CN101408358A

CN101408358A - Method and equipment for preparing clean energy of low price and high efficiency

Info

Publication number: CN101408358A
Application number: CNA2007101639332A
Authority: CN
Inventors: 孔喜; 孔德凯
Original assignee: Individual
Current assignee: Individual
Priority date: 2007-10-12
Filing date: 2007-10-12
Publication date: 2009-04-15

Abstract

The invention provides a method and equipment used for preparing clean energy resource with low cost and high efficiency; wherein, the equipment consists of cold storage and deep cold storage of a multi-step refrigeration quantity enlarger which gains potential from the gas by an adiabatic expansion principle, an air cold phase change disc pipe, a gas storage tank, a manual wind-power generator, a hydrogen preparing machine, a solid hydrogen or hydrogen oil synthesis equipment, a bottled fluidified air shunting machine and a coldness exchanger, can utilize the potential in-situ to sequentially prepare cold energy, gas energy, electric energy, solid hydrogen or hydrogen oil at low cost so as to particularly pull the ecological development of the coldness engineering, aerodynamic vehicles, environmental protection generation industry, energy-saving buildings or under film off-season cultivation, and can realize the sustainable development of the resource disposal of CO2.

Description

Cheap highly effective is produced the method and the equipment of clean energy resource

Field of the present invention:

The invention belongs to the clean energy resource field, particularly environmental protection and low-cost sustainable method and the equipment of producing deep cooling energy, liquefied air, electric energy, solid hydrogen and hydrogen oil.

Background technology of the present invention:

Because productive life of fossil energy is less than 40 years, in time finds novel clean energy resource very urgent, but wind-power electricity generation is a developing direction is subjected to the wind resource limitation and can not popularizes employing and maybe can not obtain stable electric power; It is developing direction but cost is too high that brine electrolysis is produced hydrogen energy source, produce the hydrogen that is equivalent to 1 kilogram of gasoline heat energy and need power consumption 21 degree, the cost height be difficult for coming into the market; Utilize nuclear energy water Jie method can reduce the hydrolytic hydrogen production cost, but the infusion of financial resources of nuclear energy water Jie hydrogen manufacturing equipment is too big, and development nuclear energy does not meet the principle of human security existence; See the scheme of utilizing compressed air engine to replace combustion heat power machine development zero-emission railcar is arranged, but the compression power consumption cost of producing liquefied air is greater than electrolytic hydrogen production, whole world automobile pollution is above 700,000,000, by each average year travel 20,000 kilometers if all adopt to compress and liquefy air be that power is then annual needs more than power consumption 20,000,000,000,000 degree, obvious reduction liquefied air to produce cost significant; The human solar energy of having known together is the abundantest energy, the heat energy that sun per minute passes to the earth is equivalent to 2.4 hundred million tons of standard coals, as calculated daytime surface temperature should be higher than and the sun between 127 ℃ of the surface temperatures of the close moon of distance, but the earth does not produce high temperature, reason is to have 50% solar energy to be consumed in the lasting phase transformation and the motion of 520,000 cubic kilometers of rainwater, having only few part conversion of solar energy is vegetation and petrochemical industry energy, where have a large amount of solar energy gone? the solar energy of considerable amount stores in fact, and the earth becomes " potential ", " potential " can be obtained with forms such as " it are cold to dive ", and the drilling rod when for example prospecting bores and reaches the underground overstocked high concentration CO that has ₂The lime stone layer time, CO ₂Gas scurries out to bear deep cooling in the hell natural birth along drilling rod makes the drilling rod mouth bear the shining white dry ice of one deck, and the formation temperature of dry ice must be below-72 degree, and what this cold come from? reason is CO ₂The adiabatic expansion behavior has taken place in air velocity when very fast, its can draw gas in environment latent cold energy and form low temperature; Modal adiabatic expansion phenomenon is the CO that human is breathed out out when chewing Ba Haqi ₂Be hotness, and firmly with chewing the CO that blows out when crust is blown ₂Then be creeping chill, the CO that comes out in chew ₂All be same human body temperature, it can heat and the difference that can freeze is CO ₂The flow velocity difference; All gas all has in adiabatic expansion the ability of emitting " it is cold to dive ", and Chinese 98117685.2 patents of invention disclose use ammonia refrigeration working medium, U.S.'s U6339936B1 patent of invention discloses use CO ₂As the method for refrigeration working medium adiabatic expansion refrigeration, Chinese 200510053502.1 patents of invention have proposed to utilize ammonia refrigeration cold compensation CO ₂The adiabatic expansion refrigerating method, the adiabatic expansion cryogenic temperature of gas with various is different, routine CO ₂The restriction refrigerating environment must not be lower than-62 ℃, CO when being lower than-62 ℃ during as refrigeration working medium ₂No longer gasify and have the adiabatic expansion ability no longer; Utilize all gas all to have to store and in adiabatic expansion, obtain deep cooling relatively behind the solar energy or continue more the ability of cryogenic environment can be used for liquefying all gases and transform into various clean energy resourcies.

Content of the present invention:

