106 and 2108 burners 2130, 2138 and 2146. Burner 2130, 2138 and 2146 can be equipped with a gas ignition device, Flame shape and style control device, Standard industrial burner for flame detection equipment. Burner 2130, 2138 and 2146 are based on cloth 20 gas operation, And there is a motor drive blower, Gas supply solenoid valves and gas nozzles. Burner 2130, The 2138 and 2146 sets are matched to produce a flame above 1200 °C. Burner 2130, 2138 and 2146 may be arranged to be separately injected into the processing chamber 2104 by flame, 2106 and 2108 internal.  Brown gas burner 2130, 2138 and 2146 are assembled for the first process 49 200837310 Room 2104, The second processing chamber 2106 and the third processing chamber 2108 are respectively produced at about 800 ° C, Flames at temperatures of 1000 ° C and 1200 ° C. particular, Flue gas components such as carbon monoxide (CO), Hydrogen (H2), And the self-ignition temperature of methane (CH4) is about 800 ° (: Up to 1600° (: between. Once burned by the combustion of flue gas 2103 and the addition of Brown gas, In the processing room 2104, When 2106 and 2108 reach the desired temperature, Brown gas burner 2130, 2138 and 2146 stopped working. When the first processing chamber 2104,  The temperatures of the second processing chamber 2106 and the third processing chamber 21〇8 are respectively lowered to 800 ° C, At 1000 ° C and 1200 ° C, Brown gas burner 2130, 2138 and 2146 began to burn Brown gas. At the beginning of the process, Brown gas burner 213〇,  10 2138 and 2146 burn Brown gas to heat the first processing chamber 2104, The second processing chamber 2106 and the furnace interior space inside the second processing chamber 2108. The Brown gas flow rate and combustion time are controlled to be available in each processing chamber 21〇4, 21〇6 and 21〇8 reach the preset temperature.  First processing chamber 2104, The second processing chamber 21〇6 and the third processing chamber 21〇8 15 may have an elongated structure. To allow a residence time of at least 2 seconds to complete the combustion of the flue gas 2103. In addition, The first processing chamber 21〇4, The second processing chamber 21〇6 and the third processing chamber 2108 may each be made of two or more interconnected small furnaces of similar or different construction. Exposing the exposure time of the treatment by prolonging the flue gas 21〇3, To achieve a more complete treatment of flue gas 2103. The first processing chamber 21〇4,  At least one of the second processing chamber 2106 and the third processing chamber 2108 may be further equipped with a grid block (not shown).  The grid block can be carried in the first processing chamber 21〇4, The inner metal frame of at least one of the second processing chamber 21〇6 and the third processing chamber 2108. Highly permeable perforated grid blocks can be molybdenum, steel, Nickel-chromium alloy, Recorded alloy or its 50 200837310 combination. Nets and Brown Gas Burner 2130, The Brown gas flame positive reaction generated by 2138 and 2146 comes from the first processing chamber 21〇4, The second process reaches a high temperature inside the 2106 and the second processing chamber 2108. The bubbles in the grid squares can have any suitable shape and size. For example, the bubble of the grid square can be square, Triangle or polygon. particular, The grid blocks can be composed of a multi-layered structure. To maximize contact with the input flue gas 21〇3, And maximize exposure to the Brown Gas Burner 2130, Brown Flame 0 flue gas generated by 2138 and 2146 and by Brown gas burner 2130, The directivity of the 10 Brownian flame directions generated by 2138 and 2146 with respect to the grid squares is perpendicular to each other or parallel to each other. The grid block is positioned and associated with the Brown Gas Burner 2130, The Brown ash produced by 2138 and 2146 is aligned. From the flue gas vent 21 21 The flue gas 2103 of the first processing chamber 2104 or the second processing chamber 2106 is guided through the channel and passes through the first processing chamber 2104, respectively. A grid of second processing chamber 2106 and third processing chamber 15 2108. When the grid block is exposed to the Brown Gas Burner 2130, When the Brown Flames produced by 2138 and 2146, The grid square glows and reaches a temperature that can react with the incoming flue gas 21〇3. In the process,  Flue gas components such as CO, H2 And other gaseous hydrocarbon compounds are oxidized to become environmentally innocuous components, Such as carbon dioxide ((3〇2), Water and relatively no harmful gases. particular, The nitrogen-containing flue gas 2103 is dissociated into an elemental component after reacting with hydrogen in the brown gas. Thereby nitrogen is produced.  