CN103191570B - Recycling device capable of decomposing and burning matters through vapor clash - Google Patents
Recycling device capable of decomposing and burning matters through vapor clash Download PDFInfo
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Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
- Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply
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- Engine Equipment That Uses Special Cycles (AREA)
Abstract
The invention discloses a recycling device capable of decomposing and burning matters through vapor clash. The recycling device mainly comprises a first liquid feeding tank, a second liquid feeding tank, a first solid feeding tank, a second solid feeding tank, a hot water exchange tank, a high-pressure plunger pump, a drying-type steam generator, a high-pressure atomizing device, a matter steam disintegrating pipe coil, a spray explosion cooling reduction chamber, a constant temperature furnace, a circulating pump, a fuel feeding tank, a high-position expansion tank, a low-position oil storage tank, a steam header, a steam turbine and a generator. The recycling device has the following advantages: 1, the recycling device can be used for solving the detects of conventional boilers and breaking through steam temperature without needing pressure; and 2, the recycling device can be used for solving traditional process production and making use of steam for supporting heat energy, generating electricity, desalinating seawater, treating sewage and garbage, decomposing at high speed, concentrating, extracting, drying the matters and deeply processing products, steam is reheated in a 80 DEG C furnace body and is cracked into hydrogen and oxygen which are used for circular burning, the matters are burned through reheated steam, and the recycling device is multipurpose high-efficiency energy-saving emission reduction environmental protection equipment.
Description
Technical field
The present invention relates to a kind of dry type steam generator.A kind of steam head-on collision substance decomposition burn cycle device specifically.
Background technology
The concentrated drying plant complex process multistage of tradition, machines cumbersome, cost of investment is high, consumes energy high.The development in the fields such as the industrial crystallization bodies such as serious restriction China food, desalinization, pharmacy, sugaring, papermaking, alcohol, chemical industry, rubbish, sewage, mineral products are concentrated, extract, decompose, dry.The present invention improves upgrading on circulation electric generating apparatus, multipurpose spraying-exploding type high-pressure tempered gas decomposition dry type steam generator in original solar oil heat conducting and supplying device, heat radiation.After the steam producing in dry type steam generator and various material clash within material steam decomposes coil pipe, by the water transform in material, be gas, enter spray quick-fried reduction chamber, aloft showy distance is different with the position than resedimentation, result that it obtains is different, can decompose any material, and water becomes distance after the cooling reduction of steam farthest, reductive water is capable of circulation to be used to hot water storage tank's continuous circulation, plays the effect of high-efficiency water-saving, energy-conservation, environmental protection and high-temperature sterilization.Its advantage is can adopt different temperature to regulate separation according to the composition of different material.Material decomposition rate is fast, and steam is by furnace body metal coil pipe post bake, and being warming up to that 800 degree are above can By Direct Pyrolysis oxyhydrogen combustion, other combustibles is clashed to be transported in furnace body by steam simultaneously and burns together with the kindling material of source.Device simple, cost of investment is low, and the thermal efficiency that is only improved pot (generator) could real efficient energy-saving and emission-reducing.
Summary of the invention
The steam head-on collision substance decomposition burn cycle device of the object of this invention is to provide a kind of pattern novelty, simple structure, energy-efficient, thermal conversion efficiency is high, generator heat exchange area all makes full use of, moment produces high-temperature high-pressure overheat steam, environmental protection.