The present invention discloses a kind of expansion technique of cryogenic insulating step by step of gas with various and equipment cheapness utilized and produces cold energy, gas energy, electric energy, solid hydrogen and hydrogen oil; Content of the present invention is: " a kind of Cheap highly effective is produced the method and the equipment of clean energy resource ", by multistage adiabatic expansion refrigeration cold enlarger, be close to the multistage deep cooling storehouse of freezer, the cold phase transformation coil pipe of air of band filter and compression pump, air accumulator, the artificial airflow generator, hydrogen making machine, Gu hydrogen or the synthetic equipment of hydrogen oil, can liquefied air shunting machine and cold power interchanger are formed, the deep cooling storehouse of at least two above phase disjunctors is under the freezer or in the freezer, the cold phase change disk pipe range of air range hadn wheel is put by colder deep cooling storehouse of a ratio and insert the liquefied air storage tank by compression pump in the coldest deep cooling storehouse, and the efferent duct of liquefied air storage tank is connected installation of liquefied air diversion cans or strength generator through intelligent Self controlling valve shunting; Refrigeration working medium employing critical-temperature in the multistage adiabatic expansion refrigeration cold amplification equipment in the freezer of related ground is-62 ℃ CO ₂, cold compensation source is selected ammonia refrigeration device or iso-butane refrigerator and multistage CO for use ₂Refrigeration cold enlarger is formed conjuncted refrigeration equipment; Wherein the ammonia refrigeration device is by the ammoniacal liquor basin, ammoniacal liquor circular flow siphunculus, ammonia spirit electric heating evaporation section on the ammoniacal liquor runner pipe, smart gold-plating device section and the cointegrate of being made up of with condenser section and refrigerator pipe or frozen water pipe respectively " L " type heat pipe and ammoniacal liquor fuse section to be formed, the lower end of " L " type heat pipe in the cointegrate is adjacent to into coenosarc with parallel ammonia condensing area under control section, the upper end of " L " type heat pipe is adjacent to into coenosarc with refrigerator pipe or frozen water pipe again, " L " type heat pipe that can be adjacent to mutually, refrigerator pipe or frozen water pipe and condenser pipe section all adopt the half-moon-shaped hollow and thin-walled metal tube of square or band side plane, pipe plane between the tube and tube abuts against each other into coenosarc, is full of parallel hollow inorganic fibre pipe and hot superconductive medium in " L " type heat pipe; The related refrigeration cold of freezer or deep cooling storehouse amplifier all is multistage connected structure refrigeration bodies, is made up of choke valve, adiabatic expansion chamber, cold compensator, refrigerant liquid delivery pump, refrigeration working medium and refrigeration working medium storage chamber; The present invention is lower than the composite environmental-friendly gas that corresponding employing critical-temperature in-50 ℃ the deep cooling storehouse is lower than-62 ℃ in temperature be refrigeration working medium, the compound alkane of example, compound lithium bromide etc., in last deep cooling storehouse of the most following or innermost layer, multistage adiabatic expansion refrigeration working medium adopts critical-temperature a little less than-196 ℃ environmental protection gas; Be in that the adiabatic expansion of the chopped-off head refrigerator in freezer or the deep cooling storehouse is indoor to be equipped with two small-sized refrigerating colds compensation sources, one is the cold compensation source of independently freezing, and another back level refrigeration source from refrigeration cold amplifier distributes; Wherein the back level refrigeration cold amplifier of seat of honour freezer also on the cold compensation source that distributes parallel connection distribute another cold compensation source, its upper end with " L " type heat pipe of ammonia refrigeration device is adjacent to into the cooling source that the coenosarc structure becomes the quick loss of heat device of ammonia refrigeration device; Related can liquefied air shunting machine is made up of barometric transfusion house steward, shunting woven hose, liquefied air jar that preposition intelligent control valve and observation liquefied air reach full irrigation pressure, the shunting woven hose is the parallel connection structure, and its termination has to chew with the gas of liquefied air jar and can make things convenient for the closed salable hickey that spins; Related gas driven generator is made up of the appendix of the larger storage tank that absorbs natural energy, preposition intelligent control valve, fan blade, fan blade casing, rotating shaft mounting, gear-box, the gas driven generator of band rotating shaft, the insertion of underground heat heat pipe that is in central authorities in the larger storage tank is underground, it is equipped with the dispel the heat upper end of stainless copper sheet of disjunctor and is in the liquefied air, the fan blade central rotating shaft stretches out the rotating shaft mounting and connects the rotating speed of controlling alternator shaft with change gear box, but the standardized wind-driven generator of related gas driven generator adapted; Related cold power interchanger, be equipped with the water-carriage system that the cold water inlet pipe of pulsating pump, the frozen water efferent duct inhaling cooling coil and be equipped with water-delivery pump are formed periodic duty by connection, cold water inlet pipe and the cold power user of the parallel process of frozen water efferent duct, cold power user can be off-season cultivation equipment under the film, is made up of the weather-proof air cushion plastic film of plantation canopy frame, good transmittance under cold scattering water pipe, the film and holds CO ₂Gas is fertile and hold space environment under the film of cold or warm temperature, and the dropper cold scattering water pipe in the plantation canopy becomes the canopy film planting environment cooling source of cheap cooling of heat phase under the frozen water of circulation cooling is flowed through film from freezer; Cold power user can be the dwelling house of central heating, frozen water is used the delivery pipeline and is entered the residential area through carrier pipe enter dwelling house from distributive pipe under output water pump effect, the frozen water distributive pipe is at first fitted with the loss of heat pipe of efficient ammonia refrigeration refrigerator and is made efficient ammonia refrigeration absorption refrigerator can produce freezing deep cooling, the frozen water blower fan frozen water coil pipe air-conditioning of flowing through, blower fan is sent the cold of frozen water in the coil pipe to the dwelling house cooling with convection type, and the cold fresh-keeping built-in wardrobe of not power consumption is formed in the frozen water frozen water coil pipe association that rear wall is equipped with in the cold antistaling cabinet of Aumbry type of frozen water coil pipe of also can in parallel flowing through; Related electrolytic water device can adopt standardized equipment; Related electron resonance water-splitting hydrogen production machine splits Jie's water device by the electron resonance that is communicated with through gas compression pump and the liquid gas diversion cans is formed, it is the hollow ring resonator that electron resonance splits Jie's water device, be in water in the water pipe at resonator center by the mist of resonance splitting Cheng Qing and oxygen, gas compression pump is pressed into hydrogen and oxygen gas mixture in the special-purpose basin and makes into liquefaction, and liquid gas shunting basin top and the bottom respectively have a shunting to chew; Related solid hydrogen paint storage tank machine for adding hydrogen is made up of liquid hydrogen paint storage tank, gas compression pump, solid hydrogen paint storage tank, compression pump is positioned on the withstand voltage wireway that connects solid hydrogen paint storage tank and liquid hydrogen paint storage tank, and solid hydrogen paint storage tank fills hydrogen also can be adopted liquefied air shunting can equipment to be connected in series compression pump hydrogen is filled in a plurality of hydrogen paint storage tank parallel connections admittedly simultaneously; The synthetic equipment of related hydrogen oil is by the steam pipe of built-in safe jet electric heating heat booster, synthetic tower, the mixing intensification tower of coal dust, carbon dioxide and hydrogen, catalyst filtered and recycled device, cooling tower is formed, cut syndeton in wherein the mixing intensification tower of coal dust, carbon dioxide and hydrogen is equipped with the carbon dioxide input pipe of unidirectional defeated material intelligence control magnetic valve and hydrogen input pipe and the inwall garden face that mixes the intensification tower becomes, the recyclable catalyst that recycles is delivered in the conveying pipeline that is between synthetic tower and the mixing intensification tower via pipe special; The cross section that wherein safe excess temperature heats the jet electroheat member is a square and is made up of the jet hot hole road of massive parallel, four jiaos of jet electroheat member that the cross section is square are tangent and form the heat insulation side rooms of four obstructed steam of sealing along tube wall with steam pipe garden inwall, jet electric heating duct is made up of the flat aluminum pipe wall and the aluminium flake heat transfer muscle that clamp the high stone paper Electric radiant Heating Film parts of microballoon concentration in twos, wherein the stone paper electroheat member is formed by clamping stone paper tin oxide electrothermic film element in two layers of insulating trip, stone paper electrothermic film element two sides is a pair of tin oxide face electric heating field boundary parallel and that power is close that evenly equates, the waist central authorities that a pair of common electrode is in stone paper tin oxide electrothermic film element make the electrothermic film element parallel connection on stone paper two sides, electrode and connection lead are in the heat insulation side room enclosed environment that does not contact steam, this invented technology is the carbon dust that contains the catalyst composition that need not to reclaim, carbon dioxide, hydrogen is delivered into mixing column via the explosion-proof water back of special use respectively according to part ratio of joining of pure content weight, the edge garden inwall tangent with mixing the intensification tower rotated the formation eddy current naturally and evenly mixes with carbon dust when liquid high-pressure carbon dioxide and liquid high pressure hydrogen were rushed in and mixed the intensification tower, after the further heat temperature raising of fire-proof and explosion-proof electrical heat exchanger to the technological temperature in limited time nature supercharging enter in the reaction tower through intelligence control valve that can only one-way flow, the recyclable catalyst that recycles is delivered in the conveying pipeline that is between synthetic tower and the mixing intensification tower via pipe special and is mixed in the synthetic tower, be transported to from boiler the steam that loses temperature near reaction tower by be built in the steam pipe the jet electric heater by heat reach 480 degree by intellectuality control can only one-way flow solenoid control enter in the reaction tower, when high-temperature steam and carbon dust, carbon dioxide, hydrogen, when the mixture of catalyst reaches technological temperature and operation pressure, all can only one-way flow the intelligent electromagnetic switch close automatically by the intelligence control, coal dust, carbon dioxide, it is hydrogen oil that the lasting phase transformation of hydrogen generation becomes dimethyl ether, the dimethyl ether that generates imports the storage storehouse or directly divides can to advance paint storage tank by being serially connected in the cooling tower behind the catalyst filter haustorium in the conveying pipeline to flow out through intelligent control valve, has 85% molybdenum thing to be filtered haustorium by catalyst approximately and reclaims to insert after treatment and realize recycling in the catalyst tank.

