CN201203151Y - Apparatus for instantly gasification combusting biomass - Google Patents

Abstract

Disclosed is a biomass instant gasification burning device which is composed of a main stove, a gas stove and a pipeline connecting piece. The utility model is characterized in that the main stove comprises an upper part and a lower part. The upper part is a smokeless cleaning feeding gas guide device, and the lower part is an infrared insulation reaction barrel. The barrel wall of the infrared insulation reaction barrel is internally provided with a controllable vacuum superconducting device which extends outsides the stove and/or infrared heating materials, as well as the lower part of the infrared insulation reaction barrel is provided with an ignition gas supply device; the gas stove is provided with an annular splint condenser, an infrared burner and a water seal oil-water separator or a liquid seal groove or a U-shaped liquid seal pipe, an inside hollow part of the annular splint condenser is provided with a gas supply regulating device, and meanwhile, the infrared burner is internally provided with the infrared heating materials having the advantages of no dust and tar pollution, safety, environmental protection, high efficiency, energy conservation and great development value.

Description

Biomass instant gasification uses device

Technical field:

The utility model relates to a kind of living beings gasification and uses device, and the biomass instant gasification of especially a kind of " not air storage of bin stock " uses device, belongs to biomass energy cleaning trans-utilization technical field.

Background technology:

The gasification furnace that living beings can be changed into combustion gas at present is of a great variety, but because the secondary pollution problem of flue dust and tar can not get effective solution always, cause China's living beings gasification to utilize work progress slow, the living beings of having gone into operation concentrate gasifying supplier also most of in paralyzed state, and vast farmers still is forced to use traditional bavin kitchen range or the honeycomb briquette stove that the thermal efficiency is low and smoke contamination is very serious.Utilize flue dust and tar pollution problem in the process in order to solve living beings gasifications, country stares at sight in the research and development of " gasification process and the device that do not have burnt combustion gas " about scientific research department always, and ignored containing the research of burnt biomass fuel gas firing, especially ignored the research that the biomass instant gasification to " not air storage of bin stock " uses method and device, as Chinese patent " the thermal-cracking decoking biomass gasification furnace " (patent No.: ZL00101428.5) and " a kind of low-tar biomass gasifying method and device " (patent No.: ZL200510043836.0) or the like, these are intended to obtain the gasification process of " not having burnt combustion gas " and install not only complex process, the equipment manufacturing cost height, operation easier is big, gasification cost height, and since its rely and biomass coke tar is carried out catalytic bed or Pintsch process district that cracking transforms be limited anoxic zone, when the biological fuel gas that contains tar (macromolecular organic compound) is flowed through this anoxic zone, be difficult to obtain to be enough to make " the big molecule of tar " to realize that complete cracking transforms required reaction condition and (comprises the time of staying, supply of reaction temperature and ionic group or the like), thereby its final gained biological fuel gas still contains a certain amount of biomass coke tar inevitably, this biological fuel gas that contains tar is not suitable for utilizing pipeline to carry at a distance, can not realize completing combustion at the general gas kitchen range kitchen range of prior art, thereby can not be used for civil area.

In contrast, the gasification furnace among the people that some are propagandized hotly just throughout the country, though on the global design technology of living beings gasification and burning, explore to some extent, but for want of to the further investigation of living beings gasifications and fuel gas buring mechanism thereof, mostly flow in low-level simple combination, thereby in actual use, flue dust and tar pollution are still, 200610166019.9) and Chinese patent Chinese patent application for example: a kind of integral compound gasification stove (application number:: biomass gasifying furnace igniting and gasification installation (patent No. ZL200520050980.2) and supporting biomass gas appliance (patent No. ZL03284074.8) thereof or the like, just there is extremely serious tar pollution problem in actual use, just because of this, the existing biomass gasifying furnace that every for a long time inflow family uses and use device, all become the household arrangement of these users " the labor life is lost money " bar none, trace it to its cause, mainly be the biomass gasifying furnace of prior art and use device above-described except that existing " tar pollution ", also have the various scarce limit of the following stated simultaneously more or less:

1, smoke contamination is very serious, uncaps when feeding in raw material especially midway, and fire door all has dense smoke to overflow, have a strong impact on normal operation, not only can not improve the weather of peasant's existing " smoke fire burns ", increased the weight of peasant's indoor pollution degree on the contrary to a certain extent, so the peasant can not accept;

2, aerogenesis speed is slow, aerogenesis off and on, the system gas very unstable, thereby influence normal cooking operation;

3, fuel gases calorific value is little, and flame temperature is low, and its heat flow can not satisfy the normal need of the cooking of generally cooking;

4, combustion gas quality is poor, and fuel gas buring is incomplete, and burner is lighted difficulty, and secondary pollution is more serious;

5, main furnace igniting inconvenience, and when igniting smoke contamination serious;

6, the materials requirement is very strict, can not use the higher material of moisture content, more can not add house refuse in stove, thereby can not be used for garbage disposal;

7, material utilizes insufficiently, and the thermal efficiency is low, and energy-saving effect is poor;

8, bank up a fire and lose gas in the stove of back and escape, can cause secondary pollution, have a strong impact on the healthy of user and surrounding resident, the adverse environment protection indoor and outdoor surroundings;

9, equipment fault is many, and operation easier is big, and service life is short, the assembling maintenance difficult.

Think through inventor's years of researches:

1, " water " is that the living beings gasification utilizes in the process, produce " flue dust and tar pollution " main arch-criminal, be to influence the living beings gasification and make biological fuel gas be difficult to the one of the main reasons that realizes completing combustion and produce secondary pollution, it simultaneously also is one of principal element of influence " fuel gases calorific value; the flame temperature and the thermal efficiency ", therefore, must give strict control, but for a long time, scientific worker both domestic and external is used as the dotey to " water " always, that have in addition biomass gasifying furnace as coal gasification furnace " moisturizing " or combustion gas condensate liquid (moisture more than 90%) all returned gasification furnace in stove, Chinese patent for example: a kind of producer (patent No. ZL 200520052111.3) just is provided with water replanishing device in its gasification reacting furnace, in fact concerning not doing the biomass gasifying furnace of gasifying agent with pure oxygen, moisturizing or charge into the practice of water vapour in the stove, it is a kind of wrong practice that loses more than gain, also be domestic and international scientific worker's big thought mistaken ideas, we can say that it has hindered the development of biomass energy cleaning trans-utilization technology to a certain extent;

2, tar is a kind of high-grade energy, if can be reasonably trans-utilization in addition, not only can greatly improve fuel gases calorific value and flame temperature, produce bigger heat flow, also can effectively avoid secondary pollution simultaneously, therefore, exert it is thoroughly removed from combustion gas with it, not as making the best use of the situation, reasonable diffluence, a part is collected standby after liquefying or is imported once more and participates in second pyrolysis and burning in the stove, and another part enters burner by it with combustion gas, and manages to make it to realize completing combustion in burner.

In fact, at the international level in, a kind of nothing " flue dust and tar " is polluted, and can effectively overcome the above biomass instant gasification that all lack limit of prior art and use device, yet there are no report so far.

Summary of the invention:

The purpose of this utility model is to provide a kind of no flue dust and tar pollution at the deficiency of prior art, and can effectively avoid the above all scarce biomass instant gasification of limitting of prior art to use device.

