CN203108239U - Steam colliding material decomposition and combustion circulating device - Google Patents
Steam colliding material decomposition and combustion circulating device Download PDFInfo
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- CN203108239U CN203108239U CN2013201426623U CN201320142662U CN203108239U CN 203108239 U CN203108239 U CN 203108239U CN 2013201426623 U CN2013201426623 U CN 2013201426623U CN 201320142662 U CN201320142662 U CN 201320142662U CN 203108239 U CN203108239 U CN 203108239U
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- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
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- Y02A20/124—Water desalination
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- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
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Abstract
The utility model discloses a steam colliding material decomposition and combustion circulating device, mainly consisting of a first liquid charging tank, a second liquid charging tank, a first solid charging tank, a second solid charging tank, a hot water exchange tank, a high-pressure plunger pump, a dry steam generator, a high-pressure spraying device, a material steam decomposition coil pipe, a spray explosion cooling reduction room, a constant temperature furnace, a circulating pump, a fuel charging tank, a high-position expansion tank, a low-position oil storage tank, a steam header, a steam turbine and a generator. The steam colliding material decomposition and combustion circulating device has the advantages that the device overcomes the defects of the traditional boiler, and breaks through the limit that steam temperature is obtained through pressure; and the device solves the traditional process production, applies steam to heat energy supply and power generation, can be used for sea water desalination, sewage and garbage disposal, high speed material decomposition, concentration, extract, drying, product deep processing, 800-DEG C high temperature furnace body reheat steam cracking oxyhydrogen circulation combustion and material reheat steam combustion, and is a multi-purpose, efficient, energy-saving and emission-reduction and environment-friendly device.
Description
Technical field
The utility model relates to a kind of dry type steam generator.It specifically is a kind of steam head-on collision substance decomposition burn cycle device.
Background technology
Tradition concentrates drying plant complex process multistage, machines cumbersome, and the cost of investment height, power consumption is high.The serious development that restricts fields such as industrial crystallization bodies such as China's food, desalinization, pharmacy, sugaring, papermaking, alcohol, chemical industry, rubbish, sewage, mineral products concentrate, extraction, decomposition, drying.The utility model is that circulation electric generating apparatus, multipurpose spraying-exploding type high pressure temperature adjustment gas decomposition dry type steam generator improve upgrading in original solar oil heat conducting and supplying device, heat radiation.After the steam that produces in the dry type steam generator and various material clash in material steam decomposes coil pipe, be gas with the water transform in the material, enter the quick-fried reduction of spray chamber, aloft the distance of Piao Fuing is different with the position than resedimentation, the difference as a result that it obtains can be decomposed any material, and water become after the steam cooling reduction distance farthest, reductive water is capable of circulation to be recycled continuously to the hot water storage tank, plays the effect of high-efficiency water-saving, energy-conservation, environmental protection and high-temperature sterilization.Its advantage is that the composition according to different material can adopt different temperature to regulate separation.The material decomposition rate is fast, and steam is warming up to the above directly cracking oxyhydrogen combustion of 800 degree by furnace body metal coil pipe post bake, simultaneously other combustibles is clashed to be transported in the furnace body by steam and burns with the source kindling material.Device simple, cost of investment is low, has only the real efficient energy-saving and emission-reducing of thermal efficiency ability that improves pot (generator).
The utility model content
The purpose of this utility model provides a kind of pattern novelty, simple structure, energy-efficient, thermal conversion efficiency is high, the generator heat exchange area all takes full advantage of, moment produces high-temperature high-pressure overheat steam, environmental protection steam head-on collision substance decomposition burn cycle device.