Advantage of the present invention is to adopt the refrigeration working medium gas of value function to utilize multistage adiabatic expansion theory structure to absorb airborne " it is cold to dive " formations " value cryogenic environment " replacement freon refrigeration with the continuous cold liquid air that is phase-changed into of air respectively respectively, liquid air can directly become the transportation and energy, liquid air absorbs and to be converted into mechanical energy behind the potential energization and to become the Pneumatic electric generating energy, and the surplus electricity of Pneumatic electric generating electric power brine electrolysis or electron resonance on the spot splits Jie's water and is converted into hydrogen energy source; Obvious the present invention one can pay the electricity charge to obtain plantation and the ecological urban construction down of the cold power Project Realization anti-season film of the universal development of environmental protection freezer less, the 2nd, the stable potential of artificial acquisition replaces unsettled wind resource and the ripe wind generating technology of utilization is popularized artificial wind power generating, and the 3rd, can conveniently popularize and obtain solid hydrogen or low-cost non-renewable energy resources so the decrement discharge CO of replacing of hydrogen wet goods hydrogen energy source that makes things convenient for logistics and convenient use ₂Stop global warming, the 4th, but resource type treating CO ₂Make CO ₂Become cheap synthetic hydrogen oil raw material, the 5th, the air-powered car that can be China's initiative is popularized the liquefied air energy that provides cheap, the pulling Chinese Automobile Industry ' obtains opportunity to develop with the environment-friendly advantage of " afford, afford to use, zero-emission ", and the 6th, but conservation of power net cost of erection is realized electric power increase-volume or the convenient blind electricity district electric power of realizing and is popularized; The present invention can realize " potential " that cheapness utilizes environment-friendly high-efficiency new prospect of starting sustainable development of producing with regard to cold energy, automobile power energy, electric energy and solid hydrogen or the novel hydrogen energy source of hydrogen wet goods in a word.

Accompanying drawing and supplementary notes:

Fig. 1 is the principle schematic of manufacture method of the present invention; It also is Figure of abstract;

Fig. 2 is the level Four interlock CO of ammonia refrigeration power-assist ₂Refrigeration cold amplification method and principle schematic;

Fig. 3 is the deep cooling principle schematic of the different refrigeration working medium level Four interlock of the employing refrigeration cold amplification method of silks refrigeration power-assist in the fluorine;

Fig. 4 is the supplementing structure schematic diagram of Fig. 2;

Fig. 5 is the supplementing structure schematic diagram of Fig. 3;

Fig. 6 is efficient ammonia refrigeration method principle schematic;

Fig. 7 is applied to use CO for freezer ₂For the film of gas fertilizer is planted the cool principle schematic diagram down;

Fig. 8 is applied to the method and the principle schematic of ecological residence refrigeration for freezer;

Fig. 9 produces the packaging process schematic diagram of air car with the liquefied air energy; It also is the method schematic diagram that solid hydrogen is produced in pressurization;

Figure 10 realizes the method principle schematic of natural energy generating for the deep cooling storehouse;

Figure 11 is electric Jie's water hydrogen production process principle schematic;

Figure 12 is the method principle schematic of electron resonance water-splitting hydrogen production;

Figure 13 fills the hydrogen methods schematic diagram for solid hydrogen paint storage tank;

Figure 14 is the process schematic diagram of synthetic hydrogen oil;

Figure 15 is for producing the jet electroheat member structural representation of superheated steam; It also is the structural representation of the hollow electric heating isothermal body in the solid hydrogen paint storage tank;

Fig. 1 has provided three of under freezer disjunctors, and structure of the present invention and the deep cooling in deep cooling storehouse produce the gas energy step by step, gas can change into electric energy, electric energy hydrogen manufacturing and utilize the Method And Principle of ice water circulation supply user cold energy, 1 is freezer, 2 is the deep cooling storehouse of disjunctor, 3 is adiabatic expansion technology refrigeration equipment, 4 have the phase transformation coil pipe of compressed pneumatic pump 5 for tandem connection, phase transformation coil pipe 4 coils respectively each deep cooling storehouse 2 of deep cooling step by step of putting by disjunctor, 6 are the preposition air inlet that air cleaning filter is arranged of compressed pneumatic pump 5, 7 is the liquefied air storage tank, cold air in freezer 1 through the air inlet 6 of front compressed pneumatic pump 5 pump in cold phase transformation coil pipe 4 step by step cooling liquefaction in the deep cooling storehouse by after in compression pump 5

suction storage tanks

7, 8 is adiabatic transporting liquefied air pipe, 9 is intelligent control valve, 10 divide filling chamber for liquefied air, 11 larger storage tanks for liquefied air absorption atural beat, 12 is the strength power generation room, 13 expression freezer heat insulation layers and the heat insulation layer that is embedded in the deep cooling storehouse in

soil

38, 37 expression ground, 14 is the hydrogen making room of brine electrolysis or electron resonance fission water, 15 is the circulating water cooling coil pipe, 16 for the cold water pipe of tape input water pump 18, heat insulation layer is arranged outside

cold water pipe

16, 17 are the frozen water efferent duct with heat insulation layer, 18 expression output water pumps or input water pump, the 19 cold power users of expression, 37 expression ground, 38 expression subsurfaces, disjunctor deep cooling freezer 2 more than at least two is in close proximity to freezer 1, its optimum position is to be placed in the basement of freezer 1 to become " Ku Xiaku ", or the deep cooling storehouse 2 of disjunctor is placed in freezer 1 and becomes " library of libraries ", Cryogenic air in freezer 1 pumps into through gasing pump 5 that the disjunctor deep cooling storehouse 2 of a deep cooling of the cold phase transformation coil pipe 4 inherent ratios of air is interior to be followed into cooling and reach or approach the liquefaction critical-temperature along coil pipe 4, in liquefied air, the critical-temperature of oxygen is-183 ℃, the critical-temperature of nitrogen is-196 ℃, its critical-temperature is more approaching, compression pump 5 pressurizations through being in phase transformation coil pipe 4 tail ends, the oxygen that enters cryogenic almost can be synchronizeed to be liquefied with nitrogen and is pressed in liquefied air storage tank 7, liquefied air enters respectively liquefied air through three-way intelligent Self controlling valve 9 and divides filling chamber 10 to be poured into user's steel cylinder or enter the interior strength power generation room 12 that enters of gas larger storage tank 11 after absorbing solar thermal energy and geothermal energy energization and be used to generating, electric energy in brine electrolysis or electron resonance cracking water hydrogen making room 14 for the manufacture of hydrogen and oxygen, freezer 1 except as cold fresh-keeping, Yu Leng output continues cooling to cold power user, method is under the directional push of a plurality of water pumps, cold water to be divided frozen water to be input into cold power user and to return freezer via the 16 circulation water deliverys of cold water carrier pipe and lowered the temperature to the function of the lasting cooling of cold power user again via frozen water efferent duct 17 for frozen water along 15 cooling of frozen water coil pipe, this cooling is carried to divide and is used the solution of therrmodynamic system pipeline season, in the present invention, the directed delivery pump power consumption of the transfer delivery pump electricity consumption of refrigeration working medium and fluid is less, all can be from few part of the electric power of producing voluntarily, be not subjected to the mains supply conditionality, therefore the present invention can be in the non-Electric region performance for electrical dominance, Fig. 2 has provided the refrigeration target at the ground freezer embodiment more than-50 ℃, has adopted the four levels of linkages CO of ammonia refrigeration power-assist₂Refrigeration cold amplification method and principle, 20 is ammonia machine, chain-dotted line district 21 has represented one-level CO₂Refrigeration and cold enlarger, chain-dotted line district 21 and each rear class CO that is connected and links₂Refrigeration cold enlarger district and use the principle in other gas adiabatic expansion refrigeration enlarger district consistent, 22 be adiabatic housing, and 23 be the adiabatic expansion chamber, and 24 is adiabatic expansion generation mouth, and 25 is liquid CO₂Delivery outlet, 26 is liquid CO₂The working medium shifting pump, 27 is liquid CO₂Input port, 28 is adiabatic liquid refrigeration working medium carrier pipe example CO₂Carrier pipe, 29 expression liquid refrigeration working medium example CO ₂39 are liquid refrigeration working medium storage chamber, 30 is choke valve, 31 are gasificated into the freezing by change of state generator of middle concentration refrigeration working medium for the high concentration refrigeration working medium, the 32 high concentration refrigeration working medium gas delivery ports for liquid refrigeration working