For reaching above-mentioned purpose, the utility model adopts following technical scheme:

A kind of biomass instant gasification uses device, form by main stove, gas-cooker and pipeline connecting parts, described its profile of main stove can be a technology vase formula streamlined structure, it also can be the contour structures of cylindrical or other shape, no matter how its profile includes upper and lower two parts, top is smokeless cleaning charging gas operated device, and the bottom is infrared adiabatic reaction bucket, and is provided with the igniting feeder in the bottom of described infrared adiabatic reaction bucket; Described smokeless cleaning charging gas operated device is made up of the material storage barrel of upper and lower opening and the sealing bell that is arranged on this material storage barrel upper port, and be provided with " squirrel-cage " annular condensation liquefaction diffluence room and/or annular air channel the week of described material storage barrel laterally, and described annular condensation liquefaction diffluence room and/or annular air channel communicate with described infrared adiabatic reaction bucket; Described material storage barrel is material envelope formula material storage barrel or the sealed material storage barrel of gas material, wherein, described material envelope formula material storage barrel is that empty cylindrical shell and top are that cylindrical lower portion is an empty cylindrical shell in the combined type of truncated inverted cone shape in empty cylindrical shell in upper and lower opening cylindrical, the truncated inverted cone shape; The sealed material storage barrel of described gas material is made up of described material envelope formula material storage barrel and the truncated inverted cone shape feed hopper that is arranged in the described material envelope formula material storage barrel, and is provided with inlet duct on the annular passage that is made of described feed hopper and described material envelope formula material storage barrel bucket wall; Described sealing bell is for the usual pressure sealing bell of making encapsulant with various sealing gaskets or sealing ring or make the traditional gravity sealing bell of encapsulant or band water vapor condensate with water, high-hydroscopicity resin, adhesive sticker mud, noninflammability inorganic material powders and noninflammability liquid and divide the multifunctional gravity that the multi-functional pressure sealing bell that flow device or band water vapor condensate divide stream device and/or air-pressure balancing device and seal bell; Described water vapor condensate divides the stream device, combine by the distributing damper and the bell shell that are arranged in the described sealing bell, and in the annular intake chute that is constituted by described distributing damper and bell shell, be provided with fluid guidance port, and on described distributing damper, be provided with at least one ventilation mouth; Described air-pressure balancing device is to be arranged on the gas permeable devices that described Sealing furnace covers, and is made up of control piece and ventilation mouth, and described control piece is a sealing-plug or by the combination of permeability cell and Pneumatic valve, spring valve or seal cover; Described infrared adiabatic reaction bucket is made up of infrared fire-resistant bucket and thermal insulating warm-keeping layer of being arranged on around its outside, described infrared fire-resistant bucket is the common metal bucket, the heat-resisting alloy bucket and in establish the composite wood charging basket of infrared heating material or their combination, described thermal insulating warm-keeping layer is the thermal current heat-insulation layer, vacuum heat-insulating layer, a kind of in the inserts heat-insulation layer or point to the heat-reflecting layer and the thermal current heat-insulation layer of reaction container central axis by reflection direction, vacuum heat-insulating layer, a kind of high temperature resistant infrared composite heat-insulating layer that combines in the inserts heat-insulation layer, one cover also can be set in the wall at the bucket of described infrared adiabatic reaction bucket in case of necessity adorn the superconducting device of superconducting fluid in stretching to stove outside, and in described superconducting device, controlled superconducting pipe is set, described controlled superconducting pipe and the interior empty that communicates with it have enough big interior empty volume, the maximum gas pressure that its compressive resistance may occur after being gasified totally greater than described superconducting fluid; Described igniting feeder is combined by electric heating air igniter, alternating temperature vaporizer and inlet duct or electric heating air igniter and inlet duct or air plasma generator and inlet duct or igniting ash hole and inlet duct; Described electric heating air igniter is made up of blast pipe and electric calorifie installation two parts, described blast pipe communicates with described electric calorifie installation, wherein said electric calorifie installation is again by air preheating chamber, infrared excitation chamber and the infrared electric heating body that is arranged in this infrared excitation chamber are formed, described infrared electric heating body is an infrared heating porous electric furnace pan, infrared heating porous ceramic plate and high temperature resistant heating or heat-resisting alloy pipe, the combination of electrician's level magnesia and high temperature resistant heating or carborundum and high temperature resistant heating or silicon nitride and high temperature resistant heating, described high temperature resistant heating is common electric furnace heating wire, the common electrical heated filament, the high-temperature electric resistance furnace silk, high-temperature electric heat silk or tungsten filament; Described inlet duct is the combination of annular passage, blast pipe, air blast and control valve or molecule fission promoters, blast pipe, air blast and control valve or blast pipe, air blast and control valve, and communicates with described alternating temperature vaporizer, electric heating air igniter, air plasma generator or material storage barrel; Described molecule fission promoters is pagoda shape eddy flow or the efficient oxygen supply air guide of jet nozzle, be made by heat-resisting metal or nonmetal heatproof material more than 800 ℃, described heat proof material is a heat-stable ceramic, plain cast iron, heat-resisting cast iron or heat resisting steel, high temperature resistant molten admittedly catalyst also can be set in case of necessity therein, by cylinder, central airway, the venthole and the pore the brim of a hat are formed, described central airway is arranged on the interior central axis of described cylinder, be cylindrical air guide channel, simultaneously be provided with at least one the pore the brim of a hat laterally, and the cylinder upper edge under every pore the brim of a hat circumferentially is laid with at least 2 ventholes in described cylindrical week; Described venthole communicates with described central airway and is downward or level rotary flow venthole, a kind of downwards or in the horizonally projected jet venthole;

Described gas-cooker is provided with annular clamping plate condenser, and be provided with infrared burner in the top or the outside of described annular clamping plate condenser, inside position at described annular clamping plate condenser is provided with the air feed regulation device, is provided with hydrolock oil water separator, liquid seal trough or U type liquid sealing pipe in the bottom of described annular clamping plate condenser; Described annular clamping plate condenser is that rectangle desk formula four foot supports and two thickness being looped around inside and outside four foot supports combine at the annular sheet that is optimized for below the 3mm below the 1mm by cross section, and place the middle and upper part of described four foot supports, be empty sealed cylinder in the indirect cooled annular of an air, on the wall of described annular clamping plate condenser, be provided with air inlet pipe, escape pipe and fluid guidance port simultaneously; Described annular clamping plate condenser also can be single pin, both feet or multiway support or their combination of triangle, square, circle, ellipse or other shape and be looped around inside and outside the set support and thickness combines at the annular sheet that is optimized for below the 3mm below the 1mm by cross section; Described infrared burner is the common burner of heat sublimation burner, common infrared ray burner or band infrared energy-conserving cover; Described heat sublimation burner is made up of air inlet pipe, housing, infrared heating porous ceramic plate, the agent of graininess infrared heating and/or high temperature resistant infrared heating alloy silk screen, and in described infrared heating porous ceramic plate, be provided with the infrared heating agent, the particle diameter of described graininess infrared heating agent is greater than the mesh aperture of described infrared heating porous ceramic plate, and is arranged on the described infrared heating porous ceramic plate; Described high temperature resistant infrared heating alloy silk screen is arranged on the top of agent of described graininess infrared heating and/or infrared heating porous ceramic plate; Described infrared heating porous ceramic plate comprises that preferred 16～17 orders of 15～18 orders, each mesh area are 0.78～1.89mm ²Preferred 1.12～1.38mm ², thickness of slab is that the preferred 12～15mm of 10～20mm, wall thickness are the support type infrared heating porous ceramic plate that thin wall type plane infrared heating porous ceramic plate, corrugated surface infrared heating porous ceramic plate and the surface applied of the preferred 0.4mm of 0.3～0.5mm has combustion catalyst; The sphere that described infrared energy-conserving cover is a upper and lower opening, hemispherical, variant sphere, conical butt or top are empty cylindrical shell in the columniform infrared thermal insulation for the conical butt bottom; Described air feed regulation device is gas-liquid separator, revolve the combination of branch separator, aid distributing pipe, escape pipe, evacuated tube and control valve or aid distributing pipe, escape pipe, evacuated tube and control valve or air blast, aid distributing pipe, escape pipe, evacuated tube and control valve or gas-liquid separator, the combination of revolving branch separator, escape pipe, evacuated tube and control valve or aid distributing pipe, escape pipe, evacuated tube, distribution bucket and control valve or above various assembly and tempering warning device or tempering warning self-con-tained unit; Described distribution bucket is one to be provided with the interior empty of fuel gas inlet, air intlet, condensate outlet and mixed gas outlet; Described control valve is Pneumatic valve, exhaust-valve, collection control valve, regular tap valve or magnetic valve; Described collection control valve is by the cylindrical interior empty cylindrical shell of inside and outside two one ends sealing other end opening, be that inner barrel and outer cylinder body socket combine, and be provided with valve handle at the blind end of described inner barrel, on the circular side wall of described inner barrel, be provided with at least one through hole, on described valve handle, be provided with or the binomial that is selected from pointer and the positive stop strip simultaneously; On described outer cylinder body, be provided with at least two pipe joints, wherein be arranged on described outer cylinder body blind end and not with the inner barrel lap on pipe joint be the normal open pipe joint, the pipe joint that is arranged on the remainder is controlled pipe joint, and the openend at described outer cylinder body is provided with or the binomial that is selected from sealing location end cap and the function direction board simultaneously; Described hydrolock oil water separator is made up of hopper, feed tube, tar delivery line and water delivery line, and the liquid outlet of the tar overfall of described tar delivery line and described feed tube all is positioned under the water overflow outlet of described water delivery line; Described infrared heating material is the combination that is selected from a kind of in infrared heating agent and the high temperature resistant infrared heating alloy silk screen or two kinds, and described infrared heating agent is magnesia, zinc oxide, zirconia, iron oxide, aluminium oxide, silica, carborundum, silicon nitride or their combination; Described high temperature resistant infrared heating alloy silk screen comprises that preferred 6 orders of 5～7 orders, each mesh area are 8～16mm ²Preferred 8.0～11mm ², silk footpath is the Aludirome silk screen of the preferred 0.8～0.9mm of 0.7～1.1mm.