The technical scheme that the utility model solves the problems of the technologies described above is:
1. steam head-on collision substance decomposition burn cycle device is characterized in that: it mainly decomposes coil pipe, spray by the first liquid head tank, the second liquid head tank, the first feeding-in solid body jar, the second feeding-in solid body jar, hot water swap tank, high-pressure plunger pump, dry type steam generator, high pressure sprays fog equipment, material steam and produces an unexpected winner and but reduce chamber, constant temperature oven, circulating pump, fuel-feed jar, high-order expansion slot, low level oil storage tank, gas-distributing cylinder, steam turbine and generator and form;
1) structure of each parts is as follows:
1.1) the described first liquid head tank and the second liquid head tank be the slack tank body, the liquid material that interior splendid attire need decompose;
1.2) the described first feeding-in solid body jar and the second feeding-in solid body jar be the slack tank body, the solid particle material that interior splendid attire need decompose;
1.3) described hot water swap tank is the slack tank body, interior splendid attire water;
1.4) described fuel-feed jar is the slack tank body, interior contain fuel;
1.5) described high-order expansion slot is the slack tank body, the conduction oil after interior splendid attire expands;
1.6) described low level oil storage tank is the slack tank body, interior splendid attire conduction oil;
1.7) described constant temperature oven is the body of heater of heated at constant temperature, body of heater has heat-insulation layer outward, and interior is heating clamber, is provided with heat conduction coil pipe, material steam combustion tube and the high temperature steam metal coil pipe of band conduction oil import and export pipe in the heating clamber;
1.8) described spray produces an unexpected winner and but reduce the chamber front end and be equipped with and regulate replenish that blower fan, inside are equipped with the diffusion barrier net, the below is equipped with recovery pond, has cooling sandwith layer, tail end that waste heat cooling water pipe and condensed water filtering ponds are installed outward;
1.9) described dry type steam generator is for there being the multilayer annular seal circuit of heat-insulation layer outward, it is respectively the first heat conduction oil reservoir, the second heat conduction oil reservoir, the 3rd heat conduction oil reservoir, the 4th heat conduction oil reservoir, the 5th heat conduction oil reservoir, the 6th heat conduction oil reservoir, the 7th heat conduction oil reservoir and the 8th heat conduction oil reservoir, first vapor film, second vapor film, the 3rd vapor film, the 4th vapor film, the 5th vapor film, the 6th vapor film and the 7th vapor film, first vapor film and second vapor film, second vapor film and the 3rd vapor film, the 3rd vapor film and the 4th vapor film, the 5th vapor film and the 6th vapor film, the 6th vapor film and the 7th vapor film are respectively equipped with communicating pipe, the first heat conduction oil reservoir and the second heat conduction oil reservoir, the second heat conduction oil reservoir and the 3rd heat conduction oil reservoir, the 3rd heat conduction oil reservoir and the 4th heat conduction oil reservoir, the 4th heat conduction oil reservoir and the 5th heat conduction oil reservoir, the 5th heat conduction oil reservoir and the 6th heat conduction oil reservoir, the 6th heat conduction oil reservoir and the 7th heat conduction oil reservoir, the 7th heat conduction oil reservoir and the 8th heat conduction oil reservoir are respectively equipped with communicating pipe;
2) connected mode of described each parts of described a kind of steam head-on collision substance decomposition burn cycle device is as follows:
The outlet of hot water swap tank is connected with the import of high-pressure plunger pump by pipeline;
Import with first vapor film of dry type steam generator is connected the high-pressure plunger delivery side of pump with high pressure sprays fog equipment by high-pressure plunger pump pipe outlet pipe;
The 7th vapor film outlet of dry type steam generator is connected with the import of gas-distributing cylinder by the vapor film outlet conduit;
Three outlets of gas-distributing cylinder are connected with the import of material steam decomposition coil pipe, material steam combustion tube, high temperature steam metal coil pipe and steam turbine respectively by pipeline; The second feeding-in solid body jar and the second liquid head tank are installed decomposing on the pipeline that coil pipe is connected with material steam respectively; With pipeline that the material steam combustion tube is connected on the first feeding-in solid body jar and the first liquid head tank are installed respectively; At the pipeline that is connected with high temperature steam metal coil pipe the fuel-feed jar is installed;
The outlet that material steam decomposes coil pipe is but reduced the import of chamber and is connected with spraying to produce an unexpected winner;
Spray produces an unexpected winner and but reduces the import and export pipe of cooling sandwith layer of chamber and be connected with the going out of cooling water circulating line, inlet tube respectively, and recovery pond is housed below cooling sandwith layer; Spray produces an unexpected winner and but reduces the outlet of chamber interior by the waste heat cooling water pipe and be connected with the import of hot water swap tank, in connecting pipe the cooling water filtering ponds is housed;
The outlet of the heat conduction coil pipe of constant temperature oven is connected with the import of the first heat conduction oil reservoir of vapour generator and the import of low level oil storage tank respectively by the heat conductive oil inlet pipeline; The heat conduction coil pipe import of constant temperature oven is connected with outlet of circulating pump by the conduction oil outlet conduit; Outlet of circulating pump is connected with the 8th heat conduction oil reservoir outlet of dry type steam generator; The outlet of high-order expansion slot is connected with the import of low level oil storage tank.
