CN110325733A

CN110325733A - The method for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system

Info

Publication number: CN110325733A
Application number: CN201680090646.0A
Authority: CN
Inventors: 瓦列里·斯捷潘诺维奇·麦索特森科
Original assignee: Orie Technology Co Ltd
Current assignee: Orie Technology Co Ltd
Priority date: 2016-09-07
Filing date: 2016-09-07
Publication date: 2019-10-11
Also published as: WO2018046979A1; AU2016422298A1

Abstract

It include making dry channel of the atmosphere air-flow by pipeline using the method that atmospheric evaporation drive system generates electric power, wherein the air-flow is pre-chilled by contact surface dried side and evaporating liquid soaks the wet channel of pipeline.Air-flow is reintroduced to generate electric power by turbine from dry channel to wet channel, and directly contacts as control air with evaporation liquid.Control air is carried out the moisture wetting of spontaneous evaporation liquid.The advance that indirect heat exchange increases in wet channel from low altitude area to High aititude rises the temperature and water capacity of control air in flowing.Then, it heats and moist control air is discharged into atmosphere.Control air and/or evaporation liquid are before the wet channel for entering pipeline or by passing through heat by solar radiation during the wet channel of pipeline.

Description

The method for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system

Technical field

Present invention relates in general to atmosphere and solar energy (wind energy) to convert, and is in particular to driven using atmospheric evaporation The method that dynamic system generates electric power, cooling capacity and distilled water, to generate down current in dry channel, and it is raw in wet channel At ascending air.Turbine is located at the low altitude area in dry channel and turbogenerator, and the energy of moving air is converted into Electric power, cooling capacity and the distilled water of useful type.In addition, using solar radiation and/or the heat and other shapes of exhaust uptake gas The efficiency of these systems can be improved in the heat of formula.

Background technique

Atmosphere is made of air, and air is made of the molecule of such as gas with various such as nitrogen, hydrogen and oxygen.Sunlight is always It impinges upon on our atmosphere.But it unevenly heats earth surface, therefore atmosphere is warm in some places, and Elsewhere, atmosphere is cold.As air warms, its particle scatters.This makes air lighter or less dense, therefore It can rise.As air is cooling, it becomes heavier, or finer and close, and sinks.When warm air rises, from compared with cold-zone The air in domain flows into the air to replace heating.This process is known as convection current and air is caused to flow.The difference of earth surface adds Heat and the convection current thus generated are the reason of causing the wind on this celestial body, it is for determining the biotic environment of land and to people It is cleaned for class, is most important for the cheap energy.Wind energy is a kind of cleaning and reproducible power source, and in the world The fastest-rising energy.Caused by wind is the different heating as the sun to earth surface.Wind is the solar energy of indirect form, therefore It is " reproducible ", i.e., the sun is always supplementing it.But wind energy has the shortcomings that serious.The wind speed in any area be all it is variable, Therefore wind is intermittent power source.In quiet wind period, wind turbine cannot generate any electric power.Electricity needs was with one day In time and one week in day and change, therefore each power grid can generate superfluous production capacity.When wind comes, wind-force whirlpool is come from The electric power of wheel can be used for replacing thermal power plant, but when there is no wind, other power sources must make up the difference.Therefore, wind Power generator cannot be 365 days 1 year, operate within 24 hours one day.In typical wind power plant, time of the wind turbine in 65-80% Interior operation, but usually less than oepration at full load, because wind speed is not optimum level.Therefore, capacity coefficient 30-35%.Through Ji property also plays very big effect in terms of the capacity of wind-driven generator.The wind energy conversion system with higher capacity coefficient can be built Device, but it is uneconomic for doing so.Some researchers propose to create no disadvantages mentioned above using atmospheric evaporation drive system " artificial wind " energy system.It is well known that heated dry air will be with the decline of the speed of enhancing when passing through water-spraying control.It is this Phenomenon occasional occurs in nature, and has been learned and had recorded for a long time.Many inventors attempt using certainly The direct application of right power is to utilize the renewable energy in atmosphere, because the evaporation of water generates high wind by vertical pipe, and It can be used for driving turbine to generate electric power, and generate fresh water in the region for needing electric power and fresh water.

All existing patents and technology all use in vertical pipe, using traditional adiabatic evaporation cooling technique, in fact Nice and cool and wet air is now generated, temperature can cool down (in the ideal case) to wet-bulb temperature.Certainly, this nice and cool humidity Air there is bigger density than external warm and dry air, therefore tend to fall to the ground.But this density contrast Pressure drop (pressure difference between the entrance and exit of turbine) not on too small and turbine also very little.

The main drive of the electric power generated by atmospheric evaporation drive system is the extra pressure of air, with going out from turbine The less amount of external air pressure that mouth comes out is compared, and the extra pressure of air is directed into turbine.

The present invention can be recycled by Mai sotsenko and is implemented in combination with the device of dew point evaporative cooler.These are used for The device of dew point evaporative cooler is produced by Coolerado Inc. (city, Denver), they can be in trade mark " Coolerado Air It is commercially available under Conditioner ".The present invention provides a kind of economic and Environmental security method, for passing through Maisotsenko Circulation with tower ("Tower (Exergy Tower) ") collaboration generation electric power, cooling capacity and distilled water.

The present invention provides dramatically increase the air pressure for guiding turbine into and reduce the air pressure flowed out from turbine outlet A possibility that.In other words, the present invention provides by generating cold and dry air in dry channel and generating in wet channel Warmer and wet air is come a possibility that dramatically increasing pressure difference (or density contrast), the wherein cold and dry air temperature It can be cooled to dew-point temperature in the ideal case.For this purpose, the present invention is used with two sseparated dryings and is moistened logical The pipeline in road is used for the two air streams, for example, the structural equivalents of two vertical concentric cylinders (annular), and at them it Between be constantly present heat exchange mechanism.When the pressure drop on turbine increases, therefore increasing can as obtained by evaporation cooling It transmits electric power.

Proposed atmospheric evaporation drive system is in addition to realizing the disclosed side for generating electric power, cooling capacity and distilled water Except method, they are also cheaper, smaller and more easily produced and be placed on difference for different power capacities Place.

Therefore, all existing systems are not efficient because the density of down current air is small and turbine in Pressure drop also very little.