From the first processing chamber 2104, The partially heated flue gas 2103 of each of the second process chamber 2106 and the third process chamber 2108 can be directed to a post-treatment unit. The aftertreatment unit can be a scrubbing assembly 2176. Details are detailed later. In addition,  51 200837310 Partially from the processing chamber, in particular the heated flue of the third treatment chamber 21〇8, is introduced into the water tube steam boiler 2148. The water was pumped into the steam pin furnace 2148 by the pump 2170. In the steam boiler 2148, The water circulates in the water pipe 2150, The water pipe is guided to the steam boiler 5 2148 by the third processing chamber 2108. , The second heated flue gas 21〇3 is heated externally. When the water-filled tube 2150 contained in the steam boiler 2148 is exposed to the high-temperature flue gas 2103, The water temperature in the water officer 2150 rises, Manufacture of water vapor 2154, The water vapor then rises to the water vapor drum 2152 in the steam boiler 2148. The water vapor 2154 is separated from the top of the water helium drum 2152. Ultra-hot water vapor can be produced by heating in a super heater (not shown) as needed. The flue gas 2103 is then directed to the aftertreatment unit for processing the flue gas 2103, It is then discharged into the atmosphere to become the exhaust gas 2194. The aftertreatment unit can be a scrubber assembly 2176. Details are detailed later.  The spa gas 2154 or super hot water vapor is then used to drive the water vapor turbine 2156. E.g, The super hot water vapor can be 25 (rc or more. The water vapor turbine 2156 15 can be a single stage steam turbine or a multi-stage steam turbine. The steam turbine 2156 is coupled to a generator 2158 for power generation by a spindle 2160. Water vapor 2154 is fed to steam turbine 2156 at a high pressure. The water vapor turbine 2156 spins, Causes the spindle 2160 to also spin. As a result of the spin of the spindle 216, The magnet in generator 2158 also rotates. The magnet has a metal coil wound around the magnet. When the magnet inside the power generation unit 2158 rotates, The coil generates a current. Generator 2158 converts mechanical energy into electrical energy. The power generated by the generator 2158 is then transmitted to the power grid 2168.  Water vapor 2154 or super hot water vapor passing through steam turbine 2156 is then directed to heat exchanger 2166. Water vapor 2154 is cooled in heat exchanger 2166 by 52 200837310 to condense into water. The condensed water is then pumped into a water vapor pot 2150 in a water tube 2150 by a pump 2170 for absorption of heat from the flue gas 2103 to produce water vapor 2154. The feed water flowing into the heat exchanger 2166 for cooling the super hot water vapor from the steam turbine 2156 is supplied from the water supply source 2172 via the pipeline network 2174. Heat exchanger 2166 also cools excess super hot water vapor or excess water vapor 2154. When the steam turbine 2156 reaches its maximum capacity and is unable to take any water vapor 2154 or super hot water vapor, Water vapor 2154 is considered excessive. When this happens, Excess water vapor 2154 or excess superheated water vapor is directed to the heat exchanger by bypass tube 2162. As explained above, Excess water 10 Vapor 2154 and excess superheated water vapor are cooled in heat exchanger 2166 and condensed into water. Then, the pump 2170 is pumped back into the water pipe 2150 of the steam boiler 2148, Used to absorb heat from the flue gas 2103 for the manufacture of water vapor 2154.  From the steam boiler 2148, First processing chamber 2104, The flue gas 2103 of the second process chamber 2106 and/or the third process chamber 2108 is directed into the interior of the scrubber 15 assembly 2176. The scrubber assembly 2176 includes a wet scrubber 2178 and a quench 2188. From the steam boiler 2148, First processing chamber 2104, The flue gas 2103 of the second process chamber 2106 and/or the third process chamber 2108 is submerged into the wet scrubber 2178. The wet scrubber 2178 can be a chemical wet scrubber. The wet scrubber 2178 can be one of a plurality of interconnected enclosures. Each chamber is formed by a perforated plate 20 to slow the passage of flue gas 2103 through the wet scrubber 2178. The wet scrubber 2178 processes the flue gas 2103 to remove sub-micron or larger fly ash, Dust and granules. The wet scrubber 2178 has a series of high pressure fluid spray nozzles 2180. E.g,  The fluid can be an alkaline solution, Such as sodium hydroxide or calcium hydroxide. The alkaline fluid neutralizes the acidic flue gas 2103. The alkaline fluid is also washed to remove fly ash and large particles from the flue gas 2103 53 200837310.  