Above-mentioned steam head-on collision substance decomposition burn cycle device, it act as atomizing heated moisture body described dry type steam generator, is 1-1000 dry type steam generator assembly in parallel.
Above-mentioned steam head-on collision substance decomposition burn cycle device, described constant temperature oven is 1-100 constant temperature oven assembly in parallel.
Advantage of the present utility model:
1. steam head-on collision substance decomposition burn cycle device, power consumption are half of conventional boiler, reduce production costs greatly, shorten the technological process of production.
2. break through the pattern of steaming that century-old boiler water boils bubble type that goes up, produce steam by heating the wet steam body and need not high temperature, the generator heat exchange area all takes full advantage of, and injects liquid material cold water, and moment produces the high pressure-temperature superheated steam.
3. the thermal conversion efficiency of dry type steam generator is up to more than 95%, the jet chimney of dry type steam generator steam flow speed processed reaches per hour more than 110 kilometers, also can be in conjunction with various energy resources and the complementary heating of solar energy conduction oil, energy-conservation more remarkable, reduce production costs greatly, zero-emission, environmental protection.
4. vapor (steam) temperature need not painstakingly to realize that by pressure steam pressure and temperature can be regulated arbitrarily, realizes the high speed substance decomposition.
5. the platform number of dry type steam generator can be expanded increase-volume at any time, has solved the unnecessary wasting of resources of enterprise's enlarged reproduction.
6. solve the conventional boiler defective, realize no condensed water, no incrustation scale, no blowdown in the dry type steam generator, reduce artificial treatment incrustation scale and charges for disposing pollutants and use.
7. by moisture content, drying, expanded in the high-temperature steam head-on collision substance decomposition material, its speed of action is fast, hot mechanical efficiency height.
8. use high-temperature steam head-on collision sewage, mud, fowl and animal excrement decomposition concentrate or pulvis to obtain spraying the material of quick-fried reduction chamber, be allocated as the high nutritious fertilizer of liquid of crops by the secondary deep processing.
9. use high-temperature steam head-on collision rubbish, after the autoclave sterilization drying, be allocated as the senior organic fertilizer of various crops by the secondary deep processing.
10. use high-temperature steam head-on collision vegetables, fruit, but deep processing is pulvis, liquid beverage, solid food, prolongs the food consumption phase.
11. use the high-temperature steam various materials that clash, as medicine, chemical industry, seawater, sugaring, starch, dairy products, food etc., can concentrate, drying, separation, dehydration, crystallization, play energy-saving and environment friendly, ringing.
12. use high-temperature steam head-on collision fine coal and other combustible, can heat up to be delivered in the furnace body by indirect steam and burn with the source kindling material.
13. steam can be cracked into the endogenous kindling material of hydrogen-oxygen and stove and burn together by more than the secondary temperature elevation to 800 ℃.
14. use high-temperature steam head-on collision rubbish, mud, fowl and animal excrement, organic concentrate (as the sewage of alcohol effluent, papermaking wastewater, starch industry etc.), living beings, to furnace body, directly burn with the source kindling material, but the material deep processing after the burning becomes organic fertilizer.
15. be used in the industrial of required high-temperature low-pressure steam, safer.
16. steam may be used on cryogenic high pressure for steam launch, steam-driven motor and cogeneration of heat and power use.
17. can accomplish generator fixed fire producing steam at any time in using this device procedures, the conduction oil in heat carrier furnace and the generator plays the accumulation of energy effect when not steaming, conduction oil specific heat plays the adjusting temperature action during Datong District, also plays a role in energy conservation.