An embodiment of the invention is the spy by using heat simultaneously with solar radiation, flue gas or other heat sources Different regeneration evaporates cooling procedure to maximize obtainable only transportable electric power.

Another embodiment of the invention is to obtain cooling capacity and distilled water in one way for consumer, this is than all Existing method is more cost effective.Another embodiment of the invention is to create novel free convection cooling tower, not only It generates cold water (temperature can be cooled to dew-point temperature rather than the wet-bulb temperature of traditional cooling tower in the ideal case), and It can also power simultaneously.

High-temperature water helps to improve the efficiency of atmospheric evaporation drive system, and it is (in the ideal case, warm not only to generate cold water Degree can be cooled to dew-point temperature rather than the wet-bulb temperature of traditional cooling tower), but can also power simultaneously.In addition, it can be with Power consumption and the noise for significantly reducing proposed free convection cooling tower, with the traditional cooling tower phase for needing fan Than proposed free convection cooling tower does not need fan.

Another embodiment of the invention is that the structure of rising passway is used for using a small amount of material, to obtain conversion system The feasible cost efficiency of system.

Summary of the invention

The invention discloses a kind of methods for generating electric power, cooling capacity and distilled water using atmosphere and solar thermal energy converting system (“Tower "), down current is generated in dry channel using atmospheric evaporation drive system, is generated in wet channel and is risen gas Stream.The two channels are connected to the bottom of pipeline, turbogenerator are equipped at the bottom of pipeline, turbogenerator is used for will The energy of moving air is converted into electric power, cooling capacity and the distilled water of useful type.In addition, using solar radiation and/or exhaust cigarette The heat of road gas and the heat of other forms, can be improved the efficiency of these systems.

Detailed description of the invention

Fig. 1 is the perspective view of the atmospheric evaporation drive system according to embodiment of the present invention, for generating electric power, The system is the structural equivalents of two vertical concentric cylinders (annular).

Fig. 2 is the schematic of the atmospheric evaporation drive system according to embodiment of the present invention, for generating electric power Cross-sectional view.

Fig. 2 a is identical as Fig. 2, and still, according to embodiment of the present invention, this is used to generate the atmospheric evaporation of electric power Drive system includes the individual turbine 4 for outside air 7 and control air 8.

Fig. 3 be according to embodiment of the present invention, at the same generate the atmospheric evaporation driving of electric power and cold air The schematic cross sectional views of system.

Fig. 4 be according to embodiment of the present invention, at the same generate the atmospheric evaporation driving system of electric power and cold water The schematic cross sectional views of system.

Fig. 5 is the schematic cross sectional views of atmospheric evaporation drive system according to embodiment of the present invention, is used The heat of exhaust uptake gas generates electric power and/or cooling capacity simultaneously.

Fig. 6 is the atmospheric evaporation drive system with the inflatable tedge that pressurizes according to embodiment of the present invention Schematic cross sectional views.

Fig. 6 a is identical as Fig. 6, but the atmospheric evaporation drive system for being used to generate electric power includes inside wet channel 3 Surface 15, according to embodiment of the present invention, moistening channel 3, (such as ammonia or water-ammonia mix by low boiling point evaporation liquid 5 Object) replace water to soak.

Fig. 7 be according to embodiment of the present invention, at the same generate the atmospheric evaporation driving of electric power and distilled water The schematic cross sectional views of system.

Fig. 8 be according to embodiment of the present invention, at the same generate the atmospheric evaporation driving of electric power and distilled water The top view of system.

Fig. 9 is identical as Fig. 4, and still, according to embodiment of the present invention, this is used to generate electric power and cold water simultaneously Atmospheric evaporation drive system includes that multiple dry channels 2 and these channels of the extension element in wet channel 3 are located at a pipeline 1 In.

Figure 10 is identical as Fig. 9, but the atmospheric evaporation drive system also includes use according to embodiment of the present invention In the water jacket 41 for passing through heat by solar radiation water.

Figure 11 is identical as Fig. 7, but according to embodiment of the present invention, this is used to generate electric power and distilled water simultaneously Atmospheric evaporation drive system include multiple dry channels 2, the extension element in wet channel 3 and condensation channel 34 and for leading to Cross the water jacket 41 of heat by solar radiation saline solution.

Figure 12 is identical as Figure 10, but according to embodiment of the present invention, which includes point The solar water heater 45 set is opened rather than water jacket 41, for passing through heat by solar radiation water 5.

Figure 13 is identical as Fig. 2, but according to embodiment of the present invention, which also includes dry The absorber coatings in dry channel 2, such as limewash 46 extract carbon dioxide (or such as liquid drier out from outside air 7 46, vapor is extracted out from outside air 7).

Figure 14 is identical as Fig. 2, but according to embodiment of the present invention, which also includes row The absorber coatings in gas channel 30, such as limewash 46, the absorber coatings extract carbon dioxide out from exhaust uptake gas 31.

Figure 15 is identical as Figure 13, but according to embodiment of the present invention, which also includes Solar generator 47, for being recycled after weak absorbing agent 46 is by dry channel 2 to it.

Figure 16 is according to embodiment of the present invention, for the atmosphere of natural air adjusting and ventilation in building Evaporate drive system.

Figure 17 is identical as Figure 16, but according to embodiment of the present invention, this is used for the natural air in building It adjusts and the atmospheric evaporation drive system of ventilation includes solar generator 47, it is dry logical for passing through in weak liquid drier 46 It is recycled after road 2.

Figure 18 is the perspective of the atmospheric evaporation drive system according to embodiment of the present invention, for generating electric power Figure, wherein using special horizontal turbine 55, which goes back while realizing between outside air 7 and control air 8 Heat and mass exchange process.

Figure 19 is the perspective view of horizontal turbine 55, which includes being divided into a series of blades by axial groove 59 Disk.The turbine 55 realizes the heat and mass exchange process between outside air 7 and control air 8 simultaneously.Here: according to this hair A bright embodiment, 56 be regrown material, 57 be the entrance sector of regrown material 56,58 be regrown material 56 exhaust fan Area, 60 be the wet sector of regrown material 56,61 be injector, 5 be water.

Figure 20 is identical as Figure 18 and Figure 19, but according to one embodiment of the present invention, this is used to generate the atmosphere of electric power Evaporating drive system includes short dry channel 2.