medium storage chamber

39,33 is the efficient loss of heat pipe of

ammonia machine

20, and 34 gasifications of the ammoniacal liquor for ammonia machine 20 deepen refrigerating generator mutually; Fig. 3 has provided the difference classification of deep cooling storehouse and has used the Method And Principle as the dark refrigeration working medium adiabatic expansion refrigeration of environmental protection and the amplification of cold deep cooling such as compound different alkane, compound lithium bromide, oxygen, nitrogen, 35 are environmental protection small-power compression refigerating machine, 36 are the refrigerating generator of environmental protection compression refigerating machine 35, and the expression of 31 in Fig. 3 critical-temperature is lower than CO₂The cryogenic refrigeration working medium refrigeration cold-patch of critical-temperature is repaid source; Fig. 3 has provided cryogenic refrigeration and dark refrigeration amplification principle, all gas all has adiabatic expansion and produces the cold ability of diving, the selected refrigeration working medium gas of refrigeration at different levels is that its critical-temperature must be relative approaching with the absolute value of the temperature difference of refrigerating environment temperature, the example ammonia gas has relatively high critical-temperature under different pressure, therefore the most applicable chopped-off head refrigeration cold-patch of doing is repaid the refrigeration working medium in source, CO₂the critical-temperature of gas is-62 ℃, therefore freezer or deep cooling storehouse secondary adiabatic expansion refrigeration working medium more than the most applicable work-50 ℃, in like manner, compound different alkane is applicable to the further rear class adiabatic expansion refrigeration working medium in the deep cooling storehouse of appropriateness cooling of environment below-50 ℃, oxygen is applicable to approach the final stage adiabatic expansion refrigeration working medium in deep cooling storehouse more than-185 ℃, have the ability to make airborne oxygen cryogenic liquefying, the critical-temperature that makes airborne nitrogen approach the liquefaction critical-temperature or improve nitrogen in pressurized environment makes easy liquefaction, when the oxygen that has liquefied or the nitrogen that closes on the oxygen of liquefaction and close on liquefaction obtain the compression pressurization, all can be phased-changed in advance liquid air, the present invention utilizes this principle, can only consume less compressed air machine energy, be compressed into liquid air and store up in liquefied air storage tank 7 being in cryogenic air in cold phase transformation coil pipe 4 in deep cooling storehouse, can find out adiabatic expansion refrigeration of the present invention and cold amplification principle from chain-dotted line district 21: the liquid refrigeration working medium reserves in refrigeration machine refrigeration working medium storages at different levels chamber 39 are conventional more than 1.2 times of working medium of refrigeration machine refrigeration, high concentration refrigeration working medium gas flow becomes the heat energy in middle concentration refrigeration working medium GAS ABSORPTION refrigerating generator 31 ambient air and makes cooling refrigeration after refrigerating generator 31, middle concentration refrigeration working medium will become low concentration refrigeration working medium gas while continuing to flow through choke valve 30 and form high speed refrigeration working medium air-flow and scurry out at adiabatic expansion mouth 24 places and adiabatic expansion occurs produce deep cooling and reach below the critical-temperature of this refrigeration working medium and make this refrigeration working medium gas cold be phase-changed into liquid refrigerant to fall into the bottom of adiabatic expansion chamber 23, working medium delivery pump 26 in time enters liquid refrigeration working medium liquid refrigeration working medium storage chamber 39 from liquid refrigeration working medium input port 27 through adiabatic conducting tube 28 from liquid refrigeration working medium delivery outlet 25, the form that obvious refrigeration working medium is transferred to from storage chamber 23 in storage chamber 29 is liquid to liquid state, its delivered volume is than being " 1 to 1 ", and conventional refrigeration working medium to become the liquid gas-liquid delivery ratios that shift into the storage chamber in 39 from the gaseous compressed of storage chamber 23 be about " 104 to 1 ", the refrigeration working medium of the heavy amount such as obvious this method shifts power consumption and only needs 1/104 of compression refrigeration method, realize that relatively refrigerating capacity amplified 103 times, keep in adiabatic expansion chamber 23 and have that to recur the prerequisite that adiabatic expansion produces liquid refrigeration working medium be to have a cold compensator in adiabatic expansion chamber 23, freezer cold compensator 34 is from ammonia machine 20, deep cooling storehouse cold compensator 36 is from environmental protection small-power compression refigerating machine 35, and cold compensator 31 is from rear class adiabatic expansion refrigerating capacity enlarger, the cold of every grade of refrigeration cold amplification mechanism cold-peace " amplification " mainly is consumed in the adiabatic expansion chamber 23 of rear class adiabatic expansion refrigeration cold amplifier, comprise being consumed in this grade refrigeration cold amplifier and keep refrigeration working medium circulation and can continue to carry out the cold power function of adiabatic expansion and supplement operating cold scattering loss, the cold that amplifies nearly a hundred times of using only has 10% cold that amplifies as adiabatic expansion rear class refrigeration cold to compensate, multistage adiabatic expansion refrigeration cold enlarger decuples the ability that the cold of prime cold compensation source cold enters next stage adiabatic expansion refrigeration cold enlarger with regard to having every grade of acquisition, Fig. 2 and level Four adiabatic expansion shown in Figure 3 refrigeration cold amplify conjuncted being in cold that the refrigeration generating source 31 in freezer or deep cooling storehouse can emit and should reaching elementary cold-patch and repay source 34 or elementary cold-patch and repay thousands of times of source 36 colds of fourth stage refrigeration cold enlarger that be equipped in, the present invention observes Energy conservation law, the reason that cold is exaggerated is that refrigeration working medium has had the chance that continuous thermal insulating expands to absorb airborne " diving cold " in the present invention, the rear class refrigeration amplification quantity of multistage adiabatic expansion refrigeration cold amplifier can be fed back the elementary cold-patch of a small amount of cold replacement and repays source and can realize larger cold amplification effect, Fig. 2 and Fig. 3 have given expression to this rear class cold-patch and have repaid source structure 31, cold amplification efficiency of the present invention depends on choke valve, the adiabatic efficiency of cold compensation and equipment, every grade of refrigeration cold amplification efficiency of multistage adiabatic expansion refrigeration machine can follow into continuation with " one-level amplification one-level " form greater than ten times of amplifying powers, the progression of multistage amplification cold is unrestricted, therefore can tackle freezer or the deep cooling storehouse of any requirement and set the multistage adiabatic expansion refrigeration cold amplification combination device that meets value function, the best disjunctor in related deep cooling storehouse is built in the interior basement of freezer or is built in freezer and becomes library of libraries, to pursue maximum freezer utilization ratio, refrigeration working medium quantity in the built-in more conventional compression-type refrigeration device of adiabatic expansion refrigeration working medium quantity of apparatus of the present invention is many more than 1.2 times, more cryogenic temperature when in therefore forming before choke valve, concentration adiabatic expansion gas makes the refrigeration working medium gas flow rate of altering choke valve reach this refrigeration working medium adiabatic expansion, can make this refrigeration working medium reach the liquefaction of phase transformation below its critical-temperature completely, can realize adopting the compression pump reduction transfer refrigeration working medium power consumption that liquid shifting pump replaces becomes gas compression liquid, realize enlarging refrigerating efficiency adiabatic expansion refrigeration purpose nearly a hundred times, Fig. 3 has provided the four levels of linkages adiabatic expansion refrigeration cold enlarger operation principle that adopts corresponding cold-patch to repay the refrigeration power-assist, for pursuing value function, must choose the refrigeration working medium of different critical temperature and realize refrigeration by seat step by