The utility model is mainly studied the thermal efficiency of pot and the dry spraying-exploding type steam generator of stove and the steam substance decomposition that directly clashes.This product safety is reliable, and the life-span is long, and device simple is easy to maintenance, and cost of investment is low.How the whole world all improves the thermal efficiency and material, the ultra-supercritical boiler etc. of body of heater always in research, all pot and stove are come together to talk the thermal efficiency, but ignored separately the research of pot (dry type steam generator), the principle that the utility model utilizes material to be present in intermolecular a kind of attraction is studied.Material for composition and structural similarity, it is to the boiling point of water, fusing point, heat of gasification, melting heat, solubility, surface tension, physicochemical properties such as viscosity have decisive, generally strengthen along with the increase of relative molecular mass, so improve a pot thermal efficiency, will Bian with mechanical pump pressure liquid water being become steam fog heats and realizes that producing steam uses, adopt heat carrier furnace and dry atomizing generator, the fast specific heat of conduction oil intensification thermal velocity is big, when not steaming, conduction oil can play energy storage and regulate characteristics such as temperature action, getting around the poach bubble type steams, at kiss and the point by the timing pressure size of generator and thermal power and the continuous post water spray of mechanical pump pressure amount, the thermal-radiating distance of structure in the generator, the kiss of heat exchange area and tube side and timing points, for this reason singly in pot we just can to improve the thermal efficiency over half, for in the future steam boiler can save can Minus row over half, can with traditional poach bubble type pot contrast.Dry atomizing generator can produce the low-voltage high-temperature superheated steam, also but high pressure-temperature docks use with solar oil heat conducting and supplying device.Use the work done in tube side of high-temperature steam head-on collision material, steam and material be timing kiss and the decomposed substance of proportional quantity at the volley.High temperature steam metal coil pipe and furnace body fire box temperature, to kiss and the point of the temperature speed of indirect steam intensification cracking oxyhydrogen combustion and material head-on collision burning, reach with the source kindling material combustion purpose, form a whole set of recycling device, the conversion gas thermal efficiency speed that has really improved pot (dry type steam generator) realizes energy-saving and emission-reduction.
Description of drawings
Fig. 1 is the utility model steam head-on collision substance decomposition burn cycle apparatus structure schematic diagram.
Among the figure: constant temperature oven 1, chimney 2, waste heat coil pipe 3, air-introduced machine 4, dry type steam generator 5, high pressure sprays fog equipment 6, hot water swap tank 7, high-pressure plunger pump 8, low level oil storage tank 9, high-order expansion slot 10, circulating pump 11, gas-distributing cylinder 12, jet chimney 13, steam turbine 14, generator 15, fuel-feed jar 16, high temperature steam metal coil pipe 17, material steam combustion tube 18, feeding-in solid body jar 38, liquid head tank 39, feeding-in solid body jar 40, liquid head tank 41, material steam decomposes coil pipe 42, spray produces an unexpected winner and but reduces chamber 43, regulate and replenish blower fan 44, cooling sandwith layer 45, diffusion barrier net 46, recovery pond 47, waste heat cooling water pipe 48, condensed water filtering ponds 49, cooling water circulating line 50, circulating pump 51.
Fig. 2 is the utility model dry type steam generator A end structure schematic diagram.
Fig. 3 is the utility model dry type steam generator B end structure schematic diagram.
Among the figure: heat conduction oil reservoir 19,21,23,25,27,29,31,33, vapor film 20,22,24,26,28,30,32, high pressure injection plug delivery side of pump pipeline 34, heat conductive oil inlet pipeline 35, conduction oil outlet conduit 36, vapor film outlet conduit 37.
The specific embodiment
Steaming in dry type steam generator of the present utility model inherence does not have condensed water in the fluid motion, no incrustation scale, the dry type steam generator can coincide in generator for the sprayer unit spraying by the electric-controlled mechanical pump pressure, belonging to dry spraying-exploding type steams, in the breakthrough the big water gaging of century-old one-time heating repeat the acting and the poach bubble type steam, steam pressure and the temperature high-temperature low-pressure producing steam that is not directly proportional, but also HTHP producing steam, also can utilize the complementary heating of various energy resources and solar energy conduction oil, thermal energy transfer is arrived the dry type steam generator, the wet gas current that is atomized in the heat drying formula steam generator, make the heat content in the whole moments generation of the water expansion absorption front end conduction oil, conduction oil operating temperature 100 to 320 degree are adjustable, vapor (steam) temperature can be controlled in 80 to 300, the high pressure that reaches a high temperature conversion steam, the thermal conversion efficiency of dry type steam generator is up to more than 95%, the generator pipeline holds B end steam flow speed processed per hour to reach more than 110 kilometers from A, and the utility model can be applicable to modern national defense, space flight, industry, generating, steam catapult in the field, use on the equipment such as steam-driven motor.Realize critical effect, have only in the dry type steam generator thermal efficiency of raising vapour speed processed really to play a role in energy conservation.Use high-temperature steam head-on collision solid particulate matter, liquid substance does work in tube side, make the moisture in the material convert the quick-fried reduction chamber of arriving of gas spray rapidly to by high steam, gas and material are decomposed in the process of sedimentation, the ratio of material is great, the little distance that it flies of specific gravity of gas, high-temperature steam head-on collision solid matter penetration capacity is strong, play dry swelling and watering effect, liquid substance plays and decomposes particle powdery inspissation, be converted into distilled water after the gas cooled reduction, be recycled to sedimentation and filtration ditch, recycle with hot water exchanger water again.Post bake steam metal coil pipe cleavable oxyhydrogen combustion in the furnace body simultaneously with other combustibles, is transported in the furnace body by the steam head-on collision and burns with the source kindling material, plays the effect of air blast air inducing, forms the equipment of a whole set of reproducible utilization resource.