Figure 21 is identical as Figure 20, but according to one embodiment of the present invention, which drives Dynamic system includes that turbine 4 and rotary regenerative heat and mass exchanger 62 are used as two individual devices.

Figure 22 is identical as Figure 20, but according to embodiment of the present invention, this is used to generate the atmospheric evaporation of electric power Drive system includes vertical turbine 55, wherein being soaked the wet water 5 of sector 60 using fluid box 65, the rotor of vertical turbine 55 It immerses in fluid box 65.

Figure 23 is the view of the atmospheric evaporation drive system according to embodiment of the present invention, for generating electric power, It includes turbines 4 and dew point indirect evaporative cooler 68 to be used as two individual devices.

Figure 23 a is identical as Figure 23, but according to embodiment of the present invention, this is used to generate the atmospheric evaporation of electric power Drive system is also that consumer produces distilled water, and it includes additional condenser 100 for this purpose.

Figure 24 be for and meanwhile generate electric power and distilled water 37 atmospheric evaporation drive system schematic cross sectional views, wherein Vacuum passage 73 is added with salt water 5, and salt water 5 is adjacent with condensation channel 74 and connect.In addition, an embodiment party according to the present invention Formula, the two channels 73 and 74 are all placed between dry channel 2 and wet channel 3.

Figure 25 be for and meanwhile generate electric power, cooling capacity and distilled water atmospheric evaporation drive system schematic cross sectional views, The system is inserted into underground.According to embodiment of the present invention, which is also thermoelectric generator, using underground heat or/and Soil heat source is to generate additional electric power, and it is using the air in earth atmosphere as working fluid application.

Figure 26 is the schematic cross sectional views for generating the atmospheric evaporation drive system of electric power, by the water directly from cloud It realizes.

Figure 27 shows the atmospheric evaporation driving for generating electric power according to embodiment of the present invention, disclosed System ("Tower ") and known energy tower (Energy Tower) and solar column (Solar Tower) process air line Figure.

Specific embodiment

Fig. 1 and system shown in Fig. 2 include: pipeline 1, for example, two vertical concentric cylinders 15 and 17 or vertical ring-shaped Structural equivalents are inside placed with the wet channel 3 (annular shape) of dry channel 2 (circle) and outside.Furthermore, it is possible to pass through Plate 15 (instead of two vertical concentric drums 15 and 17) creation dry channel 2 and wet channel 3, plate 15 are placed on pipeline 1 inside.But must exist always between the air-flow wet channel 3 passed through therebetween and dry channel 2 and pass through these plates The heat exchange mechanism that 15 surface (or surface of cylinder 15 and 17) carries out.The entrance 11 (referring to fig. 2) and atmosphere of dry channel 2 Connection, outlet 12 are connect with turbine 4, and the outlet of turbine 4 is connect with the entrance 13 in wet channel 3.The outlet 14 in wet channel 3 with Atmosphere connection.15 evaporated liquid 5 of surface wetting inside wet channel 3, such as water or saline solution evaporate 5 conduct of liquid The mobile film 16 of liquid moves from top to bottom along surface 15.Turbine 4 and generator 6 are located in low in dry channel 2 At height above sea level.It is heated by solar radiation (and heat of other forms) outer surface 17 in wet channel 3.In this case, lead to It is reasonable for crossing black coating or covering outer surface 17 using the material 10 for absorbing heat well from solar radiation.

For generate electric power system operation as shown in Fig. 2, its working principles are as follows: dry channel 2 entrance 11 Place provides outside air 7.The air 7 flows through dry channel 2, and the dry channel 2 and wet channel 3 carry out heat transferring contact, work Make air 8 and passes through wet channel 3.Therefore, it moistens channel 3 to be arranged to via surface 15 and 2 heat transferring contact of dry channel, this limit Corresponding dry channel 2 is made.The reverse side on the surface 15 in a part in wet channel 3 is steamed by using other methods availalbes The mobile film of lotion body 16 (such as water or saline solution) soaks.It surface 15 can be by materials such as wicking, plastics, metal, desiccant The composition of material or these materials is made.It should be appreciated that using term surface, but execute dry channel 2 and wet channel 3 Separation or by control air 8 from any structure of the isolated function of dry channel 2 be all suitable.Pass through the outer of dry channel 2 Portion's air 7 will be cooled to close to its dew-point temperature without changing its water capacity.Then, because cold air is heavier, cold air 7 passes through Dry channel 2 is from High aititude to low altitude area Doenward flow.7 density of cold air increases and sinks, and forms inverse stack effect.Cold is outer Portion's air 7 is flowed in dry channel 2 with high-speed, provides power for turbine 4, and is escaped into as control air 8 wet Channel 3, turbine 4 are connected to generator 6.

Because the temperature of cold outside air 7 after passing through dry channel 2 and next turbine 4 always lower than big first The temperature of gas, so it includes cooling capacity qo.This cooling capacity qo is advantageously possible for the cold source as consumer.For example, Using the air mediate contact of this cold outside air 7 and the air-conditioning system of consumer in the case where no consumption energy The cooling air is reasonable.Therefore, electric power (electricity) not only can be generated in the present invention, but also can be generated cooling capacity qo's Byproduct, for example, being used for air-conditioning system.

With for example for the air mediate contact of the air-conditioning system of consumer after, outside air 7 is heated.

Hereafter (referring to fig. 2), it is directed into wet channel 3 as this heating air of control air 8, it is logical there It crosses wet channel 3 and will rise from low altitude area and flow to High aititude.It is contacted with moist surface 15, such as evaporated liquid 16 is (such as Water or saline solution) wetting wicking plastics or capillary porous material.When control air 8 passes through along wet channel 3, its quilt Heating, wetting and its density get lower than the density of outside air.Therefore, the control air 8 for heating and soaking it is lighter and It will rise in wet channel 3, and generate stack effect.In wet channel 3, evaporation latent heat is removed, this causes in wet structure On 15 cooling work air 8 and finally due to by surface 15 heat transmitting in dry channel 2 be pre-chilled outside air 7. If outside air 7 is directly derived from atmosphere and first via turbine 4 by dry channel 2, when it is used as control air 8 When, pass through wet channel 3 and contact the mobile film 16 of evaporation liquid, the dew-point temperature close to outside air can be cooled to.? When doing so, the outside air 7 in dry channel 2 can in the ideal case by moisten channel 3 in evaporation it is cold But dew-point temperature is arrived, surface 15 of the evaporation between dry channel 2 and wet channel 3 obtains latent heat.In fact, due to The resistance on surface 15, this temperature still can be higher.