After the flue gas 2103 passes through the wet scrubber 2178, The semi-treated flue gas 2103 is washed down into the quench 2188 for rapid quenching. The quencher 2188 has a series of high volume water spray nozzles 2190 to provide rapid cooling of the flue gas 2103 to a temperature of between about 200 ° C and 300 ° C. Then the flue gas 2103 is released into the atmosphere 2194, To curb the formation of Dioxin and urethanes in the atmosphere. Quenching also reduces the odor of the semi-treated flue gas 2103. The feed water fed to the quench 2188 is derived from the water supply and demand source 2172. Water from the water supply and demand source 2172 is pumped through the line network 2196 to the chiller 2188 by the pump 2192. The fluid 2182 containing fly ash and large particles collected at the bottom of the scrubber assembly 2176 can pass through a filtration system. The spray nozzle 2180 of the wet scrubber 2178 is then circulated back by the pump 2184. At regular intervals, The fluid 2182 at the bottom of the scrubber assembly 2176 can be discharged into the processing unit 2186. It is chemically treated there. The chemically treated fluid is circulated back to the wet scrubber 15 2178, Or it can be discharged into the drainage system.  Optionally, Exhaust gas 2194 released by scrubber assembly 2176 can be connected to an air filter system for further processing. It is then discharged into the atmosphere.  Exhaust gas 2194 also contains saturated water vapor. Therefore, a gasifier can be installed at the gas outlet of the scrubber assembly 2176 to remove the saturated water vapor in the exhaust gas 2194. Take 20 to prevent the formation of plumes in the atmosphere. As for another option, The treated flue gas 2103 can also pass through the gas system. It is then vented to the atmosphere to remove submicron sized particles.  Throughout the process, The first processing chamber 21〇4, The second processing chamber 21〇6 and the second processing chamber 2108 are maintained at a negative pressure to ensure the processing chamber 21〇4,  54 200837310 2106 and 2108 to steam boiler 2148 and flue gas 2103 flue gas 2103 flow to form proper ventilation. For example, the pressure is about -50 Pa. In the first processing chamber 2104, The negative pressure of the second processing chamber 2106 and the third processing chamber 2108 can be transmitted through the first processing chamber 2104. The flue gas discharge end of the second process chamber 2106 and the third process chamber 2108 5 or the exhaust fan of the ventilating end of the scrubber assembly 2176 is achieved.  BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic diagram of a system in accordance with an embodiment of the present invention.  Figure 2 is a still further embodiment of the present invention, A schematic diagram of an absorption cooler 10 .  Figure 3 is a still further embodiment of the present invention, An indication of an incineration unit.  Figure 4 is a still further embodiment of the present invention, A localization that directs Brown gas and hot water and cooling water to a multi-storey building, Storage and transport 15 System schematic.  Figure 5 is a still further embodiment of the present invention, A schematic diagram of a system.  Figure 6 is a view showing still another embodiment of the present invention, A schematic diagram of a system utilizing heat from a flue gas produced by a combustion chamber.  20 is a still further embodiment of the present invention, A schematic diagram of a system utilizing heat from a flue gas produced by a combustion chamber.  Figure 8 is a still further embodiment of the present invention, A schematic diagram of an assembly.  55 200837310 [Explanation of main component symbols] 102. .  . Water supply source 104. .  . Power Supply 106...Control Panel 108···Reverse Osmosis (RO) Water Filter 110. .  . RO sink 112... pump 114... power supply, line 116. .  . Brown gas generator 118. .  . Heat exchanger 120. .  . Brown gas 121... pipeline 122. .  . Brown gas storage tank 124...hexane 126...hexane storage tank 127... pump 128. .  . Relief valve 130. .  . Pipeline network 132··. Check valve 133...pressure regulator 134. .  . Control valve 136. .  . Flash fire suppressor 138...pipeline 140. .  . Check valve 141...pressure regulator 142. .  . Control valve 144... flash fire suppressor 146... steel furnace and burner unit 148. .  . Burner 150... boiler 152. .  . Line 154... Line 156... Line 157... Line 158... Pump 159. .  . Solar collector 200. .  . Absorption cooler 201. .  . Hot water tank 202. .  . Condenser 204. .  . Generator 205... heat exchanger 206. .  . Gasifier 208. .  . Absorber 210. .  . Lithium bromide, lithium bromide collection 212. .  . Water 214... water vapor 215. .  . Heat exchanger 56 200837310 216. .  . Heat exchanger 218...pipeline 220. .  . Expansion valve 222... refrigerant spray 223... collect water 224. .  . Cooling water pipe 226. .  . Pipeline 228. .  . Expansion valve 230. .  . Concentrated lithium bromide 232. .  . Lithium bromide solution 236... pump 238... pump 240. .  . Cooling water 242. .  . Micro-high temperature water 244. .  . South Wenshui 248...cooling water 250. .  . Cooling water tower 300... Incineration unit 302. .  . Pipeline network 303··. Check valve 305. .  . Control valve 306. .  . Multi-head valve 307. .  . Control valve 308. .  . Flash fire suppressor 310. .  . Flash fire suppressor 311. .  . Grid block 312. .  . Combustion chamber 313. .  . Brown gas burner 314...reoxidation chamber 315. .  . Brown gas burner 316. .  . Pre-processing unit 318. .  . Pre-processing unit 320...collection unit 322. .  . Classifier 324. .  . Dryer 326...collection unit 328. .  . Filter 330. .  . Gasifier 332. .  . Flue gas 334. .  . Room 335. .  . Flue gas 336. .  . Wet scrubber 338. .  . Heat exchanger 340. .  . Exhaust gas 342... pipeline network 344... water vapor settling tank 346... pump 348. .  . Multi-head valve 57 200837310 350. .  . Multi-head valve 352. .  . Multi-head valve 1102. .  . Water supply source 1104... power supply 1106... control panel 1108. .  . Reverse Osmosis (RO) Water Filter 1110... Pump 1112... Power Cord 1113... Brown Gas Generation System 1114. .  . Brown gas generator 1116...heat exchanger 1117. ··Line 1118...Cooling tower 1119...Line 1120. .  . Brown gas 1121... pipeline 1122. .  . Brown gas storage tank 1124. .  . Hexane 1126...hexane storage tank 1128. .  . Relief valve 1130. .  . Pipeline network 1132...check valve 1134...pressure regulator 1136. .  . Control valve 1138. .  . Flash fire suppressor 1140. .  . Burner 1142...combustion chamber 1142a. ·· Single stage combustion unit 1201. .  . The bottom ash is 1202. .  . Flue gas 1204... water pipe steam boiler 1206. .  . Water filling pipe 1208. .  . Water vapor drum 1212. .  . Pump 1214. .  . Water vapor 1216... water vapor turbine 1218···spindle 1220. .  . Generator 1222. .  . Heat exchanger 1224. .  . Pipeline network 1226. .  . Bypass tube 1228a. . . Channel 1228b. . . Channel 1229. .  . Channel 1230. .  . Pre-processing unit, post-processing ordering —- early 兀 1232... wet scrubber 1233. .  . Pumps 58 200837310 1234. .  . Quench cooler 1236. .  . Exhaust gas 1238. .  . Pipeline network 1242. .  . Pre-processing unit 1243. .  . Tube bundle 1244. .  . Channel 1302...reoxidation chamber 1303. .  . Multi-head valve 1304·. ·Check valve 1306...pressure regulator 1308. .  . Control valve 1310. .  . Flash fire suppressor 1312. .  . Brown gas burner 1313. .  . Grid block 1314. .  . Flue gas 2102. .  . Flue gas venting device 2103. .  . Flue gas 2104...first processing chamber 2106...second processing chamber 2108. ··The third processing room 2110. .  . Brown gas storage tank 2111. .  . Relief valve 2112. .  . Pipeline network 2114. .  . Check valve 2116. .  . Corner valve 2118. .  . Pipeline network 2121. .  . Pipeline network 2122. .  . Pipeline network 2124...pressure regulator 2126. .  . Control valve 2128. .  . Flash fire suppressor 2130...burner 2132...pressure regulator 2134. .  . Control valve 2136. .  . Flash fire suppressor 2138. .  . Burner 2140. ··Pressure regulator 2142. .  . Control valve 2144. .  . Flash fire suppressor 2146. .  . Burner 2148...water pipe steam boiler 2150...water filled water pipe 2152. .  . Water vapor drum 2154. .  . Water vapor 2156. .  . Water vapor turbine 2158. .  . Generator 2160. ··Spindle 2162. .  . Bypass pipe 59 200837310 2166...Heat exchanger 2168···Power grid 2170···帮浦 2172. .  . Water supply source 2174. .  . Pipeline network 2176. .  . Gas scrubbing assembly 2178...wet scrubber 2180...fluid spray nozzle 2182. .  . Fluid 2184·. ·The pump 2186...processing unit 2188. .  . Quench cooler 2190. .  . Water spray nozzle 2192. .  . Pump 2194... exhaust gas 2196. .  . Pipeline network 2194... exhaust gas 60

Claims (1)