The technical scheme that the present invention 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 first liquid head tank, second liquid head tank, the first feeding-in solid body tank, the second feeding-in solid body tank, 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 tank, 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) described first liquid head tank and second liquid head tank are slack tank body, the liquid material that interior splendid attire need decompose;
1.2) described the first feeding-in solid body tank and the second feeding-in solid body tank are slack tank body, the solid particle material that interior splendid attire need decompose;
1.3) described hot water swap tank is slack tank body, interior splendid attire water;
1.4) described fuel-feed tank is slack tank body, interior contain fuel;
1.5) described high-order expansion slot is slack tank body, the conduction oil after interior splendid attire expands;
1.6) described low level oil storage tank is slack tank body, interior splendid attire conduction oil;
1.7) body of heater that described constant temperature oven is 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 high temperature steam metal coil pipe with conduction oil import and export pipe in heating clamber;
1.8) described spray produces an unexpected winner and but reduces chamber front end and be provided with and regulate supplement that blower fan, inside are equipped with diffusion barrier net, below is provided 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, for to have the multilayer annular seal circuit of heat-insulation layer outward, 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, the first vapor film, the second vapor film, the 3rd vapor film, the 4th vapor film, the 5th vapor film, the 6th vapor film and the 7th vapor film, the first vapor film and the second vapor film, the 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) described in described a kind of steam head-on collision substance decomposition burn cycle device, the connected mode of each parts is as follows:
The outlet of hot water swap tank is connected with the import of high-pressure plunger pump by pipeline;
High-pressure plunger delivery side of pump is connected with the import of the first vapor film of dry type steam generator 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 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; On the pipeline being connected with material steam decomposition coil pipe, the second feeding-in solid body tank and second liquid head tank are installed respectively; The first feeding-in solid body tank and first liquid head tank are installed respectively on the pipeline being connected with material steam combustion tube; On the pipeline being connected with high temperature steam metal coil pipe, fuel-feed tank 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 circulation pipeline, 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 waste heat cooling water pipe and be connected with the import of hot water swap tank, and cooling water filtering ponds are housed in connecting pipe;
The heat conduction coil pipe outlet of constant temperature oven is connected with the import of low level oil storage tank with the import of the first heat conduction oil reservoir of vapour generator respectively by heat conductive oil inlet pipeline; The heat conduction coil pipe import of constant temperature oven is connected with circulation delivery side of pump by conduction oil outlet conduit; Circulation delivery side of 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 parallel combination body.
Above-mentioned steam head-on collision substance decomposition burn cycle device, described constant temperature oven is 1-100 constant temperature oven parallel combination body.
Advantage of the present invention:
1. steam head-on collision substance decomposition burn cycle device, power consumption are half of conventional boiler, greatly reduce production costs, and shorten the technological process of production.
2. break through the pattern of steaming that upper century-old boiler water boils bubble type, by heating wet steam body and without high temperature, produce steam, generator heat exchange area all makes full use of, and injects liquid material cold water, and moment produces high pressure-temperature superheated steam.
3. the thermal conversion efficiency of dry type steam generator is up to more than 95%, the jet chimney steam flow speed processed of dry type steam generator 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, greatly reduce production costs, zero-emission, environmental protection.
4. vapor (steam) temperature is without deliberately realizing by pressure, and steam pressure and temperature can regulate arbitrarily, realizes high speed substance decomposition.
5. the number of units 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 conventional boiler defect, realize in dry type steam generator without condensed water, Non-scale, without blowdown, reduce artificial treatment incrustation scale and charges for disposing pollutants and use.
7. by the high-temperature steam moisture content in substance decomposition material, dry, expanded that clashes, its speed of action is fast, and hot mechanical efficiency is high.
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, by secondary deep processing, be allocated as the high nutritious fertilizer of liquid of crops.
9. use high-temperature steam head-on collision rubbish, after being dried by autoclave sterilization, by secondary deep processing, be allocated as the senior organic fertilizer of various crops.
10. using high-temperature steam head-on collision vegetables, fruit, can deep processing be pulvis, liquid beverage, solid food, extends the food consumption phase.
11. use the high-temperature steams various materials that clash, and as medicine, chemical industry, seawater, sugaring, starch, dairy products, food etc., can concentrate, be dried, 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 furnace body by indirect steam and burn together with the kindling material of source.
13. steam can, by more than secondary temperature elevation to 800 ℃, be cracked into hydrogen-oxygen and burn together with the endogenous kindling material of stove.