In order to increase cooling potential (and greatly increase outside air 7 in dry channel 2 density and simultaneously reduce it is wet Moisten the density of the control air 8 in channel 3), control air 8 can pass through such as solar radiation (and heat of other forms) Method its from low altitude area to High aititude by being heated during wet channel 3, in wet channel 3, control air 8 It is contacted with moist surface 15.The temperature for improving control air 8 can increase latent capacity, to improve the steaming in wet channel 3 Send out the efficiency of cooling procedure.This is because influence of the latent heat to enthalpy is greater than sensible heat, and have as the temperature rises bigger It influences.In addition, its absolute humidity can be increased and therefore reduce its density by increasing the temperature of control air 8.In this case, The flow velocity of control air 8 increases in wet channel 3, therefore increases and can transport electric power as obtained by evaporation cooling.

The heating process of control air 8 is used for using solar radiation, it is advantageous that by black coating or use material 10 The outer surface 17 in wet channel 3 is covered, material 10 absorbs the heat (referring to fig. 2) from solar radiation well.

It is effective for generating lower pressure in wet channel 3 for control air 8.This generates two-fold advantages, increase Evaporation rate, and the rate of heat transfer in dry channel 2 is increased, wherein compared with wet channel 3, in 7 He of outside air There are lower rates of heat transfer between surface 15.Lower pressure in wet channel 3 means the lower dew point temperature of control air 8 Degree, therefore, it increases density and its power generation rate in the dry channel 2 of outside air 7.Here it is use to have greatly The atmospheric evaporation drive system (for example, vertical ring-shaped system, i.e. " pipe inner tube " pipeline 1) of possible height is reasonable grounds. Therefore, higher height generates the pressure in lower external air pressure and lower wet channel 3；It reduces turbine and goes out Air pressure in mouth (or the entrance 13 in wet channel 3).This also significantly increases the pressure drop on turbine 4, and therefore increases It can transport electric power as obtained by proposed atmospheric evaporation drive system.

Fig. 2 a is identical as Fig. 2, but this atmospheric evaporation drive system for generating electric power includes being used for outside air 7 and work Make the individual turbine 4 of air 8.It sometimes, will be individual when the main driving force inside atmospheric evaporation drive system 1 is quite high Turbine 4 is reasonable for control air 8.It depends on the parameter (temperature and humidity) of outside air, generates the volume of air External pressure, the pressure are directed to turbine 4.

Described atmospheric evaporation drive system (referring to Fig. 1, Fig. 2 and Fig. 2 a) can be used for generating electricity in day and night Power.Maximum power production rate occurs that solar radiation can be used to increase the temperature of the control air 8 in wet channel 3 in system When daytime.In this case, entire cold and dry outside air 7 is conducted through after through dry channel 2 Turbine 4 and it as control air 8 escape into wet channel 3.It is cold when solar radiation is not present at night (referring to Fig. 3) Turbine 4 is conducted through after through dry channel 2 with dry outside air 7 and it is escaped into as control air 8 Wet channel 3.But a part of this cold dry air 18 is extracted and is used as the cold source of consumer.Certainly, this In the case of, power generation rate reduces (because less control air 8 is by moistening channel 3), but simultaneously, at night, the system Generate electric power and cooling capacity.But this is reasonable for consumer, because usually at night, energy consumption is fewer than daytime.It adjusts The ratio (referring to Fig. 3) of the flow 8 and 18 of cold drying outside air 7 makes it easy to the electric power and cooling capacity for adjusting while generating.

Fig. 4 shows while generating the schematic cross sectional views of the atmospheric evaporation drive system of electric power and cold water 16.The system Similar to Fig. 2, wherein by after dry channel 2, entire cold and dry outside air 7 be conducted through turbine 4 and its Wet channel 3 is escaped into as control air 8.But in this case, there are excessive evaporation liquid 16, such as water or salt Aqueous solution flows downward along the surface 15 in wet channel 3.It, should after passing through from the top to the bottom in wet channel 3 The temperature of excessive water 16 can be cooled to the dew-point temperature of outside air in the ideal case.This cold water 16 from bottom Consumer is directed to as cold source.Using seawater or brackish water, when seawater desalination system is connected to seawater Or when brackish water 16, the synergistic combination of the technology of seawater desalination system is added after through wet channel 3, and is hereafter desalinated Water is utilized as cold source by consumer.In this case, seawater desalination system uses such as reverse osmosis.It should be noted that , which does not need heat for example from solar radiation, because moistening the water passed through in channel 3 Temperature is usually above the temperature of external atmospheric air.It is because water is from electric power and/or cooling system before this that this thing happens System discharge heat, hot water is directed into atmospheric evaporation drive system (cooling tower) and is cooled down later.Therefore, it is mentioned using this paper Invention out can recycle heat, which is invalidly discharged in atmosphere in traditional cooling tower.

Atmospheric evaporation drive system be only used for power generation (referring to Fig. 1 and Fig. 2) or generate simultaneously electric power and cold air (referring to In application Fig. 3), if not using excessive water 16, water flow will be exactly equal to occur most during wet 3 stage of channel Big evaporation.The wicking of the entire scope of the inner surface 15 in wet channel 3 would be desirable.When using brackish water or seawater, The excessive water 16 for advantageously using 10-25%, reduces the precipitating of solute.

Using proposed atmospheric evaporation drive system, electric power, cooling capacity are generated using the heat of exhaust uptake gas It is economical with distilled water.For this reason, it is necessary to which the design to traditional chimney carries out some constructive changes.In such case Under, if the absolute humidity of exhaust uptake gas is less than or equal to the absolute humidity of outside air, can be used presented here Atmospheric evaporation drive system, come generated electricity (referring to Fig. 1 and 2) or simultaneously generate electric power and cold air (referring to Fig. 3) or Electric power and cold water (referring to fig. 4) are generated simultaneously, without any change.For this purpose, the exhaust uptake gas of heat is directed to wet lead to Road 3 is directly contacted with control air 8, and improve control air 8 (reduces close by the temperature and humidity during moistening channel 3 Degree).