Below in conjunction with accompanying drawing and concrete enforcement the utility model is further described.
Steam head-on collision substance decomposition burn cycle apparatus structure as shown in Figure 1, steam head-on collision substance decomposition burn cycle device, it mainly decomposes coil pipe 42, spray by the first liquid head tank 39, the second liquid head tank 41, the first feeding-in solid body jar 38, the second feeding-in solid body jar 40, hot water swap tank 7, high-pressure plunger pump 8, dry type steam generator 5, high pressure sprays fog equipment 6, material steam and produces an unexpected winner and but reduce chamber 43, constant temperature oven 1, circulating pump 11, fuel-feed jar 16, high-order expansion slot 10, low level oil storage tank 9, gas-distributing cylinder 12, steam turbine 14 and generator 15 and form;
1) structure of each parts is as follows:
1.1) the described first liquid head tank and the second liquid head tank be the slack tank body, the liquid material that interior splendid attire need decompose;
1.2) the described first feeding-in solid body jar and the second feeding-in solid body jar be the slack tank body, the solid particle material that interior splendid attire need decompose;
1.3) described hot water swap tank 7 is the slack tank body, interior splendid attire water;
1.4) described fuel-feed jar 16 is the slack tank body, interior contain fuel;
1.5) described high-order expansion slot 10 is the slack tank body, the conduction oil after interior splendid attire expands;
1.6) described low level oil storage tank 9 is the slack tank body, interior splendid attire conduction oil;
1.7) described constant temperature oven 1 is the body of heater of heated at constant temperature, body of heater has heat-insulation layer outward, and interior is heating clamber, is provided with heat conduction coil pipe, material steam combustion tube 18 and the high temperature steam metal coil pipe 17 of band conduction oil import and export pipe in the heating clamber;
1.8) described spray produces an unexpected winner and but reduce chamber 43 front ends and be equipped with and regulate replenish that blower fan 44, inside are equipped with diffusion barrier net 46, the below is equipped with recovery pond 47, has cooling sandwith layer 45, tail end that waste heat cooling water pipe 48 and condensed water filtering ponds 49 are installed outward;
1.9) described dry type steam generator 5 is for there being the multilayer annular seal circuit of heat-insulation layer outward, it is respectively the first heat conduction oil reservoir 19, the second heat conduction oil reservoir 21, the 3rd heat conduction oil reservoir 23, the 4th heat conduction oil reservoir 25, the 5th heat conduction oil reservoir 27, the 6th heat conduction oil reservoir 29, the 7th heat conduction oil reservoir 31 and the 8th heat conduction oil reservoir 33, first vapor film 20, second vapor film 22, the 3rd vapor film 24, the 4th vapor film 26, the 5th vapor film 28, the 6th vapor film 30 and the 7th vapor film 32, first vapor film 20 and second vapor film 22, second vapor film 22 and the 3rd vapor film 24, the 3rd vapor film 24 and the 4th vapor film 26, the 5th vapor film 28 and the 6th vapor film 30, the 6th vapor film 30 and the 7th vapor film 32 are respectively equipped with communicating pipe, the first heat conduction oil reservoir 19 and the second heat conduction oil reservoir 21, the second heat conduction oil reservoir 21 and the 3rd heat conduction oil reservoir 23, the 3rd heat conduction oil reservoir 23 and the 4th heat conduction oil reservoir 25, the 4th heat conduction oil reservoir 25 and the 5th heat conduction oil reservoir 27, the 5th heat conduction oil reservoir 27 and the 6th heat conduction oil reservoir 29, the 6th heat conduction oil reservoir 29 and the 7th heat conduction oil reservoir 31, the 7th heat conduction oil reservoir 31 and the 8th heat conduction oil reservoir 33 are respectively equipped with communicating pipe;
2) connected mode of described each parts of described a kind of steam head-on collision substance decomposition burn cycle device is as follows:
The outlet of hot water swap tank 7 is connected by the import of pipeline with high-pressure plunger pump 8;
Import with first vapor film 20 of dry type steam generator 5 is connected with high pressure sprays fog equipment 6 by high-pressure plunger pump pipe outlet pipe 34 in the outlet of high-pressure plunger pump 8;
The 7th vapor film 32 outlets of dry type steam generator 5 are connected with the import of gas-distributing cylinder 12 by vapor film outlet conduit 37;
Three outlets of gas-distributing cylinder 12 are connected with the import of material steam decomposition coil pipe 42, material steam combustion tube 18, high temperature steam metal coil pipe 17 and steam turbine 14 respectively by pipeline; The second feeding-in solid body jar 40 and the second liquid head tank 41 are installed decomposing on the pipeline that coil pipe 42 is connected with material steam respectively; With pipeline that material steam combustion tube 18 is connected on the first feeding-in solid body jar 38 and the first liquid head tank 39 are installed respectively; At the pipeline that is connected with high temperature steam metal coil pipe 17 fuel-feed jar 16 is installed;
The outlet that material steam decomposes coil pipe 42 is but reduced the import of chamber 43 and is connected with spraying to produce an unexpected winner;