14. use high-temperature steams 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 source kindling material, the material after burning can deep processing become organic fertilizer.
15. are used in the industrial of required high-temperature low-pressure steam, safer.
16. steam may be used on cryogenic high pressure for steam ejection, steam-driven motor and cogeneration of heat and power.
17. can accomplish generator fixed fire producing steam at any time in using this device procedures, and the conduction oil in heat carrier furnace and generator plays accumulation of energy effect while not steaming, conduction oil specific heat plays adjusting temperature action during Datong District, also plays a role in energy conservation.
The present invention mainly studies 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 the research to pot (dry type steam generator) separately, the principle that the present invention utilizes material to be present in intermolecular a kind of attraction is studied.For the similar material of composition and structure, its boiling point to water, fusing point, heat of gasification, melting heat, solubility, surface tension, the physicochemical properties such as viscosity have decisive, generally along with the increase of relative molecular mass, strengthen, so improve a pot thermal efficiency, will Bian by mechanical pump pressure, liquid water being become to steam fog heats and realizes producing steam application, adopt heat carrier furnace and dry atomizing generator, the fast specific heat of conduction oil intensification thermal velocity is large, while not steaming, conduction oil can play energy storage and regulate the features such as temperature action, getting around poach bubble type steams, kiss and point in the timing pressure size by generator and thermal power and the continuous post water spray of mechanical pump pressure amount, the thermal-radiating distance of structure in 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 steam boiler Ke Jie Neng Minus in the future arranges over half, can contrast with traditional poach bubble type pot.Dry atomizing generator can produce low-voltage high-temperature superheated steam, also can dock use with solar oil heat conducting and supplying device by high pressure-temperature.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, kiss and point to the temperature speed of indirect steam intensification cracking oxyhydrogen combustion and material head-on collision burning, reach combustion purpose together with the kindling material of source, 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.
Accompanying drawing explanation
Fig. 1 is steam head-on collision substance decomposition burn cycle apparatus structure schematic diagram of the present invention.
In 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 tank 16, high temperature steam metal coil pipe 17, material steam combustion tube 18, feeding-in solid body tank 38, liquid head tank 39, feeding-in solid body tank 40, liquid head tank 41, material steam decomposes coil pipe 42, spray produces an unexpected winner and but reduces chamber 43, regulate and supplement 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 circulation pipeline 50, circulating pump 51.
Fig. 2 is dry type steam generator A end structure schematic diagram of the present invention.
Fig. 3 is dry type steam generator B end structure schematic diagram of the present invention.
In figure: heat conduction oil reservoir 19,21,23,25,27,29,31,33, vapor film 20,22,24,26,28,30,32, the outlet conduit 34 of high pressure piston pump, heat conductive oil inlet pipeline 35, conduction oil outlet conduit 36, vapor film outlet conduit 37.
The specific embodiment
Steam in fluid motion without condensed water in dry type steam generator of the present invention inherence, Non-scale, dry type steam generator can be coincide and for sprayer unit, be sprayed in generator by electric-controlled mechanical pump pressure, belonging to dry spraying-exploding type steams, in breakthrough the large water gaging of century-old one-time heating repeat acting and poach bubble type steam, steam pressure and the temperature high-temperature low-pressure producing steam that is not directly proportional, also can HTHP producing steam, also can utilize the complementary heating of various energy resources and solar energy conduction oil, thermal energy transfer is arrived to dry type steam generator, the wet gas current being atomized in heat drying formula steam generator, make the heat content in the whole moments generation of 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%, generator pipeline holds B end steam flow speed processed to reach per hour more than 110 kilometers from A, the present invention can be applicable to modern national defense, space flight, industry, generating, steam catapult in field, on the equipment such as steam-driven motor, use.Realize critical effect, only have and in dry type steam generator, improve thermal efficiency vapour speed processed and could really 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 material convert rapidly the quick-fried reduction chamber of arriving of gas spray to by high steam, in showy process, make gas and material decompose in the process of sedimentation aloft, 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, after gas cooled reduction, be converted into distilled water, be recycled to sedimentation and filtration ditch, use with hot water exchanger water circulation again.Post bake steam metal coil pipe cleavable oxyhydrogen combustion in furnace body, simultaneously by other combustibles, clashes to be transported in furnace body by steam and burns together with the kindling material of source, plays forced draft induced draft effect, forms the equipment of a whole set of reproducible utilization resource.