If the absolute humidity of exhaust uptake gas 31 is greater than the absolute humidity of outside air 7, work sky must be implemented in Gas 8 is by moistening the mediate contact between 3 period of channel exhaust uptake gas 31 and control air 8 (referring to Fig. 5).For this purpose (referring to Fig. 5), to proposed tool, there are two the wet of the atmospheric evaporation drive system 1 of vertical concentric cylinder 15 and 17 for we Profit channel 3 is added to third vertical concentric cylinder 32.It, which is provided, forms new row with known dry channel 2 and wet channel 3 A possibility that gas channel 30, wherein thermal exhaust flue gas 31 be conducted through concentric drums 32 surface and control air 8 it is indirect Contact passes through the temperature and humidity (reducing density) of increase control air 8 during moistening channel 3 in control air 8.Moreover, working as When generating dry channel 2 and wet channel 3 and placing plate 15 inside pipeline 1, plate 32 can be used rather than the Three vertical concentric cylinders 32.But it must be always between the dry channel 2 that air-flow passes through, wet channel 3 and exhaust passage 30 The heat exchange mechanism carried out in the presence of the surface (or surface of cylinder 15,17 and 32) by these plates 15 and 32.

It is worth noting that, free convection cooling tower is also atmospheric evaporation drive system.Nowadays, they are widely used, Especially for large-scale thermic load occasion.Free convection cooling tower provides air circulation using convective flow principle.Wind is not needed Fan.When the air in tower is by hot water heating, it can be risen by tower.The process sucks more air, generates natural airflow, with Evaporation cooling is provided after electric power and/or cooling system discharge heat in hot water.Tower casing is usually made of armored concrete, can be high Up to 200 meters.The efficiency of these natural cooling towers is very low, their product is cold water, and wherein temperature can be in ideal situation Under be cooled to wet-bulb temperature.Using the present invention, advanced free convection cooling tower can be created, cold water (cold water can be generated Temperature can be cooled to dew-point temperature in the ideal case) and at the same time power supply.For this purpose, it is necessary in tower casing (pipeline) Vertical dry channel 2 and wet channel 3 are organized, they are connected in bottom, and place (see Fig. 4) by turbine 4.In addition, these elder generations Into free convection cooling tower have bigger capacity because they using proposed atmospheric evaporation drive system realization More effective free convection evaporation cooling procedure (referring to fig. 4).Therefore, it is driven the invention discloses a kind of using atmospheric evaporation System generates the new method of electric power and cold water as cooling tower.It can create the advanced cooling tower of absolute last.It uses These advanced cooling towers can obtain more cold water (dew-point temperature is compared with wet-bulb temperature) and electric power simultaneously.In addition, In many cases (for example, for dry and hot climatic province), free convection cooling tower can be used instead of fan coolling Tower.Consumption electric power needed for fan work can be significantly reduced in it.

Proposed atmospheric evaporation drive system can be public by armored concrete, steel, aluminium, composite material or this field The other materials known is made.The selection of material depends on the height of atmospheric evaporation drive system.Similarly, for dry channel 2 With wet channel 3, space frame can have different geometry and material.It is to be noted, however, that modern technologies (example Such as, RUPP Industries, Inc.) the new plastic film nowadays created, they are successfully used to heating, cooling and ventilation is answered Pipeline in.These pipelines are cheap, durable, light-weight, inflatable and be made of fire-retardant special plastic material.These are managed Road is reasonably, especially in the low clearance of these systems for proposed atmospheric evaporation drive system.

Proposed atmospheric evaporation drive system realizes disclosed generation electric power, cooling capacity and distilled water Method is provided using cheap and pressurize inflatable tedge rather than valuableness, very big height and cross-sectional area show There is the only possible property of atmosphere thermal energy converting system.Traditional material needed for this huge system is so big, so that due to The inexpensive efficiency for the converting system being previously proposed and keep its cost excessively high.

The present invention provides a possibility that a small amount of material is used for riser structural is used only, driven to obtain the atmospheric evaporation The feasible cost efficiency of dynamic system.Moreover, can be constructed a kind of for keeping when the material for being used for the structure on a small quantity is used only Device with support for the structure of dry channel 2 and the rising ring pipe 1 in wet channel 3.In this case, pass through black Coating uses the substance 10 for absorbing heat well from solar radiation, it is easy to by the outer surface 17 in wet channel 3 This material (for example, plastic foil) cladding.

The concentric drums 15 and 17 that proposed atmospheric evaporation drive system uses two structures to connect are as being used for The rising ring pipe 1 of dry channel 2 and wet channel 3 (referring to Fig. 1).Compared with single cylinder, it is in static and dynamic condition It is lower to generate excellent Weight structure performance (Structural Performance to Weight).The two 15 Hes of concentric drums 17 provide more robust structure basis, which increase the structure height in channel 2 and 3 and resist various modifications mode.Having Have under the prevailing outside wind of basic horizontal component, cylindrical structure tends to be deformed into ellipse.Wind may also lead to cylindrical knot Structure is bent and deforms under torsional bending.However, for dry channel 2 and wet channel 3, the concentric drums of two structures connection 15 and 17 as the ring pipe 1 risen, for identical material weight, than single cylinder better against oval modification, buckling, Torsional bending and other deformation patterns.This is for having the pressurization for dry channel 2 and wet channel 3 to may expand tedge 1 Atmospheric evaporation drive system for be even more important.

The thin-wall expandable of structure connection rises the internal pressurization of ring duct 1 (see Fig. 6) from wet channel 3, because wet Moisten the density that the heating in channel 3 is lower than mutually level outside air with the density of the control air 8 of wetting.Wet channel 3 In the low-density of control air 8 cause in the wet channel 3 for the external pressure of the outer surface 17 in wet channel 3 High pressure, in wet 3 internal expansion of channel and support thin-walled, inflatable rise ring pipe 1.The thin-walled of structure connection can be swollen Swollen rising internal pressurization of the ring pipe 1 from dry channel 2, because of the density of the cold and dry outside air 7 in dry channel 2 Higher than the density of the control air 8 of heating and wetting in mutually level wet channel 3, thus swollen in dry channel 2 It is swollen and support thin-wall expandable rise ring pipe 1.Atmospheric evaporation drive system shown in Fig. 6 may also include balloon 19 and connection Cable 20.They at High aititude for keeping and supporting the pressurization with dry channel 2 and wet channel 3 to may expand tedge 1.In general, balloon 19 is packed into the low density gas of such as hydrogen, but the work of heating and wetting also can be used in the present invention Air 8, after the control air 8 for heating and soaking is by wet channel 3, density is lower than the density of outside air.At this In the case of kind, using the balloon 19 with double-walled (outer wall 21 and inner wall 22) generated between them for condensation space 23 Space is effective.The surface of the outer wall 21 of balloon 19 has heat exchange mechanism with external atmospheric air, and wherein temperature is always Less than the temperature in balloon 19.The surface of outer wall 21 is made by white covering or by special reflecting material, comes from the sun to reduce The heat absorption of radiation.