200837310 X. Patent application scope: 1. A system for generating, storing and using Brown gas, comprising: • at least one Brown gas generator connected to a power source and a water source; at least one first storage chamber, Connected to the generator for storing Brownian gas produced by the generator; and - the Brown gas application device is in communication with the at least one first storage chamber, wherein the generator and the first storage chamber are located adjacent to the Brown Gas application device. * 10 15 20 2. The system of claim 1, wherein the at least one first storage tank contains a predetermined amount of liquefied hydrocarbon. 3. The system of claim 2, wherein the liquefied tobacco is selected from the group consisting of hexane, heptane, methanol, and ethanol. 4. The system of any of the preceding claims, wherein the applicator comprises at least one first chamber for producing hot water, wherein the heat for heating the hot water is derived from the cloth, Brown The gas system is obtained from the first storage chamber. 5. The system of claim 4, wherein the at least one first chamber is a boiler and burner unit. H. The system of claim 4, wherein the at least the chamber comprises: a first inlet - a second inlet for receiving one of the Brown gas by the at least one first storage chamber - a second inlet; 61 200837310 a gas burner; and - discharging one of the hot water produced by the discharge, wherein Brown gas from the first inlet is combustible by the gas burner, thereby heating water from the second inlet; and wherein the The heated water can be discharged from the outlet. 7. The system of claim 6 wherein the second inlet for receiving water is connected to an outlet of at least one heat exchanger contained within the at least one Brown gas generator. 8. The system of claim 6 or claim 7, further comprising at least one flash arrester in front of the first inlet. The system of any one of claims 4 to 8, wherein the at least one first chamber comprises a reactive metal element. 10. The system of claim 9, wherein the reactive metal element is selected from the group consisting of: primary, steel, chrome or high temperature alloy. The system of any one of claims 4 to 1 further comprising at least one second storage chamber for storing hot water. 12. The purity of item U of the patent application, wherein the at least one second storage chamber is connected to an outlet of the at least one first chamber. 13·^ The foregoing claims are in the purview of each of the patents, wherein the applicator further comprises at least one second chamber for making cooling water. 14. The system of claim 13 wherein the at least one chamber is an absorption chiller unit. 15. The system of claim 13 or 14, wherein the at least one of the 62th 200837310 two chambers comprises: - receiving a first inlet of an absorbent; - receiving a second inlet of a refrigerant; - receiving cooling a third inlet of water; 5 - a fourth inlet for receiving warm water; - a first heat exchanger; - a second heat exchanger; - a first outlet for discharging warm water; and - a discharge manufactured One of the second outlets of the cooling water, 10 wherein the third inlet and the first outlet are connectable to the first heat exchanger, and the fourth inlet and the second outlet are connectable to the second heat exchanger. The system of claim 15, wherein the absorbent is selected from the group consisting of lithium bromide (LiBr) and ammonia (NH3). 15. The system of claim 15 or 16, wherein the refrigerant is water. The system of any one of claims 15 to 17, wherein the fourth inlet is connected to the at least one second storage chamber. 19. The system of any one of claims 13 to 18, further comprising at least one third storage chamber storing the cooling water. The system of any of the preceding claims, wherein the applicator further comprises at least one third chamber of the combustion waste. 21. The system of claim 20, wherein the at least one third chamber comprises: - a combustion unit that burns waste by burning Brown gas; 63 200837310 - a connection for receiving waste to one of the combustion units An inlet for receiving a Brownian gas from the at least one first storage chamber to a second inlet of the combustion unit; and - for discharging a flue gas produced by the combustion unit for connection to the combustion One of the units is exported. 22. The system of claim 21, further comprising at least one flash arrester in front of the first inlet. 