step, deep cooling and cryogenic environment more, the corresponding critical-temperature near this storehouse adiabatic expansion refrigeration working medium used of the cryogenic environment temperature in every grade every deep cooling storehouse, related many deep cooling storehouse disjunctors and building, repay source 36 no matter adopt which kind of cold-patch, cold-patch is repaid source 36 and is all only needed interim performance cold compensate function when this multi-stage refrigerating cold amplifying device starting, repay source 31 work at the rear cold-patch that is changeable employing rear class amplification cold distributes, fill the cold that part utilizes rear class to amplify, not only economize on electricity, and cold compensation rate foot, Fig. 4 has provided freezer embodiment ammonia refrigeration cold-patch and has repaid the level Four CO of source starting₂The cycle installation structure of refrigeration cold enlarger, wherein the ammonia deep cooling compensates source 34 and from the cold-patch of final stage refrigerator, repays source 31 and is in together in the one-level adiabatic expansion chamber of freezer 1; Fig. 5 has provided deep cooling storehouse embodiment and has freezed the circulation of level Four adiabatic expansion refrigeration cold enlarger that cold-patch repays the source starting by assembling structure, and the refrigeration compensation source 31 of the final stage refrigerator that wherein joins from annular is repaid source 36 with cold-patch and is in together in the one-level adiabatic expansion chamber in corresponding deep cooling storehouse 2; Can annular be connected into mutually cramped construction from the visible adiabatic expansion refrigeration cold enlargers 21 at different levels of Fig. 4 Fig. 5; Fig. 6 has provided high-efficiency ammonia refrigeration machine operation principle, and 40 is the ammonia spirit paint storage tank, and 41 for circulating the pipeline of ammonia, 42 are the fused coil pipe of ammoniacal liquor, 43 are electrical heating ammoniacal liquor evaporating region, and 44 is ammoniacal liquor rectifier section, and 45 is the ammoniacal liquor inlet of ammoniacal liquor paint storage tank 40,46 is the export mouth of hydrogen conduit 47,48 is the introducing port of hydrogen conduit 47, and 49 is electric heating element, and 50 and 51 is a pair of power safety interface on electric heating element 49,52 is heat-insulating material, and 53 are the fixing protection cylinder of heat-insulating material; the high-efficiency ammonia refrigeration principle adopts the high-efficiency absorption principle, ammonia spirit becomes the ammoniacal liquor mixed vapour in 43 heat absorptions of electric heating evaporation section and rises, water vapour in rectifying section 44 place's ammoniacal liquor mixed vapours congeals under water droplet nature and falls back to evaporating region 43, the high temperature ammonia of dehydration continues rising and enters the preposition pipeline of refrigeration coil 34, the efficient loss of heat pipe 33 of " L " shape that heat energy in ammoniacal liquor is adjacent to mutually by the preposition pipeline with refrigeration coil 34 siphons away heat energy makes the ammoniacal liquor phase transformation of lowering the temperature at a high speed become high pressure aqua ammonia, the high pressure aqua ammonia deep cooling that the heat energy in absorption coil refrigerator 34 ambient air produces below-62 ℃ refrigerator 34 when natural phase transformation is restored to ammonia gas in coil pipe refrigerator 34, ammoniacal liquor is in water-fast companion puts under the impetus of hydrogen (or nitrogen) directed movement fused coil pipe 42 enters ammonia spirit paint storage tank 40 through ammoniacal liquor, make and be evaporated into again ammoniacal liquor mixed vapour periodic duty refrigeration in waiting evaporimeter pipeline section 43 at liquid level place, water-fast hydrogen directly rises to hydrogen introducing port 48 through hydrogen conduit 47 from hydrogen outlet 46 and enters the interior promotion ammonia of refrigerator 34 phase transformation directed movement and enter for 42 times ammoniacal liquor paint storage tank 40 via coil pipe, hydrogen plays from local orientation's circular flow of 40 → 46 → 47 → 48 → 34 → 41 → 42 → 40 the ammonia phase transformation directed movement effect that promotes, in freezer 1 of the present invention from final stage CO₂The local refrigerator pipes 31 that refrigeration cold enlarger distributes is combined closely with " L " shape loss of heat pipe 33, " L " shape loss of heat pipe is a kind of high-efficiency heat conduction rod, can the heat energy in ammoniacal liquor be siphoned away with the loss of heat ability nearly a hundred times that surpasses common ammonia refrigeration heat loss through radiation mode radiating efficiency and at " L " shape heat conduction loss of heat pipe 33 and the coenosarc structure place moment elimination heat energy of refrigerator pipes 31, reach efficient loss of heat purpose, therefore this conjuncted structure utilizes final stage CO₂The high-efficiency absorption ammonia machine that after the refrigeration cold amplifies, the shunting cold energy is used for the loss of heat structure can obtain subzero deep cooling cold-patch below 62 ℃ and repay source, need not to use CO again₂Refrigeration cold amplification cold-patch is repaid the source 31 elementary cold-patches of replacement high-efficiency absorption ammonia refrigeration and is repaid source 34 and can reduce manufacture difficulty and manufacturing cost, and another purposes of high-efficiency ammonia refrigeration machine is to utilize the frozen water pipe loss of heat structure that enters cold power user conveniently to obtain the small ammonia cryogenic refrigerator and environmental protection and energy saving replacement fluorine Lyons refrigerator; Fig. 7 has provided under cold power user's film off-season cultivation equipment embodiment method, by the weather-proof air cushion plastic film of planting shed frame, good transmittance under cold scattering water pipe, film, is formed and can be held CO₂Space environment under the fertile film with holding temperature of gas, 54 are the cold scattering water pipe, and 55 is planting shed frame under film, and 56 is the weather-proof air cushion plastic film of good transmittance, and 57 for reinforcing the bar that presses solidly of air cushion plastic film 56, and 58 is Nutrition Soil or hydroponics dish, and 59 for can hold CO₂Space environment under the film of gas fertilizer, from freezer under the frozen water of circulation temperature lowering is flowed through film the cold scattering water pipe 54 that has the dropper function concurrently in planting shed, become the canopy film planting environment cooling source of cheap cooling of heat phase, can realize planting in the heat phase dish or the fresh flower in spring; In like manner, utilize the artificial Pneumatic electric generating electric power of the present invention can the phase in severe winter on the spot electric heating solve planting environment under film and heat up, dish and the fresh flower in spring are planted in realization in severe winter, under universal low this film of agriculture, off-season cultivation not only can improve plough volume increase and anti-season of dish and rises in value, and can hold firmly fill with into CO₂making becomes gas fertilizer and transforms into carbohydrate nutrition crop and oxygen, the association realization＜Kyoto Protocol when realizing sand control, new countryside construction 〉, Fig. 8 has provided embodiment and the method for the cold power supply equipment of cold power user's house, 60 is the fan coil refrigeration air-conditioner, 61 are the outlet of air-conditioning cold wind, 62 is blower fan frozen water coil pipe cold scattering source, 63 is high-efficiency absorption ammonia refrigeration refrigerator, 64 is the cold fresh-keeping built-in wardrobe of rearmounted frozen water coil pipe, 65 is the frozen water distributive pipe, frozen water enters residential quarter through the frozen water carrier pipe 17 with heat-insulating protective layer and enters house from distributive pipe 65 under 18 effects of output water pump, at first frozen water distributive pipe 65 can make high-efficiency ammonia cooling absorption refrigerator can produce the freezing function of deep cooling tool with loss of heat pipe 33 laminatings of high-efficiency ammonia refrigerator 63, the related high-efficiency ammonia cooling absorption refrigerator of the present invention can more economize on electricity than compression fluorine Lyons refrigerator, quiet, environmental protection and low cost, the frozen water blower fan frozen water coil air conditioner 60 of flowing through, blower fan is sent the cold of frozen water in coil pipe to house with convection type, obviously energy-conservation and quiet than compression fluorine Lyons air-conditioning, can parallel connection flow through frozen water coil pipe in the cold antistaling cabinet 64 of Aumbry type of rearmounted frozen water coil pipe of frozen water becomes the cold fresh-keeping built-in wardrobe of not power consumption, CO of the present invention₂adiabatic