In some cases, the shape of bagel can be made in balloon 19.Here, 21 He of outer wall of the bagel of the balloon Inner wall 22 forms condensation space 23, and condensation space 23 has the heat exchange mechanism with external atmospheric air.

The top of the condensation space 23 of balloon 19 is via entrance 24 and the expandable wet channel 3 for rising ring pipe 1 Outlet 14 is connected by conduit.The condensation space 23 of balloon 19 further includes for the outlet 25 of control air 8 and for distilled water Sink 26.

The control air 8 of heating and wetting flows in conduit via outlet 14 and entrance 24 after through wet channel 3 To the top of the condensation space 23 of balloon 19 (referring to Fig. 6).Here, control air 8 by outer wall 21 (and inner wall 22, if If balloon has bagel shapes) convection current, conduction and the radiation on surface transfer heat in atmosphere and be cooled, water as a result, Divide and is condensed in the form of distilled water 27 from the control air 8 in condensation space 23.The distilled water 27 guides downwards via sink 26 In to vertical tube 28 and by hydroturbine 29, used for consumer.The vertical downward flow driving hydroturbine 29 of distilled water 27 is with life At electric power, the electric power of generation can be used for different purposes, such as pump, which is transported to top from bottom water to soak pipeline 1 Wet channel 3.

It is proposed not use balloon with the expandable atmospheric evaporation drive system for rising ring pipe 1 It is placed in the case where 19.In some cases, it may be coupled to the side on mountain, and the upper end is located at the High aititude on mountain, and its At the low altitude area that lower end is situated at the foot of a hill.Moreover, expandable rising ring pipe 1 may be coupled to any kind of building or The side of tower.In this case, described atmospheric evaporation drive system can only generate electric power, and its work is in Fig. 1 In scheme shown in Fig. 2.

High atmospheric evaporation drive system for power generation or the system using balloon 19 (referring to Fig. 6), sometimes using for example The low boiling point of ammonia or water-ammonia mixture evaporation liquid 5 is advantageous instead of water to soak wet channel 3.The system such as Fig. 6 a institute Show.Compared with water (100 DEG C), the boiling point of ammonia is lower (- 33 DEG C).If being expanded into atmospheric pressure, high pressure ammonia will provide very low The gas of density.Therefore, when liquid ammonia 16 is evaporated in control air 8 in wet channel 3, the air-ammonia mixture tool There is the density lower than air-water mixt, because compared with water, more ammonia can be evaporated in control air 8.Using coming from Liquid ammonia 16 is evaporated in the control air 8 in wet channel 3 by the heat of the extraneous air stream 7 of dry channel 2.This Afterwards, with using water come compared with soaking the atmospheric evaporation drive system in wet channel 3,7 temperature of extraneous air stream decreases below dew Point temperature and the increase of its density.As a result, the low boiling point using such as ammonia evaporates liquid 5, the work in wet channel 3 can be reduced Make the density of air 8, while increasing the density of the extraneous air stream 7 in dry channel 2.Therefore, between air-flow 7 and air-flow 8 Density variation is increasing, and it generates more electric power by air turbine 4.

Atmospheric evaporation drive system shown in Fig. 6 a may also include balloon 19 and connection cables 20 (identical with Fig. 6). They at High aititude for keeping and supporting the pressurization with dry channel 2 and wet channel 3 to may expand tedge 1, at this The temperature of outside air is sufficiently low to condense the ammonia steam from control air 8 at High aititude.

Air-ammonia mixture via outlet 14 and enters in conduit after it is by wet channel 3 as control air 8 Mouth 24 flow to the top of the condensation space 23 of balloon 19.Here, convection current, conduction of the control air 8 by the surface of outer wall 21 It transfers heat in atmosphere and is cooled with radiation, the steam of ammonia is in the form of liquefied ammonia 27 from the work in condensation space 23 as a result, Make to condense in air 8.Liquid ammonia 27 as evaporation liquid 5 is downwardly directed toward wet channel 3 via sink 26.

In order to soak the wet channel 3 of pipeline 1, the vertical downward flow of liquid 5 is evaporated along surface 15 from the top to the bottom It is mobile, as the mobile film 16 of liquefied ammonia.

The proposed atmospheric evaporation drive system with low boiling point evaporation liquid 5 can be without using balloon 19 In the case of place.In some cases, it may be coupled to the side on mountain, and the upper end is located at the High aititude on mountain, and its lower end At the low altitude area being situated at the foot of a hill.Moreover, it can be high tower, height is enough to condense the steam of low boiling point evaporation liquid 5.

In the case where High aititude, low ambient temperature and pressure, it may be desirable to realize the relatively low temperature of low boiling point evaporation liquid 5 Degree evaporation process simultaneously provides minimum density (maximum lift) for the control air 8 inside wet channel 3.Thus, it is possible to increase gas Density contrast between stream 7 and air-flow 8, and more electric power are generated by air turbine 4.With low temperature and very at High aititude It is empty, it is easier to use with the low boiling point evaporation liquid 5 compared with low boiling temperature as evaporating liquid rather than water.It provides life A possibility that at additional power.

But Fig. 7 and Fig. 8 be the atmospheric evaporation drive system for generating electric power and distilled water simultaneously schematic cross sectional views and Top view.

The system (Fig. 7 and Fig. 8) includes the third vertical concentric cylinder 32 in the wet channel 3 of pipeline 1, and pipeline 1 has There are known two vertical concentric cylinders 15 and 17.It can form condensation channel with known dry channel 2 and wet channel 3 34, wherein condensation air 35 (a part of control air 8) is directed to lead to by the surface of concentric drums 32 in control air 8 Cross wet 3 period of channel and 8 mediate contact of control air.Vertical panel 15,32 and 17 can also be used to replace vertical concentric cylinder 15,32 and 17, with formed between dry channel 2, wet channel 3 and condensation channel 34 heat exchange surface 15,32 and 17 (referring to Fig. 7).