Utilize the utility model to realize that the mechanism of action of the safe and efficient cleaning trans-utilization of biomass energy is:

At first, infrared heating material described in the utility model, the electromagnetic infrared wave that energy fast Absorption " pyrotoxin " is sent when being heated, cause its electron outside nucleus to transit to the high level track rapidly and constantly outwards launch electromagnetic infrared wave by the low-lying level track, produce heat radiation, because the molecule activation of infrared heating material described in the utility model energy and electron work functon are higher, its surperficial high energy electron not can or very difficult effusion material surface and cause free radical, more can in gas phase, not produce the excited electronic state product, thereby itself the energy loss that physical deterioration does not have visible light yet can not occur, when adding owing to the utility model work, remove more fully to being mixed in water in reaction mass and the hot combustion gas or water vapour, removed main polar compound---the H of generation absorbing and cooling temperature effect when living beings gasification and fuel gas buring ₂O, thereby, can formation temperature accumulate in its surperficial moment, produce the surperficial high temperature below 1300 ℃, therefore, when described infrared heating material is used for biomass gasification reaction, can make the reaction mass fast dewatering in the infrared adiabatic reaction bucket and reach higher molecular balance temperature, make that the redox reaction and the pyrolytic gasification reaction of the interior material of stove are fierce more and complete, thereby increase substantially the utilization rate of the interior material of stove, output capacity combustible gas; Because the reaction mass that drops in the stove has been removed discarded metals such as copper, aluminium in advance, add in described infrared adiabatic reaction bucket and be in anaerobic condition all the time, preferential and a large amount of C, the H atoms of only oxidation atom combines in the reaction container, Cu, Al etc. are difficult for oxidized, thereby have suppressed CuO and CuCl to greatest extent ₂Deng the generation of " dioxin " secondary synthetic catalyst, therefore, the chemical reaction that does not almost have " dioxin " precursor secondary synthetic " dioxin " in infrared adiabatic reaction bucket takes place; And when described infrared heating material is used to contain burnt biomass fuel gas firing, can make the little molecule combustible gas and the big molecule of tar class thereof that enter its surperficial high-temperature region, comprise that therefore " dioxin " and the precursor fast-neutron fission thereof that may exist also cause free radical, because the initiation of combustion gas free radical occurs in the surperficial high-temperature region of red-hot infrared heating material, at this moment, add that the utility model is provided with sufficient air-breathing, thereby make biological fuel gas can realize completing combustion in its surperficial high-temperature region, and unlikely excited electronic state product that produces in the gas phase beyond its surperficial high-temperature region or its---therefore the pyrocarbon particulate also causes the visible light that causes occurring energy loss, thereby make that the heat energy conversion of biological fuel gas is more abundant, issuable CO in the time of the combustion gas spontaneous combustion can effectively being avoided again simultaneously, the secondary pollution of HC and " dioxin "; Add because the temperature (below 1300 ℃) of its surperficial high-temperature region is lower than NO _XFormation temperature (more than 1500 ℃), make airborne nitrogen can not or be difficult to combine generation NO with oxygen atom _X, from and issuable NO can effectively avoid the combustion gas spontaneous combustion time _XSecondary pollution; Just owing in use of the present utility model, finally do not have CO, HC, NO at the burner position yet _XThe generation of " dioxin " isopolarity compound, HCl, H in the final gained biological fuel gas of the utility model simultaneously ₂S, SO ₂, H ₂O, NH ₃The content of isopolarity compound is extremely low again, adds the utility model and produces low heat value H ₂(Lower heat value 10743kJ/m ³) relative product high heating value CO (the Lower heat value 12636kJ/m of institute ³) content lower again, thereby the generation water proportion that is finally formed by the protium oxidation at the burner position is less relatively, thereby makes the utility model in the heat energy conversion process of biological fuel gas, compared with prior art, because of H ₂O, HCl, H ₂S, SO ₂, NH ₃, CO, HC, NO _XThe absorbing and cooling temperature effect that " dioxin " isopolarity compound is produced drops to minimum relatively, cause biological fuel gas bigger relatively in the heat flow that the burner position is produced, end flue temperature is higher, heat energy utilization is more abundant, therefore, the thermal efficiency of the present utility model is high, and energy-saving effect is fairly obvious; In addition, when the electromagnetic infrared wave that is sent when described " pyrotoxin " weakens to some extent, being in high energy electron on the infrared heating material High-Energy Orbit just can jump and get back on its low-lying level track, and equally outwards send electromagnetic infrared wave, produce heat radiation, make biomass gasification reaction temperature and fuel gas buring temperature big fluctuation can therefore not occur, therefore original chemical reaction is stablized and is carried out, thereby reaches the dual purpose of " stable gasification, smooth combustion " and " energy-efficient, environmental friendliness ".

Specify: sieve screen apertures described in the utility model " order " is defined as: the mesh count that is comprised in the length range of per inch (25.4mm).

The utility model compared with prior art has following feature and benefit:

1, can remove water or the water vapour that is mixed in reaction mass and the gained combustion gas fast, and fundamentally overcome the above ten big limit that lack of existing in prior technology comprehensively, thereby make the utility model can really become the effective tool of solution China rural area and peasant's cleaning living usefulness energy, and use in vast family, restaurant and the unit dining room that can be widely used in rural area and middle samll cities and towns, also can be used for industrial production, have energy-efficient and eco-friendly double effects, and manipulate fool proof.

But 2 digestion process " production and use of marsh gas device " the solid-state organic domestic waste of part that can not handle, thereby make that the utility model can be supporting with existing " firedamp gas equipment ", " innoxious, resource and minimizing " that solve the rural area organic domestic waste handles problems comprehensively.

Description of drawings:

Fig. 1 and Fig. 2 are the internal structure schematic diagrames of a kind of specific embodiments of infrared heating porous ceramic plate described in the utility model, and wherein Fig. 1 is a partial sectional view, and Fig. 2 is the mansion view; Fig. 3 and Fig. 4 are the internal structure schematic diagrames of a kind of specific embodiments of infrared heating porous electric furnace pan described in the utility model, and wherein Fig. 3 is A-A cutaway view, and Fig. 4 is the mansion view; Fig. 5 and Fig. 6 are the internal structure schematic diagrames of a kind of specific embodiments of infrared energy-conserving cover described in the utility model, and wherein Fig. 5 is B-B cutaway view, and Fig. 6 is the mansion view; Fig. 7 is respectively the internal structure schematic diagram of three kinds of different specific embodiments of molecule fission promoters described in the utility model with Fig. 8, Fig. 9 and Figure 10, Figure 11 and Figure 12, wherein Fig. 7, Fig. 9 and Figure 11 are for partly cuing open schematic diagram, and Fig. 8, Figure 10 and Figure 12 are respectively C1-C1, C2-C2 and C3-C3 cutaway view; Figure 13, Figure 14 and Figure 15 are respectively internal structure schematic diagram, mansion view and the side views of first kind of specific embodiments of electric heating air igniter described in the utility model; Figure 16, Figure 17 and Figure 18 are respectively the internal structure schematic diagrames of electric heating air igniter described in the utility model second, third and the 4th kind of specific embodiments; Figure 19 is respectively the internal structure schematic diagram of three kinds of different specific embodiments of heat sublimation burner described in the utility model with Figure 20, Figure 21 and Figure 22, Figure 23 and Figure 24, wherein Figure 20, Figure 22 and Figure 24 are respectively D1-D1, D2-D2 and D3-D3 cutaway view, but do not mark hatching among the figure; Figure 25～Figure 28 is the internal structure schematic diagram of first kind of specific embodiments of collection control valve described in the utility model, and wherein, Figure 25, Figure 26, Figure 27 and Figure 28 are respectively E1-E1, E2-E2, E3-E3 cutaway view and mansion view; Figure 29～Figure 32 is the internal structure schematic diagram of second kind of specific embodiments of collection control valve described in the utility model, and wherein Figure 29 is that E4-E4 cutaway view, Figure 30 are that E5-E5 cutaway view, Figure 31 are that E6-E6 cutaway view, Figure 32 are the mansion view; Figure 33～Figure 35 is the internal structure schematic diagram of the third specific embodiments of collection control valve described in the utility model, and wherein Figure 35 is that mansion view, Figure 34 are that E7-E7 cutaway view, Figure 33 are E8-E8 cutaway view; Figure 36～Figure 38 is the internal structure schematic diagram of the 4th kind of specific embodiments of collection control valve described in the utility model, and wherein Figure 38 is that mansion view, Figure 37 are that E9-E9 cutaway view, Figure 36 are E10-E10 cutaway view; Figure 73～Figure 74 is the internal structure schematic diagram of the 5th kind of specific embodiments of collection control valve described in the utility model, and wherein Figure 74 is E11-E11 cutaway view; Figure 39 and Figure 40 are the internal structure schematic diagrames of first kind of specific embodiments of hydrolock oil water separator described in the utility model, and wherein Figure 40 is that F1-F1 cutaway view, Figure 39 are F2-F2 cutaway view; Figure 41 and Figure 42, Figure 43 and Figure 44 are respectively the internal structure schematic diagrames of second and the third specific embodiment of hydrolock oil water separator described in the utility model, wherein, Figure 42 and Figure 44 are the mansion view, Figure 41 and Figure 43 are respectively F3-F3 and F4-F4 cutaway view, but do not mark hatching among the figure; Figure 45～Figure 54 is respectively the internal structure schematic diagram of ten kinds of different specific embodiments of main stove described in the utility model; Figure 55 and Figure 56, Figure 57 and Figure 58, Figure 59 and Figure 60, Figure 61 and Figure 62, Figure 75 is respectively the internal structure schematic diagram of five kinds of different specific embodiments of gas-cooker described in the utility model with Figure 76, Figure 55 wherein, Figure 57, Figure 59, Figure 61 and Figure 75 are respectively first, second, G1-the G1 of the third specific embodiments, G3-G3, G5-G5 cutaway view, G8-G8 the cutaway view that partly cuts open schematic diagram and the 5th kind of specific embodiments of the 4th kind of specific embodiments, Figure 56, Figure 58, Figure 60, Figure 62 and Figure 76 are respectively first, second, the 3rd, the 4th and G2-the G2 of the 5th kind of specific embodiments, G4-G4, G6-G6, G7-G7 and G9-G9 cutaway view, but all do not mark hatching among the figure; Figure 63～Figure 72 is respectively the contour structures schematic diagram of ten kinds of different specific embodiments of the utility model;

The title of each part is as follows with sequence number in the accompanying drawing: (wherein similar part has used same title and sequence number) infrared heating porous ceramic plate (1), mesh (2), infrared heating porous electric furnace pan (3), groove (4), air-vent (5), infrared energy-conserving cover (6), molecule fission promoters (7), connecting thread (8), cylinder (9), the pore the brim of a hat (10), venthole (11), central airway (12), electric heating air igniter (13), blast pipe (14), electric calorifie installation (15), air preheating chamber (16), infrared excitation chamber (17), electric furnace heating wire (18), pipe shell (19), housing (20), location-plate (21), positioning runner (22), seal cover (23), stealthy electrical socket (24), electric-heating assembly (25), porcelain ring (26), infrared electric heating body (27), pipe joint (28), heat sublimation burner (29), air inlet pipe (30), infrared heating agent (31), alloy silk screen (32), divide gas hood (33), collection control valve (34), outer cylinder body (35), inner barrel (36), through hole (37), valve handle (38), function direction board (39), pointer (40), sealing location end cap (41), hanger (42), installing hole (43), hydrolock oil water separator (44), hopper (45), tar delivery line (46), overflow pipe (47), sleeve pipe (48), feed tube (49), water delivery line (50), main stove (51), gas port (52), annular passage (53), connected entrance (54), igniting ash hole (55), infrared adiabatic reaction bucket (56), infrared fire-resistant bucket (57), thermal insulating warm-keeping layer (58), annular air channel (59), annular condensation liquefaction diffluence room (60), smokeless cleaning charging gas operated device (61), lower pumping valve (62), lower seal valve (63), controlled superconducting pipe (64), upper sealing valve (65), last extraction valve (66), pilot operated valve device (67), annular liquefaction heat release chamber (68), magnesium rod (69), annular reservoir (70), top reservoir (72), combustion chamber (73), return duct (74), permeability cell (75), Pneumatic valve (76), sealing bell (77), annular water tank (78), blowoff valve (79), wireway (80), material storage barrel (81), distributing damper (82), catheter (83), vacuum heat-insulating layer (84), inserts heat-insulation layer (85), bucket (87) in the metal, the outer bucket of metal (88), alternating temperature vaporizer (90), inlet duct (91), air blast (92), air plasma generator (94), cement output tank (95), insulation cover (96), hollow insulating lid (97), feed hopper (98), air guide catheter (99), thermal current heat-insulation layer (100), sealing-plug (101), ventilation mouth (102), retaining mechanism (103), fluid guidance port (104), air guide port (105), remove cinder notch (106), gas-cooker (107), support (108), aid distributing pipe (109), annular clamping plate condensers (110), escape pipe (112), liquefied gas cooker shell (113), gas-liquid separator (115), air feed regulation device (116), exhaust-valve (117), evacuated tube (118), cyclone separator (119), by-pass cock (121), starting switch (122), common infrared ray burner (123), standby port (124), ignition (125), common burner (127), equipment label (128), pipeline connecting parts (129), cold valves (130), control valve (131), positive displacement speed hot superconductive gas-fired water heater (132), positive stop strip (133).

The specific embodiment:

[embodiment one]