expansion technology refrigeration cold amplifies that electricity consumption that freezer 1 amplifies due to refrigeration and refrigerating capacity is low ignores to being considered as, therefore needn't limit the refrigeration work time, can be in freezer 1 continuous cooling work savings cold and with the water-cycling mode cold-storage cold that electric cost is extremely low, send cold power user to, be reprocessed into frozen water the water that loses cold power is drawn back freezer 1 through water return pipeline 16 under 18 effects of backwater suction pump in and can repeat to input cold power user, Fig. 9 has provided the method for filling liquefied air, 66 is the gas transmission liquid house steward that intelligent valve 10 is controlled, the isocon 67 that upper horizontalization is capable, 68 for observing the air gauge of the interior liquefied air pressure of transfusion house steward 66, 69 is minute control manually-operated gate on isocon 67 and liquefied air tank turnover tracheae, 70 expression liquefied air tanks, after the liquefied air tank 70 of zero load is spun respectively and is combined on isocon 67, open again intelligent control valve 10 after opening respectively manually-operated gate 69, air gauge can show in the liquefied air tank whether reach full irrigation, intelligent control valve 10 also can be closed automatically when the liquefied air tank reaches the full irrigation standard, then shut manually-operated gate 69, rotating separation liquefied air tank 70, filling work has just been accused, Figure 10 has provided the operation principle of the artificial wind-power electricity generation of natural energy, 71 is the rotating wind wheel that connects with rotating shaft 72, 73 is the wind turbine housing, 74 is the rearmounted exhaust outlet of wind turbine housing, 75 are the rotating shaft mounting, 76 is change gear box, 77 is gas driven generator, 131 are equipped with the underground heat heat pipe of parallel fin 132 for the upper end disjunctor, underground heat heat pipe 131 is that a kind of built-in parallel inorganic hollow fibers tube bank and employing peroxidating metal are the metal copper pipe of heat-conducting medium, overhead nearer area sufficiently long heat-conducting copper pipe 131 is inserted the underground heat energy cleanly that can obtain continually enter liquefied air at geothermal energy resources, its upper end that is equipped with the stainless copper sheet 132 of disjunctor heat radiation is in liquefied air larger storage tank 11, liquefied air absorbs underground heat and adds that becoming the high-pressure liquefaction air via increase kinetic energy after the metal ladle bowl absorption solar energy of larger storage tank 11 is controlled and quantitatively emitted by intelligent control valve 10, the rotary wind impeller 71 that phase transformation immediately forms in high-speed wind power impact casing 73 in wind conveying pipe 66 makes rotation, the rotating shaft 72 of interlock drives change gear box 76 work and pulls gas driven generator 77 generatings, the artificial gas driven generator 77 of this comprehensive utilization natural energy can select ripe wind-driven generator slightly through the technological transformation coupling, to use, this manpower wind power generator factory utilizes cold energy to produce recycling safety and inexhaustible underground heat and the artificial wind-force kinetic energy power generation of solar energy increase after liquefied air, can not be subjected to the universal foundation of environmental limitations, the electric power of producing is except a small amount of using by oneself, a large amount of electric power can replace the thermal power plant electric power that uses non-renewable energy resources and replace nuclear plant meets the need of market, and can also not rely on electrical network and suit measures to local conditions to meet the electricity needs in blind electricity district or short of electricity district, Figure 11 has provided the Method And Principle that utilizes the remaining electric Jie's water preparing hydrogen energy of Pneumatic electric generating, 78 expression unipolarity water electrolysers, 79 expression battery lead plates, 80 expression barrier films, 81 expression division boards, 82 expression water, wherein added alkaline electrolyte, 83 expression water inlet pipes, the direct current electrode that 84 expressions are connected with battery lead plate, 85 and 86 represent respectively hydrogen and oxygen output tube, hydrogen produces from negative pole, oxygen produces from positive pole, water electrolysis equipment has the standardization homemade goods, its operating pressure is at 0.8～4.0Mpa, large-scale standardization electrolysis hydrogen production bioreactor output can reach 350M³/ h, electrolytic efficiency reaches 80%, Figure 12 has provided the Method And Principle of electron resonance water-splitting hydrogen production, 87 expression hollow ring resonators, when frequency of utilization is the above alternating current of 600Hz, be in water 82 in the water pipe at resonator 87 centers by the mist 88 of resonance splitting Cheng Qing and oxygen, gas compression pump 5 is pressed into hydrogen and oxygen gas mixture 88 in special-purpose basin 89 and makes into liquefaction, liquid hydrogen light specific gravity and float over the first half of basin 89, liquid oxygen is than the great Lower Half that sinks to basin 89, the separating tube 85 that is in basin 89 tops distributes liquid hydrogen, the separating tube 86 that is in basin 89 bottoms distributes liquid oxygen, 90 expression valve switch, the hydrogen-oxygen that 91 expressions are floated divides liquid level, 92 is pressure pipe, 93 are in outlet in basin 89 for pressure pipe, the efficiency of this electron resonance water-splitting hydrogen production technology can reach more than 90%, Figure 13 has provided hydrogen-burning automobile and has filled the hydrogen principle with solid hydrogen paint storage tank, 94 is liquid hydrogen tank, 95 is the small gas compression pump, 96 are solid hydrogen paint storage tank, it is built-in with hollow isothermal electric heating element, the jet electroheat member structure that hollow isothermal electrothermal structure can be shown in Figure 15, and both are close with production technology except the different external structures of component parameters, the 97 electroheat member electrode terminals for solid hydrogen paint storage tank, 98 are the fixedly mouth of pipe that spins with seal washer, filling hydrogen methods is, the wireway that the turnover gas tube orifice of solid hydrogen paint storage tank 96 is screwed in the gas compression pump 95 that is connected with the liquid hydrogen paint storage tank is fixedly on the mouth of pipe 98, when valve 69 is outwarded winding, the high pressure liquid hydrogen pours solid hydrogen paint storage tank, Gu the magnesium alloy powder in the hydrogen paint storage tank generates the i.e. hydrogen admittedly of hydride alloy magnesium being forced under the above state of 3Mpa the hydrogen abstraction reaction of can satisfying, gas compression pump 95 plays pressurization and promotes the effect of alloys magnesium hydrogen synthetic reaction, when Gu the heating in hydrogen paint storage tank 96 uses automobile storage battery electric constant-temp electrical heating to 250 degree to spend to 290, Gu hydrogen reduction reaction releasing hydrogen gas, Gu the hydrogen hydrogen content can reach six times of consubstantiality hydrops hydrogen amount, do not let out hydrogen under normal temperature, ignition and blasting hydrogen, can not recycle this device and be filled with the solid hydrogen cycle charge discharge hydrogen of hydrogen reaction generation again after hydrogen drains, it is the process of hydrogen oil that Figure 14 has provided dimethyl ether synthesis, 99 represent the HTHP synthetic tower, 100 represent the pipe special of the built-in flames of anger without jet electroheat member 101 Electrothermic steams of inductance work, 102 represent the carbon dioxide of the built-in flames of anger without the electrical heat exchanger 103 of inductance work, hydrogen and carbon mix the intensification tower, related electrical heat exchanger 103 use double dot dash line districts represent, 104 represent the variable-voltage power supply device, 105 represent the catalyst tank, 106 is the catalyst propulsion tube, catalyst propulsion tube 106 communicates with the hydrogen oil efferent duct 114 between synthetic tower 99 and mixing intensification tower 102, 107 is catalyst filtered and recycled device, 108 is the explosion-proof pressure display list, 109 be can only one-way flow intelligence control electromagnetic valve, 110 are connected and fixed flange for pipeline, 111 is the coal dust input pipe, 112 is the carbon dioxide input pipe, 113 is the hydrogen input pipe, carbon dioxide input pipe 112 becomes interior cut to be connected with hydrogen input pipe 113 and the inwall garden face that mixes intensification tower 102, liquid high-pressure carbon dioxide and liquid high pressure hydrogen are rushed in while mixing intensification tower 102 evenly to be mixed along the inwall natural rotation that mixes