Below in conjunction with accompanying drawing, the invention will be further described with concrete enforcement.
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 first liquid head tank 39, second liquid head tank 41, the first feeding-in solid body tank 38, the second feeding-in solid body tank 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 tank 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) described first liquid head tank and second liquid head tank are slack tank body, the liquid material that interior splendid attire need decompose;
1.2) described the first feeding-in solid body tank and the second feeding-in solid body tank are slack tank body, the solid particle material that interior splendid attire need decompose;
1.3) described hot water swap tank 7 is slack tank body, interior splendid attire water;
1.4) described fuel-feed tank 16 is slack tank body, interior contain fuel;
1.5) described high-order expansion slot 10 is slack tank body, the conduction oil after interior splendid attire expands;
1.6) described low level oil storage tank 9 is slack tank body, interior splendid attire conduction oil;
1.7) body of heater that described constant temperature oven 1 is 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 high temperature steam metal coil pipe 17 with conduction oil import and export pipe in heating clamber;
1.8) described spray produces an unexpected winner and but reduces chamber 43 front ends and be provided with and regulate supplement that blower fan 44, inside are equipped with diffusion barrier net 46, below is provided 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, for to have the multilayer annular seal circuit of heat-insulation layer outward, 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, the first vapor films 20, the 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, the first vapor films 20 and the second vapor film 22, the 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) described in described a kind of steam head-on collision substance decomposition burn cycle device, the connected mode of each parts is as follows:
The outlet of hot water swap tank 7 is connected with the import of high-pressure plunger pump 8 by pipeline;
The outlet of high-pressure plunger pump 8 is connected with the import of the first vapor film 20 of dry type steam generator 5 with high pressure sprays fog equipment 6 by high-pressure plunger pump pipe outlet pipe 34;
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 steam turbine 14 with material steam decomposition coil pipe 42, material steam combustion tube 18, high temperature steam metal coil pipe 17 respectively by pipeline; On the pipeline being connected with material steam decomposition coil pipe 42, the second feeding-in solid body tank 40 and second liquid head tank 41 are installed respectively; The first feeding-in solid body tank 38 and first liquid head tank 39 are installed respectively on the pipeline being connected with material steam combustion tube 18; On the pipeline being connected with high temperature steam metal coil pipe 17, fuel-feed tank 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 circulation pipeline 50, inlet tube respectively, and recovery pond 47 is housed below cooling sandwith layer 45; Spray produces an unexpected winner and but reduces the outlet of 43 inside, chamber by waste heat cooling water pipe 48 and be connected with the import of hot water swap tank 7, and cooling water filtering ponds 49 are housed in connecting pipe;
The heat conduction coil pipe outlet of constant temperature oven 1 is connected with the import of low level oil storage tank 9 with the import of the first heat conduction oil reservoir 19 of vapour generator 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 combination body.
Above-mentioned steam head-on collision substance decomposition burn cycle device, described constant temperature oven 1 is 1-100 constant temperature oven parallel combination body.