Instant gasification of biomass burning device, shown in Figure 63, from the main furnace (51), gas stove (107) and piping connected Contact member (129), with said main furnace (51) shown in Figure 45, the shape of vases Streamline structure, including Upper and lower two parts, the upper part is a smoke-cleaning gas feed guide means (61), the lower part of the infrared adiabatic reactor barrel (56), and in the Said infrared adiabatic reactor barrel (56) toward the outside of the furnace equipped with bucket wall, built superconducting liquid vacuum superconducting devices and infrared heat Agent (31), and in said superconducting device equipped with controllable vacuum over conduit (64), said vacuum-type superconducting device is volume Superconducting speed hot gas heater (132), the other in the infrared adiabatic reactor barrel (56) also has a lower portion of the ignition gas Means; said non-clean the feed air guide means (61) opening in the upper and lower storage tank (81) and arranged in the storage tank (81) Sealing lid on the port (77) composition and the storage tank (81) has a circumferential outer "squirrel cage" Circular Cold Shunt liquefied condensate chamber (60) and an annular air channel (59), and is condensed and liquefied in said split annular chamber (60) and an annular air channel (59) A shunt between the baffle (82), said ring is condensed and liquefied diversion chamber (60) and an annular air channel (59) and said infrared gem Thermal reaction barrel (56) is connected; said storage tank (81) for the upper and lower openings of the cylindrical sealing material storage tank, pressed the stored material Barrel (81) of insulating material to prevent the infrared reaction vat (56) within the generated gas from the furnace extraoral Yi; said sealing furnace Cover (77) for sealing material is water and the pressure balance with the gravity of the multifunction sealing lid; said pressure balancing means Is disposed in the sealing lid (77) on the ventilation device, made of breathable tube (75) and air control valve (76) composition; while The smoke-free clean feed air guide device (61) of the catheter (83) is provided with a water-sealed oil-water separator (44); from the Said water-sealed oil-water separator (44) tar solution through the inlet tube (49) is introduced into the variable-temperature gasification chamber (90) inside; Said infrared adiabatic reactor drum (56) by an infrared fire barrel (57) and disposed on the outside around the insulation layer (58) Composition, and said infrared fire bucket (57) equipped with infrared heating agent (31), said insulation layer (58) by Vacuum insulation layer (84) and filler material insulation layer (85), with said vacuum insulation layer (84) disposed in said specific red The outer refractory barrel (57) and filler insulation layer (85), between the superconducting device that the vacuum speed thermal superconducting gas volumetric heat Water heaters (132) of the basic components; volumetric velocity of the hot gas heater superconductor (132) by an annular storage chamber (70), Top of the storage chamber (72), a combustion chamber (73), sublimation burner (29) and disposed in said annular storage chamber (70) inside the Magnesium rod (69) and disposed in the annular storage chamber (70) to the outer circumferential annular liquefaction heat chamber (68) formed, and in the The outside is surrounded by a thermal insulation layer (58) in said top storage chamber (72) is provided with an overflow pipe (47) in said Annular storage chamber (70) at the bottom of a bathroom with cold water valve (130) of the inlet pipe, said inlet and overflow pipe (47) between A regulating valve (131) in said outer insulation layer (58) is provided with electronic ignition (125), said controllable super- Conduit (64) into said annular upper port liquefied heat chamber (68) of the interlayer and above the bottom 5 ~ 10cm, with When said controllable over conduit (64) of the pipeline in turn provided with a lower bottom pumping valve (62), the sealing valve (63), The sealing valve (65) and the gas vent valve (66), and said upper sealing valve (65) and above the pumping of the upper valve (66) Said opposite side, and also has a bypass return pipe (74) and means for controlling the hydraulic fluid return control valve (67), said return Flow tube (74) of the docking ports on the liquefaction heat of the annular chamber (68) at the bottom of the liquid guiding port (104); new furnace is enabled, Should be closed over the controllable catheter (64) on the lower sealing valve (63), turn on the sealing valve (65) and the pump valve (66), And drawn from the valve (66) to said controllable over conduit (64) into said inner superconducting liquid until filled with fluid in said superconducting Lower sealing valve (63) first sealing valve (65) and more than a conduit between the super-fluid pumped from said upper valve (66) until the spill, Then close the sealing valve (65), with a vacuum pump from the air valve (66) and a lower pumping valve (62), respectively, of said annular fluid Of the heat chamber (68) and a vacuum insulation layer (84) and the connecting pipe into the vacuum pump, and close the gas vent valve (66) And lower pumping valve (62) and remove its handle can; when the main furnace (51) ignition work, turn off the hydraulic control valve (67), playing Open lower sealing valve (63) and the upper sealing valve (65), this time in ultra-controllable catheter (64) All the superconducting fluid flows into the The main furnace (51) vacuum insulation layer (84), the material temperature as the furnace, the vacuum insulation layer (84) within the All superconducting fluid quickly vaporized and liquefied heat up to said annular chamber (68), the annular storage chamber (70) inside a cold Heat exchange water and converted into a liquid and collect in said return pipe (74), the time, said vacuum insulation layer (84) Has therefore become a vacuum state, and in the main furnace (51) gas production process has been to play its vacuum insulation effect; And when the main Gas furnace stopped, to prevent the material due to the pyrolysis furnace gas to escape while continuing emergence of secondary pollution, should be promptly furnace heat conduction To quickly reduce the temperature of the furnace at this time, simply open the hydraulic control valve (67), so that the superconducting fluid entered the furnace (51) inside the vacuum Insulation layer (84), the superconducting liquid within said vacuum superconducting device "endothermic gasification and liquefaction heat" cycle is repeated Can, therefore, you can use the furnace waste heat to provide hot water to the user at any time for bathing purposes, when there are many people who need a shower, you can also Restart the primary furnace (51) gas, and ignite in the volumetric gas water heater speed hot superconducting (132) of the heat rise China Burner (29), can ensure the required shower hot water supply; said ignition gas ignition device consists of ash outlet (55), Variable-temperature gasification chamber (90), electric air burner (13) and inlet means (91) formed, and in the variable-temperature gasification chamber (90) A leading upper portion of the furnace side of the inlet tube (49) in said variable-temperature gasification chamber (90) equipped with said annular duct (53) connected to a guide tube (80), said guide tube (80) and the inlet tube (49) in said variable-temperature gasification chamber (90) Dislocation was set up inside, and with the air provided in the electric igniter (13) on the upper housing communication port (54) correspond; The electric air burner (13) as shown in Figure 13 to 15, from the inlet duct (14) and electric means (15), with Of the inlet tube (14) and said heating means (15) is connected, wherein said heating means (15) and the air preheating chamber (16), infrared excitation chamber (17) and provided in the infrared excitation chamber (17) of the infrared heating element (27) composition; wherein The infrared heating element (27) by the infrared heating furnace perforated plate (3), general electric wire (18) and infrared heating porous ceramic plate (1), with said electric wire (18) disposed on said infrared heating furnace perforated plate (3) of the recess (4) inside, and Infrared heating furnace in said porous plate (3) and infrared heating porous ceramic plate (1) equipped with infrared heating agent (31); the Said intake device (91) by an annular duct (53), the inlet pipe (14), set the control valve (34) and a blower (92) composed of The variable temperature with said gasification chamber (90) and an electric air burner (13) is connected; said set of control valve (34) Figure 25 - Figure 28 shows, from the inside, the other outside two end closed cylindrical inner end opening of the inner cylinder air cylinder (36) and the outer cylinder (35) Socket combination and in said inner cylinder (36) provided round the closed end of the valve lever (38) in said inner cylinder (36) A circular side wall has three through-holes (37), wherein a long hole, the other two of the hole, while the valve handle (38) is provided with a pointer (40); said outer cylinder (35) is provided with a #, 2 #, 3 # and 4 # four fittings (28), Which provided in said outer cylinder (35) and not with the inner cylinder closed end (36) # 1 on the overlapping part is normally pass pipe fittings connected Head and the blower (92) is connected to the rest of the set 2 #, 3 # and 4 # control connector fittings are available, and the two # Pipe connector and said electric air burner (13) is connected through, # 3 and the infrared heat insulating pipe joint reaction vat (56) lower Annular duct (53) connected to pass, while four # pipe joints with the gas stove (107) with the wind pipe (109) connected to pass, while Said outer cylinder (35) has a function of the open end of the signs (39), and the sign of the functional (39) is provided with a, b, c, d four scale line, operation, when the valve handle (38) the pointer (40) is a time scale, 3 # and 4 # two fittings Is closed, and the pipe joint # 2 is turned on, then you can through said inlet means (91) on the inlet pipe (14) to the electric Air igniter (13) into the fresh air, in order to achieve the main furnace (51) non-cleaning automatic ignition; and when said handle means Pin (40) to the scale b, the 2 # and 4 # pipe joint is closed, and the 3 # pipe joint is turned on, then to the intake air by Means (91) on the progress duct (14) and an annular duct (53), to the main furnace (51) infrared adiabatic reaction vat (56) Import or mixed with fresh air from said annular variable-temperature gasification chamber (90) of tar gasification gas mixture, so that the biological Quality in the infrared adiabatic reactor barrel (56), the realization of infrared thermal insulation oxygen combustion and pyrolysis and gasification, while also allowing the Tar gasification gas in the infrared adiabatic reactor barrel (56) Infrared thermal insulation to achieve secondary combustion and catalytic cracking hypoxia; And when the Pointer said handle (40) continues to rotate clockwise, the two fittings are still closed # 3, # pipe joint still conduction state State, while the four # pipe joints but was gradually opened, this time, you can pass with four # fitting connected with the duct (109) to the fuel Gas stove (107) inside the cyclone separator (119) with more and more into the combustion air into the combustion with air at room temperature Cold air, so that when in said cyclone (119) of the gas is mixed with the raw materials, to make the water in the gas mixture Steam and coke gas in the cyclone (119) further condensation inside, making the last to enter the sublimation burner (29) Biomass gas and thus become fully premixed combustion air and water vapor and low tar mixed gas, so that the Sublimation in said burner (29) for infrared successfully complete combustion catalytic cracking regenerator, when the handle pointer (40) C to scale, the two fittings are still closed #, 3 # and 4 # and pipe fittings is at the fully conductive state, this time, blended with Combustion air reaches the maximum; when the handle pointer (40) to d during scaling, 2 #, 3 # and 4 # are all related fittings Closed at this time, the main furnace (51) to stop gas, full device into shutdown state; said gas stove (107) shown in Figure 55 and Shown in Figure 56, an annular plate condenser (110) and said annular plate in the condenser (110) provided on top of heat up Hua burner (29), a condenser of the annular plate (110) has an inner air supply control device portion (116), in the Said annular ring splints condenser (110) of the lower part of the water-sealed oil-water separator (44); said annular plate condenser (110) as shown in Figure 55 and Figure 56, the cross-section is rectangular desk type stand legs (108) and surround the stent legs (108) outside the two annular thickness of less than 1mm thin combination and legs disposed in said holder (108) of the The upper part, is an air-cooled indirect air seal annular inner cylinder, while the annular plate condenser (110) in the wall of A feed pipe (30), the outlet pipe (112) and the guide liquid inlet (104); said sublimation burner (29) shown in Figure 21 and Figure 22, the intake pipe (30), the housing (20), infrared heating the porous ceramic panel (1), particulate infrared heating agent (31) Infrared heating and high temperature alloy wire (32) composed in the intake pipe (30) is provided with an upper port holes (5) Sub-hood (33), while the infrared heat porous ceramic plate (1) equipped with infrared heating agent (31), the particles Shaped infrared heating agent (31) disposed in said porous ceramic infrared heating plate (1), said high-temperature infrared heating alloy wire (32) disposed in said particulate infrared heating agent (31) and infrared heating the porous ceramic panel (1) above, and with maintaining 10 ~ 20mm spacing; said infrared heating the porous ceramic panel (1) is 16 to 17 mesh, each cell (2) size of 1.12 ~ 1.38mm ...², thickness of slab is that 15mm, wall thickness are the thin wall type plane infrared heating porous ceramic plate of 0.4mm; The particle diameter of described graininess infrared heating agent (31) is the 3mm left and right, greater than mesh (2) aperture of described thin wall type infrared heating porous ceramic plate (1); Described air feed regulation device (116) by gas-liquid separator (115), Pneumatic valve (76), revolve a minute separator (119), exhaust-valve (117) combines; Described hydrolock oil water separator (44) is as Figure 41 and shown in Figure 42, formed by hopper (45), feed tube (49), tar delivery line (46) and water delivery line (50), and the liquid outlet of the tar overfall of described tar delivery line (46) and described feed tube (49) all is positioned under the water overflow outlet of described water delivery line (50); Described infrared heating agent (31) is magnesia, aluminium oxide and silica; Described high temperature resistant infrared heating alloy silk screen (32) is that 6 orders, each mesh area are 10.89mm², string diameter is the Aludirome silk screen of 0.8mm.