Spray produces an unexpected winner and but reduces the import and export pipe of cooling sandwith layer 45 of chamber 43 and be connected with the going out of cooling water circulating line 50, inlet tube respectively, and recovery pond 47 is housed below cooling sandwith layer 45; Spray produces an unexpected winner and but reduces the inner outlets by waste heat cooling water pipe 48 in chamber 43 and be connected with the import of hot water swap tank 7, in connecting pipe cooling water filtering ponds 49 is housed;
The outlet of the heat conduction coil pipe of constant temperature oven 1 is connected with the import of the first heat conduction oil reservoir 19 of vapour generator and the import of low level oil storage tank 9 respectively by heat conductive oil inlet pipeline 35; The heat conduction coil pipe import of constant temperature oven 1 is connected with the import of circulating pump 11 by conduction oil outlet conduit 36; The outlet of circulating pump 11 is connected with the 8th heat conduction oil reservoir 33 imports of dry type steam generator 5; The outlet of high-order expansion slot 10 is connected with 9 imports of low level oil storage tank.
Above-mentioned steam head-on collision substance decomposition burn cycle device, it act as atomizing heated moisture body described dry type steam generator 5, is 1-1000 dry type steam generator parallel connection assembly.
Above-mentioned steam head-on collision substance decomposition burn cycle device, described constant temperature oven 1 is 1-100 constant temperature oven assembly in parallel.
When implementing the utility model: conduction oil is injected in the heat conduction oil reservoir of the heat conduction coil pipe of constant temperature oven 1 and dry type steam generator 5, constant temperature oven 1 uses fuel (as coal dust, fuel oil, combustion gas, living beings etc.) the burning heating is as the kindling material in the burner hearth, ON cycle pump 11, conduction oil is circulated in the heat conduction oil reservoir of the heat conduction coil pipe of constant temperature oven 1 and dry type steam generator 5, constant temperature oven 1 arrives operating temperature with heat-conducting oil heating, make each layer heat conduction oil reservoir of dry type steam generator 5 be heated to operating temperature, each layer heat conduction oil reservoir of dry type steam generator 5 conducts heat heat to each layer vapor film of dry type steam generator 5; After the flue gas of discharging during constant temperature oven 1 burning enters chimney 4, when the waste heat coil pipe 3 in superheated water swap tank 7, the water in the hot water swap tank is heated; After water in the hot water swap tank 7 are made water fogging by high-pressure plunger pump 8 outlet conduits 34 and high pressure sprays fog equipment 6 through the outlet of high-pressure plunger pump 8, spray in first vapor film 20 of dry type steam generator 5, the high pressure spray water is heated in each layer vapor film of dry type steam generator 5 successively, the very fast steam that is converted into; Steam from the 7th vapor film 32 of dry type steam generator 5 come out, in vapor film outlet conduit 37 enters gas-distributing cylinder 12; When temperature in the burner hearth reaches more than 800 ℃, after can making fuel-feed jar 16 interior fuel (fine coal adds pulverized limestone) enter high temperature steam metal coil pipe 17, fuel is brought earlier into post bake heats up in the coil pipe of constant temperature oven 1 inside by steam, spray again and enter in the constant temperature oven 1 with the endogenous kindling material of former burner hearth burn (steam is the cracking oxyhydrogen combustion directly, plays the effect of air inducing, air blast); Solid particle material and liquid material enter in the material steam combustion pipe 18 from the first feeding-in solid body jar 38 and the first liquid head tank 39 respectively, by steam its injection are entered in the constant temperature oven 1 and burn with the endogenous kindling material of former burner hearth; Solid material and liquid charging stock enter material steam from the second feeding-in solid body jar 40 and the second liquid head tank 41 and decompose that (quantity of steam is many in the coil pipe 42, amount is few), carry it into the decomposition of clashing in the tube side that material steam decomposes coil pipe 42 by high-temperature steam, concentrate, dry, expanded, and rapid penetrating material, moisture in the material is become steam, entering spray again produces an unexpected winner and but reduces chamber 43, spray produces an unexpected winner and but reduces chamber 43 and be equipped with and regulate replenish blower fan 44 and cooling sandwith layer 45 plays the effect of cooling, recovery pond 47 is deposited in 47 li of different recovery ponds to the material of raw material different specific weight with diffusion barrier net 46, and high-temperature steam is cooled into aquae destillata by recyclable recyclings in waste heat cooling water pipe 48 inflow condensed water filtering ponds 49 or the hot water swap tank 7, water in the cooling sandwith layer 45 are circulated in hot water swap tank 7 and the cooling sandwith layer 45 by cooling water circulating line 50, play the cooling spray and produce an unexpected winner and but reduce the effect of chamber 43.