23. The system of claim 21 or 22, further comprising a heat exchanger coupled to the outlet for discharging flue gas. 10 24. A boiler and burner unit for the manufacture of hot water, the boiler and burner unit comprising: - a first inlet for receiving feed water; - a second of Brown gas from a Brown gas generator An outlet; and 15 - an outlet for the hot water produced by the discharge, wherein the Brown gas is combusted to generate heat, which heats the feed water to produce hot water. 25. The boiler and burner unit of claim 24, wherein the outlet for hot water produced by the discharge is connected to a storage tank for heat 20 water produced by the storage. 26. The boiler and burner unit of claim 25, wherein the first inlet of the boiler and the burner unit is connectable to: an outlet of the first heat exchanger of one of the Brown gas generators; at least one solar heat collection The outlet of the device, and/or the storage tank for storing the hot water produced. 64 200837310 27. A system for recovering heat generated by combustion of a combustion material, comprising: - at least one Brown gas generator connected to a power source and a water source; - for storing Brownian gas produced by the generator At least one first storage chamber in fluid communication with the generating device; - at least one combustion chamber for communicating the combustion material in communication with the at least one first storage chamber; and - adapted to receive combustion from the combustion material At least one heat eliminator chamber from the heat generated by the combustion chamber, wherein the generator and the first storage chamber are located adjacent to the combustion chamber and the heat extraction chamber. 28. The system of claim 27, wherein the at least one combustion chamber comprises: - a combustion unit for burning the combustion material by burning Brown gas; 15 - a connection for receiving the combustion material to the combustion unit One into V; - a connection to receive a Brownian gas from the at least one storage chamber to a second inlet of the combustion unit; and - a connection to discharge the flue gas produced by the combustion unit to the 20 combustion unit One of the exports. 29. The system of claim 27 or 28, wherein the combustion material is waste. 30. The system of claim 28 or 29, wherein the at least one hot extraction chamber is a boiler unit for making steam, and the hot water is used to produce a steam. The 2008 200310 heat system is derived from the flue generated by the combustion unit. gas. The system of any one of claims 28 to 30, wherein the at least one hot extraction chamber comprises: - a water inlet; 5 - a flue gas inlet that receives the flue gas produced by the combustion unit Port; - one of the first outlets of the water vapor produced by the discharge; and - one of the second outlets of the flue gas, so that the water from the water inlet is heated by the flue gas 10 from the flue gas inlet Thereby, water vapor is generated, and wherein the water vapor is discharged from the first air outlet, and the flue gas is discharged from the second air outlet. 32. The system of claim 31, wherein the flue gas inlet of the at least one heat extraction chamber is connected to the outlet gas D 〇 15 of the at least one combustion chamber. 33, as claimed in claims 27 to 32. The system of any of the preceding claims, further comprising a power generating device in communication with the at least one heat extraction chamber. 34. The system of claim 33, wherein the power generating device comprises: - at least one water vapor turbine adapted to receive water vapor generated by the at least one first chamber; 20 - in communication with the at least one water vapor turbine At least one generator for power generation; and - a device that discharges power generated by the generator. 35. The system of claim 34, wherein the at least one water vapor turbine is a single stage steam turbine or a multi-stage steam turbine. The system of any one of claims 33 to 35, wherein the power of the power is supplied to the at least one Brown gas generator and/or a power grid. 37. The system of any one of claims 34 to 36, further comprising a heat exchanger in communication with the at least one water vapor turbine and the at least one hot extraction chamber. 38. The system of claim 37, wherein the heat exchanger comprises: - a water vapor inlet for receiving water vapor from the steam turbine; and a water outlet, wherein the heat exchange The device cools the water vapor received by the steam inlet, thereby condensing the water vapor to produce water; and wherein the water is discharged from the water outlet. 