[embodiment two]

A kind of biomass instant gasification uses device, shown in Figure 64, by main stove (51), gas-cooker (107) and pipeline connecting parts (129) are formed, compare with [embodiment one], described main stove (51) as shown in figure 46, do not establish alternating temperature vaporizer (90) and annular passage (53) in the bottom of described infrared adiabatic reaction bucket (56), the infrared fire-resistant bucket (57) that constitutes described infrared adiabatic reaction bucket (56) is empty cylindrical shell in cylindrical, its inlet duct (91) is by molecule fission promoters (7), blast pipe (14), collection control valve (34) and air blast (92) are formed, described molecule fission promoters (7) as shown in Figure 7 and Figure 8, be pagoda shape eddy flow outgassing nozzle, specifically be arranged on the central axis of the interior bottom of described infrared adiabatic reaction bucket (56), by cylinder (9), central airway (12), the venthole (11) and the pore the brim of a hat (10) are formed, the week that the described pore the brim of a hat (10) is arranged on described cylinder (9) laterally, described venthole (11) is arranged on the below of the described pore the brim of a hat (10), described central airway (12) is arranged on the interior central axis of described cylinder (9), and described venthole (11) communicates with described central airway (12); In addition, on the catheter (83) of described smokeless cleaning charging gas operated device (61), do not establish hydrolock oil water separator (44); Do not establish at the bucket of described infrared adiabatic reaction bucket (56) that to comprise ring vaccum insulation interlayer be the superconducting device of vacuum heat-insulating layer (84) in the wall, the thermal insulating warm-keeping layer (58) that constitutes described infrared adiabatic reaction bucket (56) is the asbestos heat-insulation layer, and is provided with high temperature heat-resistant reflective thermal-insulating dope layer on the interior sidewall surface of barrel (87) in the metal that constitutes described thermal insulating warm-keeping layer (58); Described gas-cooker (107) is controlled a burner jointly by a Pneumatic valve of former usefulness (76) and a gas-liquid separator (115) and is changed present embodiment into and only use burner of shown in Figure 73 and Figure 74 one collection control valve (34) control shown in Figure 75 and Figure 76; The used infrared heating agent of present embodiment is zinc oxide, aluminium oxide and silica in addition; In addition, remainder is all identical with [embodiment one].

[embodiment three]

A kind of biomass instant gasification uses device, shown in Figure 65, by main stove (51), gas-cooker (107) and pipeline connecting parts (129) are formed, compare with [embodiment one], described main stove (51) as shown in figure 47, do not establish annular passage (53) in the bottom of described infrared adiabatic reaction bucket (56), its inlet duct (91) is by blast pipe (14), collection control valve (34), air blast (92) and form as Fig. 9 and molecule shown in Figure 10 fission promoters (7), and described molecule fission promoters (7) is arranged on the central axis of the interior bottom of described infrared adiabatic reaction bucket (56), and the wireway (80) in the described alternating temperature vaporizer (90) is arranged on the upper blast pipe (14) of described inlet duct (91), and communicate with described blast pipe (14), described collection control valve (34) is as Figure 29～shown in Figure 32, wherein the 2# pipe joint is connected with described electric heating air igniter (13), molecule fission promoters (7) in 3# pipe joint and the described infrared adiabatic reaction bucket (56) is connected, the 4# pipe joint is connected with air blast (92), and the 1# pipe joint is connected with described gas-cooker (107) aid distributing pipe (109), and on its function direction board (39), only be provided with a, b, three graduation marks of c, during operation, when its pointer (40) points to a scale, the 3# pipe joint is closed, and 4# and 2# pipe joint are switched on, the lower blast pipe (14) that can pass through this moment on the inlet duct (91) imports fresh air to electric heating air igniter (13), thereby realizes the igniting automatically of the smokeless cleaning of main stove (51); And when described pointer (40) forwards the b scale to, the 2# pipe joint is closed, and 4# and 3# pipe joint are switched on, can import fresh air this moment in stove, thereby make living beings in described infrared adiabatic reaction bucket (56), realize infrared heat storing and heat preserving anoxycausis and pyrolytic gasification, because its 1# pipe joint is the normal open pipe joint, therefore, in being imported into gas-cooker (107) simultaneously, uses by the 1# pipe joint for distribution from the cold air of air blast (92); And when its pointer (40) forwarded the c scale to, 2#, 3#, 4# pipe joint all were closed, and at this moment, main stove (51) stops to make gas, and complete unit enters off-mode; In addition, on described electric heating air igniter (13) upper body, do not establish connected entrance (54) as shown in figure 45, do not establish in described infrared adiabatic reaction bucket (56) that to comprise ring vaccum insulation interlayer be the superconducting device of vacuum heat-insulating layer (84), the thermal insulating warm-keeping layer (58) that constitutes described infrared adiabatic reaction bucket (56) is the asbestos heat-insulation layer, and is provided with high temperature heat-resistant reflective thermal-insulating dope layer on the interior sidewall surface of barrel (87) in the metal that constitutes described thermal insulating warm-keeping layer (58); Described gas-cooker (107) is shown in Figure 57 and Figure 58, the infrared burner that is arranged on described annular clamping plate condenser (110) top is a common infrared ray burner (123), the air feed regulation device (116) that is arranged on described annular clamping plate condenser (110) inside position is only by a left side, right collection control valve (34) and aid distributing pipe (109) are formed, wherein said left side collection control valve (34) is as Figure 36～shown in Figure 38, inner barrel (36) and outer cylinder body (35) socket by end sealing other end opening combine, and the blind end of cylindrical shell (36) is provided with valve handle (38) within it, is provided with positive stop strip (133) and pointer (40) on described valve handle (38) simultaneously; The circular side wall of cylindrical shell (36) is provided with two through holes (37) within it, and one of them is a slotted hole, and another is a circular hole; On its outer cylinder body (35), be provided with 1#, 2#, 3# and 4# pipe joint (28), wherein 1# pipe joint (28) is for being arranged on the normal open pipe joint on described outer cylinder body (35) blind end and linking to each other with Gas Pipe, 2#, 3# and 4# pipe joint are for being arranged on the controlled pipe joint on described outer cylinder body (35) circular side wall, wherein the 2# pipe joint links to each other with aid distributing pipe (109), the 3# pipe joint links to each other with described common infrared ray burner (123), and the 4# pipe joint links to each other with evacuated tube (118); Openend at described outer cylinder body (35) is provided with sealing location end cap (41) simultaneously, and is furnished with function direction board (39), on described function direction board (39), be provided with a, b, three graduation marks of c, described function direction board (39) specifically is arranged on gas-cooker corresponding with it (107) shell, be provided with simultaneously and be convenient to its hard-wired hanger (42), and on hanger (42), be provided with installing hole (43) at the blind end of described outer cylinder body (35); During work, when described pointer (40) is in a scale, 2# and 4# pipe joint are closed, and the 3# pipe joint is switched on, at this moment the combustion gas that enters its common infrared ray burner (123) is not for allocating the pure biological fuel gas of air into, be difficult in the acquisition completing combustion of burner position, this moment is when described valve handle (38) when continuing to move in the direction of the clock, can allocate increasing combustion air into to described combustion gas, when described pointer (40) forwards the b scale to, 2# and 3# pipe joint all are in complete conducting state, and the 4# pipe joint still is in closed condition, and the air capacity that allocate to combustion gas this moment reaches maximum; When described pointer (40) forwarded the c scale to fast by the b scale, 2# and 3# pipe joint all were closed, and the left side burner quits work, and the 4# pipe joint is switched on, and at this moment, can realize the emptying operation by the evacuated tube (118) on the described gas-cooker (107); Described right collection control valve (34) is as Figure 33～shown in Figure 35, compare with aforementioned left side collection control valve (34), remove and on the circular side wall of the outer cylinder body symmetrical (35), have additional the controlled pipe joint of 5# with the 4# pipe joint, and on its function direction board (39), be provided with a, b, c, outside four graduation marks of d, remainder is all identical with the structure of described left side collection control valve (34), during work, when described pointer (40) is in a scale, 4# pipe joint as standby port (124) is closed with the 2# and the 5# pipe joint that are connected with aid distributing pipe (109), and the 3# pipe joint that is connected with common infrared ray burner (123) is switched on the 1# normal open pipe joint that is connected Gas Pipe, the combustion gas that enters its common infrared ray burner (123) this moment is not for allocating the pure biological fuel gas of air into, be difficult in the realization completing combustion of burner position, at this moment when described valve handle (38) when continuing to move in the direction of the clock, can allocate increasing combustion air into to described combustion gas, and when described pointer (40) forwards the b scale to, 2# and 3# pipe joint are by conducting fully, and 4# and 5# pipe joint still are in closed condition, and the air capacity that allocate to combustion gas this moment reaches maximum; When described pointer (40) forwards the c scale to, 2#, 3# and 5# pipe joint all are closed, and the 4# pipe joint is switched on, at this moment pure biological fuel gas that can will not allocate air into imports external equipment and uses, this moment is when described valve handle (38) when continuing to move in the direction of the clock, can allocate increasing combustion air into to the biological fuel gas that imports external equipment, and when described pointer (40) forwarded the d scale to, the air capacity of allocating into to the combustion gas that imports external equipment reached maximum; When described pointer (40) was turned back to the c scale and closes the Pneumatic valve (76) that is located on the standby port (124) by the d scale, right side burner and external equipment all were in off-mode; Described infrared heating agent simultaneously is a carborundum; In addition, remainder is all identical with [embodiment one].