Always wet channel 3 is arranged between dry channel 3 and condensation channel 34, and wet channel 3 is by wet Moisten wetting in 3 surface 15 and 32 of channel and there is heat exchange relationship with the latter.Surface 15 has dried side (in dry channel 2 In a part) and its reverse side be wet wall (in a part in wet channel 3).Another surface 32 has dried side (cold In a part in solidifying channel 34) and its reverse side be wet wall (in a part in wet channel 3).These surfaces 15 and 32 it is anti- It is soaked to wet wall using any art methods seawater or brackish water 5, such as coats this with wetting capillary porous material A little plates.

The wet wall on surface 15 and 32 forms wet channel 3 as a result, and their dried side forms atmospheric evaporation driving system The dry channel 2 and condensation channel 34 of system, for generating electric power and distilled water simultaneously.

The operation for the system for generating electric power and distilled water simultaneously is as shown in FIG. 7 and 8, its working principles are as follows: dry logical Outside air 7 is provided at the entrance 11 in road 2.The air 7 flows through dry channel 2, and the dry channel 2 and wet channel 3 carry out heat Transmitting contact, control air 8 pass through wet channel 3.Therefore, channel 3 is moistened to be arranged to pass via surface 15 and 2 heat of dry channel Contact is passed, which has limited corresponding dry channels 2.In a part in wet channel 3, the reverse side evaporated liquid 16 on surface 15 The mobile film of (such as seawater or brackish water) soaks.It will be cooled to by the outside air 7 of dry channel 2 close to its dew-point temperature Without changing water capacity.Then, because cold air is heavier, cold air 7 will be declined by dry channel 2 from High aititude to low altitude area Flowing.Cold air 7 improves its density and sinks, and generates inverse stack effect.Cold outside air 7 is with high-speed in dry channel 2 Middle flowing provides power for turbine 4, and escapes into wet channel 3 as control air 8, and turbine 4 is connected to generator 6.This Afterwards, control air 8 flow to High aititude from low altitude area rising by wet channel 3.It is contacted with moist surface 15, moist surface 15 are soaked by the mobile seawater of fluid film 16 or brackish water 5.

Meanwhile control air 8 is contacted with moist surface 32, moist surface 32 also by mobile fluid film 16 seawater or Brackish water 5 soaks.

When control air 8 passes through along wet channel 3 (Fig. 7), it is heated, soaks and its density is lower than outside air Density.Therefore, the control air 8 for heating and soaking is lighter and will rise in wet channel 3, generates stack effect.? After wet channel 3, a part of control air 8 is discharged into atmosphere, and another part quilt as condensation air 35 It is directed to condensation channel 34.In wet channel 3, the latent heat of evaporation is removed, this leads to the bosher on wet structure 15 and 32 Make air 8 and finally, since the heat by surface 15 is transmitted, in dry channel 2 and also by surface 32 to outside air 7 It is pre-chilled, thus cooling in condensation channel 34 and condensation condensation air 35.

If outside air 7 extracts directly from atmosphere and first via turbine 4 by dry channel 2, when with When making control air 8, by wet channel 3 and contact wetting 16, it can be cooled to the dew-point temperature close to outside air.At this When sample is done, the evaporation cooling in wet channel 3 can be passed through in the ideal case in the outside air 7 in dry channel 2 To dew-point temperature, surface 15 of the evaporation between dry channel 2 and wet channel 3 obtains latent heat.Moreover, logical in condensation The condensation air 35 of heating and wetting in road 34 can be by moistening evaporation cooling and condensation in channel 3, the evaporation The surface 32 acted between condensation channel 34 and wet channel 3 obtains latent heat.Because condensing air 35 and above-mentioned wet channel 3 In heat exchange relationship, moisture is condensed in the form of distilled water 37 from the air-flow 35 in condensation channel 34 as a result, and distilled water 37 is For consumer's selection.

The temperature of control air 8 in wet channel 3 is always sufficiently low, to guarantee vapor from passing through condensation channel 34 Heating and wet condensation air 35 condense.Condense the indirect heat transfer for passing through surface 32 between air 35 and control air 8 Tend to condense vapor in the form of distilled water 37.

Therefore, condensation air 35 reduces its water capacity in condensation channel 34.Because cold and dry air is heavier, because This cold and dry condensation air 35 is by condensation channel 34 from High aititude Doenward flow to low altitude area.It can improve its density, And can sink, generate inverse stack effect.The condensation air 35 is flowed in condensation channel 34 with high-speed, is provided for turbine 36 dynamic Power, and escape into atmosphere, turbine 36 is connected to generator.But condensation air 35 and distilled water 37 are leading to from the top to the bottom It crosses after condensation channel 34, can be used for additional cooling application, because their temperature will be less than the temperature of outside air.

Furthermore, it is possible to which (referring to Fig. 7) moves to drive water using the vertical downward flow of the distilled water 37 from condensation channel 34 Turbine can be used for different purposes to generate additional electric power.

It should be noted that proposed atmospheric evaporation drive system, realize disclosed generation electric power, cold The method of amount and distilled water can have one group or more the drying connected, wet and condensation channel.As a result, which increase movements Heat exchange surface between air-flow, these movement air-flows pass through dry, wet and condensation channel.This always brings these systems to imitate The raising of rate.Vertical concentric cylinder or plate can be used or other geometries are the channel creation heat friendship between mobile air-flow Change surface.

For example, Fig. 9 (identical as Fig. 4) shows while generating the atmospheric evaporation drive system of electric power and cold water, but it is wrapped The extension element of dry channel 2 and wet channel 3 containing multiple connections, these dry channels 2 and wet channel 3 are located at a pipe In road 1.In addition, always having heat exchange mechanism between these dry channels 2 and wet channel 3.

But anyway, after through enough dry channels 2, entire cold and dry outside air 7 is drawn Turbine 4 was connected, provides power for turbine 4, and it is escaped into enough wet channels 3 as control air 8.