Spray produces an unexpected winner and but reduces the steam head-on collision raw material of 43 li of chambers and produce an unexpected winner in spray that but to reduce in the chamber 43 motion showy, regulated the effect of cooling that replenishes blower fan 44 and cooling sandwith layer 45, the realization reduction that cools, fall into 47 li of different recovery ponds different apart from the different specific weight raw material, steam in the steam head-on collision raw material is cooled to aquae destillata and flows in condensed water filtering ponds 49 or the hot water swap tank 7, reaches the separation purpose.
Bian concentrates oven dry with steam boiler with the steam multistage with steam head-on collision substance decomposition burn cycle device, breakthrough traditional handicraft, its advantage is the composition according to different material solution, can adopt the different high-temperature steams concentrate drying that clashes regulate to separate, the material decomposition rate is fast, high-temperature steam penetration capacity strong (similar picture tradition lacquer spraying technique), and fly far away be that the aquae destillata of condensation reduction plays disinfective action simultaneously, device simple, cost of investment is low.The environmental protection of the utility model Product Green, safe, energy-conservation, a tractor serves several purposes can be used for desalinization, various sewage disposal (handle back water quality and reach secondary discharge standard), papermaking wastewater, alcohol effluent, industrial agriculture organic-inorganic liquid waste processing.Chemical industry, generating, mineral products, food, pharmacy, composting, sugaring, starch, milk powder, vegetables Fruit class crystalline solid, the various plant essences of concentration extraction, converted products fields such as fruit juice aquae destillata and drying.
Claims (3)
1. steam head-on collision substance decomposition burn cycle device is characterized in that: it mainly decomposes coil pipe, spray by the first liquid head tank, the second liquid head tank, the first feeding-in solid body jar, the second feeding-in solid body jar, hot water swap tank, high-pressure plunger pump, dry type steam generator, high pressure sprays fog equipment, material steam and produces an unexpected winner and but reduce chamber, constant temperature oven, circulating pump, fuel-feed jar, high-order expansion slot, low level oil storage tank, gas-distributing cylinder, steam turbine and generator and form;
1) structure of each parts is as follows:
1.1) the described first liquid head tank and the second liquid head tank be the slack tank body, the liquid material that interior splendid attire need decompose;
1.2) the described first feeding-in solid body jar and the second feeding-in solid body jar be the slack tank body, the solid particle material that interior splendid attire need decompose;
1.3) described hot water swap tank is the slack tank body, interior splendid attire water;
1.4) described fuel-feed jar is the slack tank body, interior contain fuel;
1.5) described high-order expansion slot is the slack tank body, the conduction oil after interior splendid attire expands;
1.6) described low level oil storage tank is the slack tank body, interior splendid attire conduction oil;
1.7) described constant temperature oven is the body of heater of heated at constant temperature, body of heater has heat-insulation layer outward, and interior is heating clamber, is provided with heat conduction coil pipe, material combustion tube and the high temperature steam metal coil pipe of band conduction oil import and export pipe in the heating clamber;
1.8) described spray produces an unexpected winner and but reduce the chamber front end and be equipped with and regulate replenish that blower fan, inside are equipped with the diffusion barrier net, the below is equipped with recovery pond, has cooling sandwith layer, tail end that waste heat cooling water pipe and condensed water filtering ponds are installed outward;