[embodiment four]

A kind of biomass instant gasification uses device, shown in Figure 66, by main stove (51), gas-cooker (107) and pipeline connecting parts (129) are formed, wherein, described main stove (51) as shown in figure 48, bottom at its infrared adiabatic reaction bucket (56), with the electric heating air igniter (13) in air plasma generator (94) replacement [embodiment two], and on described air plasma generator (94), be provided with the cement output tank (95) of with closure (23), described air plasma generator (94) is connected with blast pipe (14) that constitutes described inlet duct (91) and molecule fission promoters (7), described blast pipe (14) is for being located at the single channel blast pipe outside the stove, and the control valve that links to each other with air blast (92) is common Pneumatic valve (76), be provided with igniting ash hole (55) in the bottom of described infrared adiabatic reaction bucket (a 56) side simultaneously, be provided with insulation plug formula insulation cover (96) in described igniting ash hole (55), the gas permeable devices that is arranged on simultaneously on its sealing bell (77) is made up of pipe joint formula permeability cell (75) and Pneumatic valve (76); Described gas-cooker (107) is shown in Figure 61 and Figure 62, compare with [embodiment two], its air feed regulation device (116) is establishing airduct (109) not, gas-liquid separator (115) by two band catheters (83), two common Pneumatic valves (76), one cover cyclone separator (119) and the exhaust-valve (117) and the evacuated tube (118) that are arranged on the annular clamping plate condenser (110) are formed, and replace heat sublimation burner (29) in [embodiment two] with the common burner (127) of band infrared energy-conserving cover (6) in the top of its annular clamping plate condenser (110), in addition, used infrared heating agent (31) is a silicon nitride; In addition, remainder is all identical with [embodiment two].

Specify:

1, can realize that specific embodiments of the present utility model is except that the four kinds of embodiment of the above, also just like Figure 67, Figure 68, Figure 69, Figure 70, multiple specific embodiments shown in Figure 71 and Figure 72, and for the those of ordinary skill in this professional skill field, need not other annex word explanation, only need browse relevant drawings can come into plain view to various specific embodiments shown in the drawings, wherein, constitute as Figure 67, Figure 68, Figure 69, Figure 70, the internal structure of " main stove " is respectively as Figure 49 shown in Figure 71 and Figure 72, Figure 50, Figure 51, Figure 52, shown in Figure 53 and Figure 54; Formation internal structure of " gas-cooker " shown in Figure 67, Figure 68, Figure 69, Figure 70 and Figure 71 is shown in Figure 57 and Figure 58, and the internal structure that constitutes " gas-cooker " shown in Figure 72 is shown in Figure 59 and Figure 60.

2, the above only is a part specific embodiments of the present utility model; but realize that the utility model also has other multiple specific embodiments; and all be conspicuous for the those of ordinary skill of this professional range; just as space is limited; this specification is not all enumerated, therefore, and every various specific embodiments without prejudice to the utility model general plotting; comprise other various deformation programs or be equal to alternative, be effective protection scheme of the present utility model.

Claims (10)

1, a kind of biomass instant gasification uses device, form by main stove (51), gas-cooker (107) and pipeline connecting parts (129), it is characterized in that: described main stove (51) comprises upper and lower two parts, top is smokeless cleaning charging gas operated device (61), the bottom is an infrared adiabatic reaction bucket (56), and is provided with the igniting feeder in the bottom of described infrared adiabatic reaction bucket (56); Described gas-cooker (107) is provided with annular clamping plate condenser (110), and be provided with infrared burner in the top or the outside of described annular clamping plate condenser (110), be provided with air feed regulation device (116) in the inside position of described annular clamping plate condenser (110), be provided with hydrolock oil water separator (44) or liquid seal trough or U type liquid sealing pipe in the bottom of described annular clamping plate condenser (110).

2, biomass instant gasification according to claim 1 uses device, it is characterized in that: described igniting feeder is combined with inlet duct (91) with inlet duct (91) or igniting ash hole (55) with inlet duct (91) or air plasma generator (94) with inlet duct (91) or electric heating air igniter (13) by electric heating air igniter (13), alternating temperature vaporizer (90); Described electric heating air igniter (13) is made up of blast pipe (14) and electric calorifie installation (15) two parts, described blast pipe (14) communicates with described electric calorifie installation (15), and wherein said electric calorifie installation (15) is made up of air preheating chamber (16), infrared excitation chamber (17) and the infrared electric heating body (27) that is arranged in this infrared excitation chamber (17) again; Described infrared electric heating body (27) is the combination of infrared heating porous electric furnace pan (3), infrared heating porous ceramic plate (1) and high temperature resistant heating or heat-resisting alloy pipe, electrician's level magnesia and high temperature resistant heating or carborundum and high temperature resistant heating or silicon nitride and high temperature resistant heating, and described high temperature resistant heating is common electric furnace heating wire, common electrical heated filament, high-temperature electric resistance furnace silk, high-temperature electric heat silk or tungsten filament.