Implement when of the present invention: conduction oil is injected in the heat conduction coil pipe of constant temperature oven 1 and the heat conduction oil reservoir of dry type steam generator 5, constant temperature oven 1 uses fuel (as coal dust, fuel oil, combustion gas, living beings etc.) combustion heating is as the kindling material in burner hearth, ON cycle pump 11, conduction oil is circulated in the heat conduction coil pipe of constant temperature oven 1 and the heat conduction oil reservoir of dry type steam generator 5, constant temperature oven 1 arrives operating temperature by heat-conducting oil heating, make each layer of heat conduction oil reservoir of dry type steam generator 5 be heated to operating temperature, each layer of heat conduction oil reservoir of dry type steam generator 5 conducts heat heat to each layer of vapor film of dry type steam generator 5, the flue gas of discharging during constant temperature oven 1 burning enters after chimney 4, when the waste heat coil pipe 3 in superheated water swap tank 7, by the water heating in hot water swap tank, by the water in hot water swap tank 7 after the outlet of high-pressure plunger pump 8 makes water fogging by high-pressure plunger pump 8 outlet conduits 34 and high pressure sprays fog equipment 6, spray in the first vapor film 20 of dry type steam generator 5, high pressure spray water is heated successively in each layer of vapor film of dry type steam generator 5, the very fast steam that is converted into, steam from the 7th vapor film 32 of dry type steam generator 5 out, in vapor film outlet conduit 37 enters gas-distributing cylinder 12, when in burner hearth, temperature reaches more than 800 ℃, can make the fuel (fine coal adds pulverized limestone) in fuel-feed tank 16 enter after high temperature steam metal coil pipe 17, by steam, fuel first being brought into post bake in the coil pipe of constant temperature oven 1 inside heats up, spray again and enter in constant temperature oven 1 and burn together with the endogenous kindling material of former burner hearth (steam can By Direct Pyrolysis oxyhydrogen combustion, play air inducing, drum wind action), solid particle material and liquid material enter in material steam combustion pipe 18 from the first feeding-in solid body tank 38 and first liquid head tank 39 respectively, then by steam, its injection are entered in constant temperature oven 1 and burnt together 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 tank 40 and second liquid head tank 41 and decompose that in coil pipe 42, (quantity of steam is many, amount is few), by high-temperature steam, carry it into the decomposition of clashing in the tube side that material steam decomposes coil pipe 42, concentrated, dry, expanded, and rapid penetrating material, moisture in material is become to steam, entering spray produces an unexpected winner and but reduces chamber 43 again, spray produces an unexpected winner and but reduces chamber 43 and be equipped with and regulate supplement blower fan 44 and cooling sandwith layer 45 plays the effect of cooling, recovery pond 47 and diffusion barrier net 46 are deposited in 47 li of different recovery ponds the material of raw material different specific weight, and high-temperature steam is cooled into aquae destillata by waste heat cooling water pipe 48 inflow condensed water filtering ponds 49 or the interior recyclable recyclings of hot water swap tank 7, water in cooling sandwith layer 45 is circulated in hot water swap tank 7 and cooling sandwith layer 45 by cooling water circulation pipeline 50, playing cooling spray produces an unexpected winner and but reduces 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 and but reduce the interior motion in chamber 43 and float in spray, the effect of cooling of modulated supplementary blower fan 44 and cooling sandwith layer 45, the realization reduction that cools, at different distance different specific weight raw materials, fall into 47 li of different recovery ponds, steam in steam head-on collision raw material is cooled to aquae destillata and flows in condensed water filtering ponds 49 or hot water swap tank 7, reaches separated object.
For Bian, for steam head-on collision substance decomposition burn cycle device, breakthrough traditional handicraft, steam boiler is dried with steam multistage is concentrated, its advantage is according to the composition of different material solution, can adopt the different high-temperature steams concentrate drying that clashes to regulate separated, 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.Product Green environmental protection of the present invention, safe, energy-conservation, a tractor serves several purposes, can be used for desalinization, various sewage disposal (after processing, water quality reaches 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, fruit juice aquae destillata and the converted products field such as dry.