39. The system of claim 38, wherein the heat exchanger further comprises a second air inlet adapted to receive the at least one heat when the water vapor turbine reaches its maximum capacity Draw water vapor from the room. 40. The system of claim 38, wherein the water outlet of the heat exchanger is connected to a water inlet of the at least one hot extraction chamber. The system of any one of claims 27 to 40, wherein the at least one hot extraction chamber comprises a dryer for drying the combustion material prior to burning the combustion material in the combustion chamber. 42. The system of claim 41, wherein the heat of the dry combustion material is derived from the flue gas emitted by the combustion unit. The system of claim 41, wherein the dried combustion material from the dryer is combusted in at least one combustion chamber. 44. A method of recovering heat generated by combustion of a combustion material, the method comprising the steps of: - burning combustion material in at least one combustion chamber by burning Brownian gas; and - receiving a flue generated by the combustion chamber Gas is used to recover the heat. 45. The method of claim 44, further comprising the step of: 10 producing water vapor in a boiler, wherein the heat system for producing steam is derived from the flue gas produced by the combustion chamber. 46. The method of claim 45, wherein the method further comprises the steps of: - feeding the produced water vapor to at least one water vapor turbine; 15 and - providing communication with the at least one water vapor turbine for use Generator for power generation. 47. The method of claim 46, wherein the power generated by the power is supplied to the at least one Brown gas generator and/or a power grid. The method of claim 46, wherein the at least one steam turbine is a single stage steam turbine or a multi-stage steam turbine. 49. The method of claim 44, further comprising the step of drying the combustion material prior to combustion in the at least one combustion chamber, whereby the heat from drying the combustion material is derived from the flue gas produced by the combustion chamber. The method of claim 44, wherein the dried combustion material from the dryer is combusted in at least one combustion chamber. 51. An assembly for treating flue gas before it is discharged into the atmosphere, comprising: 5 - at least one processing chamber for receiving and heating the flue gas; - a device for burning brown gas to supply flue gas heating And discharging part of the heated flue gas. 52. The assembly of claim 51, further comprising at least one component in the at least one processing chamber, wherein heating the flue gas adjacent to the at least one component achieves a higher heating efficiency of the flue gas. 53. The assembly of claim 52, wherein the at least one component comprises a grid block, wherein the grid block is encased in the at least one processing chamber. 54. The assembly of claim 53, wherein the grid block is made of 15 platinum, steel, nickel-chromium alloy or aluminum-chromium alloy or a combination thereof. 55. The assembly of any one of clauses 51 to 54, wherein the apparatus is a Brown gas burner. 56. The assembly of any one of clauses 51 to 55, wherein the at least one processing chamber is heated to a temperature above 500 °C. The assembly of claim 56, wherein the at least one processing chamber is heated to a temperature above 800 °C to 1600 °C. 58. The assembly of any one of clauses 51 to 57, wherein the assembly comprises three processing chambers configured to sequentially pass flue gas through each of the three processing chambers room. The assembly of any one of claims 51 to 58 further comprising a heat extraction chamber adapted to receive a heated flue gas. 60. The assembly of claim 59, wherein the hot extraction chamber comprises a boiler unit for producing steam, and the heat system for producing steam is derived from the heated flue gas. 61. The assembly of claim 59 or 60, wherein the hot extraction chamber comprises: - a water inlet; - a water vapor outlet; and a 10 - a flue gas outlet, the heat is not configured The flue gas is allowed to heat the water to produce water vapor. 62. The assembly of any one of claims 51 to 61, further comprising a power generating device in communication with the hot extraction chamber. 