intensification tower

102, 114 for hydrogen oil be the dimethyl ether efferent duct, 115 is the Intellect electrical switch case, 116 expression power line or power supply closing lines, 117 is sense line, 118 is sensing head, chain-dotted line district 119 expression hydrogen oil cooling towers, the hydrogen oil cooling but adopts two step process for cooling, first by cold water, absorb heat and make into boiling water importing boiler, waste heat can be utilized, the refrigeration of rear use carbon dioxide adiabatic expansion generation deep cooling and cold amplifying technique freezer make rear step hydrogen oil cooling, and but moment completes, two step process for cooling had not only improved heat utilization efficiency but also had shortened the production technology time and can greatly improve hydrogen oil production efficiency, the frock ground level of 120 expression professional standards, Figure 15 has provided the high-power safe jet electroheat member structure that produces superheated steam and overfire air, 121 is flat aluminum pipe, it is the contour Aluminum Hollow section bar with waiting wall thickness of uniform thickness, 122 is the stone paper electroheat member, it forms by clamping the stone paper electrothermic film element in two layers of

insulating trip

123, 124 for being combined in the even Electric radiant Heating Film on inorganic stone paper surface, 125 is the creep age distance on inorganic stone paper surface, the 126 high temperature resistant electrodes that form for being coated with the silver conductive adhesive heat ageing, 127 be in flat aluminum pipe 121 parallel equidistant from disjunctor the thin-walled sheet heat transfer muscle on

aluminium inwall

121, 128 is the sealing wire that between adjacent two flat aluminum pipe 121 sidewalls, mutual weldering connects, 129 expression jet heat steams heat passage 130 on put the electrode leading-out sheet of minor insulation layer, the structure ﹠processes of the electroheat member in this electroheat member and solid hydrogen paint storage tank is consistent, in sum, the mankind can utilize natural energy to be resource, ask for potential and replace fossil energy or replace expensive clean energy resource, meet the demand of the mankind to cold energy, electric energy, vapour energy and various hydrogen energy source, break away from the pernicious of the earth asked for, realize the fine harmonious coexistence of the mankind and the earth.

Embodiment of the present invention:

Embodiment of the present invention is " Cheap highly effective is produced the method and the equipment of clean energy resource " or " Cheap highly effective is produced the method and the equipment of eco-energy " or " cheapness is utilized the method for natural energy and used equipment " or " the cheap preparation method of multiple clean energy resource and application equipment ", sustainablely according to the present invention produce serial clean energy resource characteristics, embodiment of the present invention can be " sustainable method and the equipment of producing cold energy gas energy electric energy hydrogen energy source ", all can realize producing the characteristics of clean energy products according to using each stage of the present invention, embodiments of the present invention can also respectively be " adiabatic expansion refrigeration cold amplifies freezer and cold power engineering " or " the cheap preparation method and the equipment of liquefied air power source " or " cheapness is produced the method and the equipment of solid hydrogen energy source " or " cheapness is produced the method and the equipment of hydrogen oil " or " the cheap preparation method and the equipment of traffic clean energy resource ".

Claims

1, a kind of Cheap highly effective is produced the method and the equipment of clean energy resource, by multistage adiabatic expansion refrigeration cold enlarger, be close to the multistage deep cooling storehouse of freezer, the cold phase transformation coil pipe of air of band filter and compression pump, air accumulator, the artificial airflow generator, hydrogen making machine, Gu hydrogen or the synthetic equipment of hydrogen oil, can liquefied air shunting machine and cold power interchanger are formed, the deep cooling storehouse of at least two above phase disjunctors is under the freezer or in the freezer, the cold phase change disk pipe range of air range hadn wheel is put by colder deep cooling storehouse of a ratio and insert the liquefied air storage tank by compression pump in the coldest deep cooling storehouse, and the efferent duct of liquefied air storage tank is connected installation of liquefied air diversion cans or strength generator through intelligent Self controlling valve shunting; The refrigeration working medium that multistage adiabatic expansion refrigeration cold in the freezer of related ground amplifies in the equipment adopts CO ₂, cold compensation source is selected ammonia refrigeration device or iso-butane refrigerator and multistage CO for use ₂Refrigeration cold enlarger is formed conjuncted refrigeration equipment, the selected refrigeration working medium gas of refrigeration at different levels is that its critical-temperature is relative approaching with the absolute value of the temperature difference of refrigerating environment temperature, in last deep cooling storehouse of the most following or innermost layer, multistage adiabatic expansion refrigeration working medium adopts critical-temperature a little less than-196 ℃ environmental protection gas.