1.9) described dry type steam generator is for there being the multilayer annular seal circuit of heat-insulation layer outward, it is respectively the first heat conduction oil reservoir, the second heat conduction oil reservoir, the 3rd heat conduction oil reservoir, the 4th heat conduction oil reservoir, the 5th heat conduction oil reservoir, the 6th heat conduction oil reservoir, the 7th heat conduction oil reservoir and the 8th heat conduction oil reservoir, first vapor film, second vapor film, the 3rd vapor film, the 4th vapor film, the 5th vapor film, the 6th vapor film and the 7th vapor film, first vapor film and second vapor film, second vapor film and the 3rd vapor film, the 3rd vapor film and the 4th vapor film, the 5th vapor film and the 6th vapor film, the 6th vapor film and the 7th vapor film are respectively equipped with communicating pipe, the first heat conduction oil reservoir and the second heat conduction oil reservoir, the second heat conduction oil reservoir and the 3rd heat conduction oil reservoir, the 3rd heat conduction oil reservoir and the 4th heat conduction oil reservoir, the 4th heat conduction oil reservoir and the 5th heat conduction oil reservoir, the 5th heat conduction oil reservoir and the 6th heat conduction oil reservoir, the 6th heat conduction oil reservoir and the 7th heat conduction oil reservoir, the 7th heat conduction oil reservoir and the 8th heat conduction oil reservoir are respectively equipped with communicating pipe;
2) connected mode of described each parts of described a kind of steam head-on collision substance decomposition burn cycle device is as follows:
The outlet of hot water swap tank is connected with the import of high-pressure plunger pump by pipeline;
Import with first vapor film of dry type steam generator is connected the high-pressure plunger delivery side of pump with high pressure sprays fog equipment by high-pressure plunger pump pipe outlet pipe;
The 7th vapor film outlet of dry type steam generator is connected with the import of gas-distributing cylinder by the vapor film outlet conduit;
Three outlets of gas-distributing cylinder are connected with the import of material steam decomposition coil pipe, material steam combustion tube, high temperature steam metal coil pipe and steam turbine respectively by pipeline; The second feeding-in solid body jar and the second liquid head tank are installed decomposing on the pipeline that coil pipe is connected with material steam respectively; With pipeline that the material steam combustion tube is connected on the first feeding-in solid body jar and the first liquid head tank are installed respectively; At the pipeline that is connected with high temperature steam metal coil pipe the fuel-feed jar is installed;
The outlet that material steam decomposes coil pipe is but reduced the import of chamber and is connected with spraying to produce an unexpected winner;
Spray produces an unexpected winner and but reduces the import and export pipe of cooling sandwith layer of chamber and be connected with the going out of cooling water circulating line, inlet tube respectively, and recovery pond is housed below cooling sandwith layer; Spray produces an unexpected winner and but reduces the outlet of chamber interior by the waste heat cooling water pipe and be connected with the import of hot water swap tank, in connecting pipe the cooling water filtering ponds is housed;
The outlet of the heat conduction coil pipe of constant temperature oven is connected with the import of the first heat conduction oil reservoir of vapour generator and the import of low level oil storage tank respectively by the heat conductive oil inlet pipeline; The heat conduction coil pipe import of constant temperature oven is connected with outlet of circulating pump by the conduction oil outlet conduit; Outlet of circulating pump is connected with the 8th heat conduction oil reservoir import of dry type steam generator; The outlet of high-order expansion slot is connected with the import of low level oil storage tank.
2. steam according to claim 1 head-on collision substance decomposition burn cycle device, it is characterized in that: it act as atomizing heated moisture body described dry type steam generator, is 1-1000 dry type steam generator parallel connection assembly.
3. steam according to claim 1 head-on collision substance decomposition burn cycle device, it is characterized in that: described constant temperature oven is 1-100 constant temperature oven parallel connection assembly.
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| CN2013201426623U CN203108239U (en) | 2013-03-27 | 2013-03-27 | Steam colliding material decomposition and combustion circulating device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103191570A (en) * | 2013-03-27 | 2013-07-10 | 赖正平 | Recycling device capable of decomposing and burning matters through vapor clash |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103191570A (en) * | 2013-03-27 | 2013-07-10 | 赖正平 | Recycling device capable of decomposing and burning matters through vapor clash |
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