3, biomass instant gasification according to claim 1 uses device, it is characterized in that: described infrared adiabatic reaction bucket (56) is by infrared fire-resistant bucket (57) and be arranged on its outside thermal insulating warm-keeping layer (58) all around and form; Described infrared fire-resistant bucket for common metal bucket, heat-resisting alloy bucket and in establish the composite wood charging basket of infrared heating material or their combination; Described thermal insulating warm-keeping layer (58) is a kind of in thermal current heat-insulation layer (100), vacuum heat-insulating layer (84), the inserts heat-insulation layer (85) or points to a kind of high temperature resistant infrared composite heat-insulating layer that combines in the heat-reflecting layer of reaction container central axis and thermal current heat-insulation layer (100), vacuum heat-insulating layer (84), the inserts heat-insulation layer (85) by reflection direction.

4, biomass instant gasification according to claim 1 uses device, it is characterized in that: described smokeless cleaning charging gas operated device (61) is made up of the material storage barrel (81) of upper and lower opening and the sealing bell (77) that is arranged on this material storage barrel (81) upper port, and described material storage barrel (81) be provided with " squirrel-cage " annular condensation liquefaction diffluence room (60) and annular air channel (59) week laterally, and described annular condensation liquefaction diffluence room (60) communicates with described infrared adiabatic reaction bucket (56) by described annular air channel (59); Described material storage barrel (81) is material envelope formula material storage barrel or the sealed material storage barrel of gas material, wherein, described material envelope formula material storage barrel is that empty cylindrical shell or top are that cylindrical lower portion is an empty cylindrical shell in the combined type of truncated inverted cone shape in empty cylindrical shell in upper and lower opening cylindrical, the truncated inverted cone shape; The sealed material storage barrel of described gas material is made up of described material envelope formula material storage barrel and the truncated inverted cone shape feed hopper (98) that is arranged in the described material envelope formula material storage barrel, and is provided with inlet duct (91) on the annular passage (53) that is made of described feed hopper (98) and described material envelope formula material storage barrel bucket wall; Described sealing bell (77) is for the usual pressure sealing bell of making encapsulant with sealing gasket or sealing ring or make the traditional gravity sealing bell of encapsulant or band water vapor condensate with water, high-hydroscopicity resin, adhesive sticker mud, noninflammability powder, noninflammability liquid and divide the multifunctional gravity sealing bell of the multi-functional pressure sealing bell that flow device or band air-pressure balancing device or be provided with the multifunctional gravity that water vapor condensate divides stream device and air-pressure balancing device simultaneously and seal bell; Described water vapor condensate divides the stream device, combine by the distributing damper (82) and the bell shell that are arranged in the described sealing bell (77), and in the annular intake chute that described distributing damper (82) and bell shell are constituted, be provided with fluid guidance port (104), and on described distributing damper (82), be provided with at least one ventilation mouth (102); Described air-pressure balancing device is for being arranged on the gas permeable devices on the described sealing bell (77), be made up of control piece and ventilation mouth (102), described control piece is a sealing-plug (101) or by the combination of permeability cell (75) and Pneumatic valve (76), spring valve or seal cover.

5, biomass instant gasification according to claim 1 uses device, it is characterized in that: described annular clamping plate condenser (110) is rectangle desk formula four foot supports (108) by cross section and is looped around two inside and outside thickness of four foot supports (108) and combines at the annular sheet that is optimized for below the 3mm below the 1mm, and place the middle and upper part of described four foot supports (108), be empty sealed cylinder in the indirect cooled annular of an air, on the wall of described annular clamping plate condenser (110), be provided with air inlet pipe (30) simultaneously, escape pipe (112) and fluid guidance port (104); Described annular clamping plate condenser (110) also can be triangle, square, circle, oval-shaped single pin, both feet or multiway support (108) or their combination and be looped around the inside and outside and thickness of set support (108) and combine at the annular sheet that is optimized for below the 3mm below the 1mm by cross section.

6, biomass instant gasification according to claim 1 uses device, it is characterized in that: described infrared burner is the common burner (127) of heat sublimation burner (29), common infrared ray burner (123) or band infrared energy-conserving cover (6), and described infrared energy-conserving cover (6) is empty cylindrical shell in the columniform infrared thermal insulation for the sphere of upper and lower opening, hemispherical, variant sphere, conical butt or top for the conical butt bottom; Described heat sublimation burner (29) is made up of air inlet pipe (30), housing (20), infrared heating porous ceramic plate (1) and infrared heating alloy silk screen, and described infrared heating alloy silk screen is arranged on the surface of described infrared heating porous ceramic plate (1); Described infrared heating porous ceramic plate (1) is that preferred 16～17 orders of 15～18 orders, each mesh (2) area are 0.78～1.89mm ²Preferred 1.12～1.38mm ², thickness of slab is that the preferred 12～15mm of 10～20mm, wall thickness are the support type infrared heating porous ceramic plate that thin wall type plane infrared heating porous ceramic plate, corrugated surface infrared heating porous ceramic plate or the surface applied of the preferred 0.4mm of 0.3～0.5mm has combustion catalyst.

7, biomass instant gasification according to claim 1 uses device, it is characterized in that: described air feed regulation device (116) is a gas-liquid separator (115), revolve branch separator (119), aid distributing pipe (109), escape pipe (112), evacuated tube (118) and control valve or aid distributing pipe (109), escape pipe (112), evacuated tube (118) and control valve or air blast (92), aid distributing pipe (109), escape pipe (112), evacuated tube (118) and control valve or gas-liquid separator (115), revolve branch separator (119), escape pipe (112), evacuated tube (118) and control valve or aid distributing pipe (109), escape pipe (112), evacuated tube (118), the combination of the combination of distribution bucket and control valve or above various assembly and tempering warning device or tempering warning self-con-tained unit; Described distribution bucket is one to be provided with the interior empty of fuel gas inlet, air intlet, condensate outlet and mixed gas outlet; Described control valve is Pneumatic valve (76), exhaust-valve (117), collection control valve (34), regular tap valve or magnetic valve.

8, biomass instant gasification according to claim 1 uses device, it is characterized in that: described hydrolock oil water separator (44) is made up of hopper (45), feed tube (49), tar delivery line (46) and water delivery line (50), and the liquid outlet of the tar overfall of described tar delivery line (46) and described feed tube (49) all is positioned under the water overflow outlet of described water delivery line (50).

9, use device according to claim 2 or 4 described biomass instant gasifications, it is characterized in that: described inlet duct (91) is the combination of annular passage (53), blast pipe (14), air blast (92) and control valve or molecule fission promoters (7), blast pipe (14), air blast (92) and control valve or blast pipe (14), air blast (92) and control valve, and communicates with described alternating temperature vaporizer (90), electric heating air igniter (13), air plasma generator (94) or material storage barrel (81); Described control valve is Pneumatic valve (76), collection control valve (34), regular tap valve or magnetic valve; Described molecule fission promoters (7) is made up of cylinder (2), central airway (5), venthole (4) and the pore the brim of a hat (3), described central airway (5) is arranged on the interior central axis of described cylinder (2), be cylindrical air guide channel, simultaneously be provided with at least one group of pore the brim of a hat (3) laterally in the week of described cylinder (2), and cylinder (2) upper edge under every group of pore the brim of a hat (3) circumferentially is laid with at least 2 ventholes, and described venthole (4) is downwards or level rotary flow venthole, a kind of downwards or in the horizonally projected jet venthole.

10, use device according to claim 7 or 9 described biomass instant gasifications, it is characterized in that: described collection control valve (34) is by the cylindrical interior empty cylindrical shell of inside and outside two one ends sealing other end opening, be that inner barrel (36) and outer cylinder body (35) socket combine, and be provided with valve handle (38) at the blind end of described inner barrel (36), on the circular side wall of described inner barrel (36), be provided with at least one through hole (37), on described valve handle (38), be provided with or the binomial that is selected from pointer (40) and the positive stop strip (133) simultaneously; On described outer cylinder body (35), be provided with at least two pipe joints (28), wherein be arranged on described outer cylinder body (35) blind end and not with inner barrel (36) lap on pipe joint be the normal open pipe joint, the pipe joint that is arranged on the remainder is controlled pipe joint, and the openend at described outer cylinder body (35) is provided with or the binomial that is selected from sealing location end cap (41) and the function direction board (39) simultaneously.

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