2, " Cheap highly effective is produced the method and the equipment of clean energy resource " as claimed in claim 1 related ammonia refrigeration device, it is characterized in that by the ammoniacal liquor basin, ammoniacal liquor circular flow siphunculus, ammonia spirit electric heating evaporation section on the ammoniacal liquor runner pipe, smart gold-plating device section and the cointegrate of being made up of with condenser section and refrigerator pipe or frozen water pipe respectively " L " type heat pipe and ammoniacal liquor fuse section to be formed, the lower end of " L " type heat pipe in the cointegrate is adjacent to into coenosarc with parallel ammonia condensing area under control section, the upper end of " L " type heat pipe is adjacent to into coenosarc with refrigerator pipe or frozen water pipe again, " L " type heat pipe that can be adjacent to mutually, refrigerator pipe or frozen water pipe and condenser pipe section all adopt the half-moon-shaped hollow and thin-walled metal tube of square or band side plane, pipe plane between the tube and tube abuts against each other into coenosarc, is full of parallel hollow inorganic fibre pipe and hot superconductive medium in " L " type heat pipe.

3, " Cheap highly effective is produced the method and the equipment of clean energy resource " as claimed in claim 1 related refrigeration cold amplifier, it is characterized in that a multistage connected structure refrigeration body, form by choke valve, adiabatic expansion chamber, cold compensator, refrigerant liquid delivery pump, refrigeration working medium and refrigeration working medium storage chamber; Be in that the adiabatic expansion of the chopped-off head refrigerator in freezer or the deep cooling storehouse is indoor to be equipped with two small-sized refrigerating colds compensation sources, one is the cold compensation source of independently freezing, and another back level refrigeration source from refrigeration cold amplifier distributes; Wherein the back level refrigeration cold amplifier of seat of honour freezer also on the cold compensation source that distributes parallel connection distribute another cold compensation source, its upper end with " L " type heat pipe of ammonia refrigeration device is adjacent to into the coenosarc structure.

4, " Cheap highly effective is produced the method and the equipment of clean energy resource " as claimed in claim 1 related can liquefied air shunting machine, it is characterized in that by preposition intelligent control valve and observe barometric transfusion house steward that liquefied air reaches full irrigation pressure, shunt woven hose, the liquefied air jar is formed, the shunting woven hose is the parallel connection structure, and the termination has to chew with the gas of liquefied air jar and can make things convenient for the closed salable hickey that spins.

5, " Cheap highly effective is produced the method and the equipment of clean energy resource " as claimed in claim 1 related gas driven generator, it is characterized in that forming by the appendix of the larger storage tank that absorbs natural energy, preposition intelligent control valve, fan blade, fan blade casing, rotating shaft mounting, gear-box, the gas driven generator of band rotating shaft, the insertion of underground heat heat pipe that is in central authorities in the larger storage tank is underground, it is equipped with the dispel the heat upper end of stainless copper sheet of disjunctor and is in the liquefied air, and the fan blade central rotating shaft stretches out the rotating shaft mounting and connects the rotating speed of controlling alternator shaft with change gear box.

6, " Cheap highly effective is produced the method and the equipment of clean energy resource " as claimed in claim 1 related cold power interchanger, it is characterized in that being equipped with the water-carriage system that the cold water inlet pipe of pulsating pump, the frozen water efferent duct inhaling cooling coil and be equipped with water-delivery pump are formed periodic duty, cold water inlet pipe and the cold power user of the parallel process of frozen water efferent duct by connection; Cold power user can be under the film off-season cultivation equipment, it is characterized in that being made up of the weather-proof air cushion plastic film of plantation canopy frame, good transmittance under cold scattering water pipe, the film holding CO ₂Gas is fertile and hold space environment under the film of cold or warm temperature, and the dropper cold scattering water pipe in the plantation canopy becomes the canopy film planting environment cooling source of cheap cooling under the frozen water of circulation cooling is flowed through film from freezer; Cold power user can be the dwelling house of central heating, frozen water is used the delivery pipeline and is entered the residential area through carrier pipe enter dwelling house from distributive pipe under output water pump effect, the frozen water distributive pipe is at first fitted with the loss of heat pipe of efficient ammonia refrigeration refrigerator and is made efficient ammonia refrigeration absorption refrigerator can produce freezing deep cooling, the frozen water blower fan frozen water coil pipe air-conditioning of flowing through, blower fan is sent the cold of frozen water in the coil pipe to the dwelling house cooling with convection type, and the cold fresh-keeping built-in wardrobe of not power consumption is formed in the frozen water frozen water coil pipe association that rear wall is equipped with in the cold antistaling cabinet of Aumbry type of frozen water coil pipe of also can in parallel flowing through.

7, " Cheap highly effective is produced the method and the equipment of clean energy resource " as claimed in claim 1 related electron resonance water-splitting hydrogen production machine, it is characterized in that splitting Jie's water device and the liquid gas diversion cans is formed by the electron resonance that is communicated with through gas compression pump, it is the hollow ring resonator that electron resonance splits Jie's water device, be in water in the water pipe at resonator center by the mist of resonance splitting Cheng Qing and oxygen, gas compression pump is pressed into hydrogen and oxygen gas mixture in the special-purpose basin and makes into liquefaction, and liquid gas shunting basin top and the bottom respectively have a shunting to chew.

8, " Cheap highly effective is produced the method and the equipment of clean energy resource " as claimed in claim 1 related solid hydrogen paint storage tank machine for adding hydrogen, it is characterized in that forming by liquid hydrogen paint storage tank, gas compression pump, solid hydrogen paint storage tank, compression pump is positioned on the withstand voltage wireway that connects solid hydrogen paint storage tank and liquid hydrogen paint storage tank, and solid hydrogen paint storage tank fills hydrogen also can be adopted liquefied air shunting can equipment to be connected in series compression pump hydrogen is filled in a plurality of hydrogen paint storage tank parallel connections admittedly simultaneously.

9, the synthetic equipment of " Cheap highly effective is produced the method and the equipment of clean energy resource " as claimed in claim 1 related hydrogen oil, it is characterized in that steam pipe by built-in safe jet electric heating heat booster, synthetic tower, coal dust, the mixing intensification tower of carbon dioxide and hydrogen, catalyst filtered and recycled device, cooling tower is formed, coal dust wherein, carbon dioxide input pipe and hydrogen input pipe that the mixing intensification tower of carbon dioxide and hydrogen is equipped with unidirectional defeated material intelligence control magnetic valve become interior cut syndeton with the inwall garden face that mixes the intensification tower, the recyclable catalyst that recycles is delivered in the conveying pipeline that is between synthetic tower and the mixing intensification tower via pipe special; The cross section that wherein safe excess temperature heats the jet electroheat member is a square and is made up of the jet hot hole road of massive parallel, four jiaos of jet electroheat member that the cross section is square are tangent and form the heat insulation side rooms of four obstructed steam of sealing along tube wall with steam pipe garden inwall, jet electric heating duct is made up of the flat aluminum pipe wall and the aluminium flake heat transfer muscle that clamp the high stone paper Electric radiant Heating Film parts of microballoon concentration in twos, the stone paper electroheat member is formed by clamping stone paper tin oxide electrothermic film element in two layers of insulating trip, stone paper electrothermic film element two sides is a pair of tin oxide face electric heating field boundary parallel and that power is close that evenly equates, the waist central authorities that a pair of common electrode is in stone paper tin oxide electrothermic film element make the electrothermic film element parallel connection on stone paper two sides, electrode and connect lead and be in the heat insulation side room enclosed environment that does not contact steam.