Claims (3)
1. steam head-on collision substance decomposition burn cycle device, is characterized in that: by first liquid head tank, second liquid head tank, the first feeding-in solid body tank, the second feeding-in solid body tank, hot water swap tank, high-pressure plunger pump, dry type steam generator, high pressure sprays fog equipment, material steam, decompose coil pipe, spray and produce an unexpected winner and but reduce chamber, constant temperature oven, circulating pump, fuel-feed tank, 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) described first liquid head tank and second liquid head tank are slack tank body, the liquid material that interior splendid attire need decompose;
1.2) described the first feeding-in solid body tank and the second feeding-in solid body tank are slack tank body, the solid particle material that interior splendid attire need decompose;
1.3) described hot water swap tank is slack tank body, interior splendid attire water;
1.4) described fuel-feed tank is slack tank body, interior contain fuel;
1.5) described high-order expansion slot is slack tank body, the conduction oil after interior splendid attire expands;
1.6) described low level oil storage tank is slack tank body, interior splendid attire conduction oil;
1.7) body of heater that described constant temperature oven is 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 high temperature steam metal coil pipe with conduction oil import and export pipe in heating clamber;
1.8) described spray produces an unexpected winner and but reduces chamber front end and be provided with and regulate supplement that blower fan, inside are equipped with diffusion barrier net, below is provided 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, for to have the multilayer annular seal circuit of heat-insulation layer outward, 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, the first vapor film, the second vapor film, the 3rd vapor film, the 4th vapor film, the 5th vapor film, the 6th vapor film and the 7th vapor film, the first vapor film and the second vapor film, the 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) described in described a kind of steam head-on collision substance decomposition burn cycle device, the connected mode of each parts is as follows:
The outlet of hot water swap tank is connected with the import of high-pressure plunger pump by pipeline;
High-pressure plunger delivery side of pump is connected with the import of the first vapor film of dry type steam generator 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 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; On the pipeline being connected with material steam decomposition coil pipe, the second feeding-in solid body tank and second liquid head tank are installed respectively; The first feeding-in solid body tank and first liquid head tank are installed respectively on the pipeline being connected with material steam combustion tube; On the pipeline being connected with high temperature steam metal coil pipe, fuel-feed tank 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 circulation pipeline, 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 waste heat cooling water pipe and be connected with the import of hot water swap tank, and cooling water filtering ponds are housed in connecting pipe;
The heat conduction coil pipe outlet of constant temperature oven is connected with the import of low level oil storage tank with the import of the first heat conduction oil reservoir of vapour generator respectively by heat conductive oil inlet pipeline; The heat conduction coil pipe import of constant temperature oven is connected with circulation delivery side of pump by conduction oil outlet conduit; Circulation delivery side of 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 head-on collision substance decomposition burn cycle device according to claim 1, is characterized in that: it act as atomizing heated moisture body described dry type steam generator, is 1-1000 dry type steam generator parallel combination body.
3. steam head-on collision substance decomposition burn cycle device according to claim 1, is characterized in that: described constant temperature oven is 1-100 constant temperature oven parallel combination body.
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| CN105910094B (en) * | 2016-06-16 | 2017-11-03 | 赖正平 | The integrated steam boiler of gas fuel, fused salt |
| CN107940426A (en) * | 2017-10-11 | 2018-04-20 | 广东欣鑫华能环保科技有限公司 | Overcritical pyrolyzing coal pneumoelectric sprays flash boiler |
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| CN102606429B (en) * | 2012-03-30 | 2013-09-11 | 赖正平 | Thermal-radiation internal-circulation power generation device |
| CN102794030B (en) * | 2012-08-23 | 2014-01-29 | 赖正平 | Multipurpose spray explosion-type high-pressure temperature-adjustment vapor decomposition drying steam generator |
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Effective date of registration: 20151221 Address after: 061000, Cangzhou City, Hebei province Wuqiao County song Industrial Park Road, latitude three and two road junction northwest corner Patentee after: Hebei can Boiler Equipment Co., Ltd. Address before: Support 530021 Nanning Road, the Guangxi Zhuang Autonomous Region No. 14 3 floor Patentee before: Lai Zhengping |
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