63. The assembly of claim 62, wherein the power generating device comprises: 15 - at least one water vapor turbine adapted to receive water vapor generated by the hot extraction chamber; - in communication with the at least one water vapor turbine At least one generator for power generation; and - means for discharging power produced by the generator. The assembly of claim 63, wherein the at least one water vapor turbine is a single stage steam turbine or a multi-stage steam turbine. The assembly of any one of clauses 62 to 64, wherein the generated power is supplied to a power grid. 66. The assembly of any one of clauses 63 to 65, further comprising 70 200837310 comprising a heat exchanger in communication with the at least one water vapor turbine and the hot extraction chamber. 67. The assembly of claim 66, wherein the heat exchanger comprises: - a first inlet 5 port for receiving water vapor from the steam turbine; and - a water outlet, wherein the heat exchange The device can condense water vapor to produce water; and wherein the water system is discharged from the water outlet. 68. The assembly of claim 67, wherein the heat exchanger further comprises a second air inlet adapted to receive heat from the water when the water turbine reaches its maximum capacity. The water vapor produced by the chamber. 69. The assembly of claim 67 or 68, wherein the water outlet of the heat exchanger is connected to the water inlet of the hot extraction chamber. 70. The assembly of any one of claims 51 to 69, further comprising a scrubber assembly comprising a flue gas scrubber; and wherein the scrubber assembly is It is suitable for receiving flue gas from the flue gas outlet portion of the heated flue gas and/or the flue gas outlet of the hot chamber. 71. The assembly of claim 70, wherein the flue gas scrubber is a gas eliminator. 20 72. The assembly of claim 71, wherein the scrubber is selected from the group consisting of: a wet scrubber, a thin waist pipe scrubber, a stamped plate scrubber, and a spray tower scrubber. group. The assembly of any one of claims 70 to 72, wherein the scrubber assembly is further included in a device for cooling flue gas before being discharged into the atmosphere. 74. The assembly of claim 73, wherein the flue gas cooling device is a quench. 75. For the assembly of claim 73 or 74, wherein the flue gas is cooled, the device cools the flue gas to a temperature below 300 °C. 76. A method of treating flue gas prior to discharge into the atmosphere, comprising the steps of: - providing flue gas to the at least one processing chamber; - providing Brown gas to a Brown gas combustion device; and 10 - burning the brown The flue gas is heated to a predetermined temperature. 77. The method of claim 76, wherein the heating step comprises heating the flue gas in the presence of at least one member that achieves a higher heating efficiency. 78. The method of claim 76, wherein the Brown Gas Combustion 15 device is a Brown Gas burner. The method of any one of claims 76 to 78, wherein the predetermined temperature is higher than 700 °C. The method of any one of claims 76 to 79, wherein the flue gas system is supplied to three processing chambers, the flue gas system sequentially passing through three chambers of three treatment chambers. 81. The method of claim 80, further comprising the steps of: - providing flue gas to a first processing chamber; - heating the flue gas in the first processing chamber to a first by burning Brown gas a predetermined temperature; 72 200837310 - directing the heated flue gas from the first processing chamber to the second processing chamber; - heating the flue gas in the second processing chamber to a second predetermined temperature by burning Brown gas 5 - directing the heated flue gas from the second processing chamber to the third processing chamber; and - heating the flue gas in the third processing chamber to a third predetermined temperature by burning Brown gas. 82. The method of claim 81, wherein the first predetermined temperature is about 10 ° 800 ° C. 83. The method of claim 81, wherein the second predetermined temperature is about 1000 °C. The method of any one of claims 81 to 83, wherein the first predetermined temperature is about 1200 °C. The method of any one of claims 76 to 84, further comprising the step of producing water vapor in a heat extraction chamber, wherein the heat of the water vapor is derived from the heated flue gas. 86. The method of claim 85, further comprising the steps of: - feeding the produced water vapor to at least one steam turbine; 20 and - providing a connection with the at least one water vapor turbine for generating electricity Motor. 87. The method of any one of claims 76 to 86, further comprising the steps of: 73 200837310 - flue gas after scrubbing in a flue gas scrubber; and/or - in the flue The heated flue gas is cooled in the air cooling device. 88. The method of claim 87, wherein the flue gas system is cooled to a temperature below 300 °C. 74