The system (referring to Fig. 9) can be used successfully as free convection cooling tower, wherein coming from electric power and/or cooling system Hot water 5 be directed into wet channel 3 as evaporation liquid 16.The high temperature of water 58 helps to improve this atmospheric evaporation driving system The efficiency of system, which, which not only generates cold water, (can be cooled to dew-point temperature for temperature in the ideal case Rather than the wet-bulb temperature of traditional cooling tower), but also power simultaneously.In addition, proposed nature can be significantly reduced in it The power consumption of convection current cooling tower and noise, compared with the traditional cooling tower for needing fan, proposed free convection is cold But tower does not need fan.

Figure 10 is identical as Fig. 9, but atmospheric evaporation drive system that is this while generating electric power and cold water also includes to be used for Pass through the water jacket 41 of heat by solar radiation water.The system includes the extension element of multiple dry channels 2 and wet channel 3, can be with It is successfully used under conditions of the spent hot water not from electric power and/or cooling system.At ambient temperature any The water 5 (can be seawater or brackish water or liquid drier etc.) of type is transported to the water jacket of pipeline 1 via pump 39 by pipe 40 41 bottom.Water jacket 41 is the space very narrow water filling (Water Flood)；The outer surface of its surface covering pipeline 1.Water jacket 41 outer surface is sufficiently large, so as to initiatively absorb the amount of heat from solar radiation.

Advantageously, being covered by black coating or using the material of heat can be absorbed well from solar radiation The outer surface of water jacket 41.Water 5 is heated in water jacket 41 by solar radiation, free convection water moving process occurs herein；Knot Fruit, most warm water layer 5 are moved to upper layer and enter water jacket 41.Here, hot water 5 is assigned to from water jacket 41 by water dispenser 42 wet Moisten the top in channel 3, wet channel 3 is soaked from the top to the bottom by the mobile moisture film 16 of heat.

It is important that it is however emphasized that, during fine day, irrigation sleeve 41 can pass through a large amount of heat of solar radiative absorption.It is this Heat is enough to run atmospheric evaporation drive system persistently effectively at night and cloudy day.

Figure 11 (identical as Fig. 7) shows while generating the atmospheric evaporation drive system of electric power and distilled water, but it includes The dry channel 2 of multiple connections, the extension element for moistening channel 3 and condensation channel 34, these channels are all located at a pipeline 1 In.

In general, realize any real system of the disclosed method for generating electric power, cooling capacity and distilled water include one group with On dry channel 2, wet channel 3 and condensation channel 34 (as shown in Figure 7).Nevertheless, each wet channel 3 must position Between dry channel 2 and condensation channel 34, and in wet between channel 3 and dry channel 2 and wet channel 3 and condensation There must be heat exchange mechanism between channel 34 always.

Therefore, entire cold and dry outside air 7 is conducted through whirlpool after through enough dry channels 2 Wheel 4 provides power for turbine 4, and it is escaped into as control air 8 in enough wet channels 3, and then it is as cold Solidifying air 35 is directed to enough condensation channels 34.

In addition, a part of control air 8 is selected to enter atmosphere side by side after through wet channel 3.

Note that proposed atmospheric evaporation drive system may include separated solar water heater 45 without It is water jacket 41, for passing through heat by solar radiation water 5 (referring to Figure 12).Here, 39 guidance water 5 of pump passes through solar water heater 45, solar water heater 45 can initiatively absorb the amount of heat from solar radiation.By solar water heater 45 it Afterwards, hot water 5 is conducted through pipeline 40 and it is assigned to the top in wet channel 3, moistens channel 3 by the mobile moisture film 16 of heat It is soaked from the top-to-bottom of pipeline 1.

Furthermore, it is possible to which solar radiation to be used for separated solar water heater 45 and water jacket 41 simultaneously.

International community concentrates on atmospheric greenhouse gas such as carbon dioxide (CO to the worry of global warming more and more₂) In effect, the effect as greenhouse gases leads to various countries and international efforts reduce the total release of carbon dioxide or seal up for safekeeping These emissions, to be isolated and be disposed into the carbon dioxide treatment pond other than atmosphere.These require in production scene or The technology of carbon dioxide is then captured from air.Some of technologies are ready.For example, the dioxy in capture air Changing carbon emission can be realized by allowing wind to take air on the absorber of absorbing carbon dioxide to.This can be by various methods It realizes, including blows air over limewash, this is by the carbon dioxide removed in air and generates lime stone.Lime captures in air Useless carbon dioxide and generate heat.The program by Columbia University physicist Klaus Lackner plan, will directly from Removing carbon dioxide is removed in air, and is stored in rock or underground.The global investigative technique in Arizona State Tucson city is public Department (Global Research Technologies) has set up the project, it is intended to which titanium dioxide in wind can be removed by building first The prototype unit of carbon, carbon dioxide are the main greenhouse gas for causing climate change.A kind of selection is venetian type shutter system System, wherein the slit in shutter will allow absorbent to flow through the structure, and carbon dioxide is continuously collected when wind passes through.It is another Possible system is using the loose wet pad for squeezing glass fibre, similar to that in automobile filter.Flow through the liquid of fiber Know from experience capture carbon dioxide.

But this prior art design has the disadvantages that

Realize that the known system of this process that carbon dioxide is captured from air spends big energy to convey air.

Known system, which must have, to be excluded to absorb hot knot after capturing carbon dioxide in air by limewash Structure.

Make by known method and design, it is impossible to efficiently and economically realize and capture carbon dioxide and simultaneously from air Generate electric power, cooling capacity and distilled water.

The invention discloses a kind of generation electric power, the method for cooling capacity and distilled water, while it is additionally provided from air or gas Unique possibility that carbon dioxide is captured in body, without extra charge.The present invention is wind-driven generator, can be from external sky Great amount of carbon dioxide is removed in gas 7 or flue gas 31 or both.

For this purpose, it is necessary to which addition concentration absorbent, the absorbent are caught from outside air 7 in the dry channel 2 of pipeline 1 Obtain carbon dioxide.

Figure 13 is identical as Fig. 2, but the atmospheric evaporation drive system 1 also includes 46 coating of absorbent of dry channel 2, such as Limewash 46 extracts carbon dioxide out from outside air 7.In addition, being transported to wet channel from dry channel 2 via surface 15 3 absorption heat helps to increase the cooling capacity in wet channel 3.Therefore, the effect increase in dry channel 2 and Heat and capability and performance in wet channel 3.

Proposed atmospheric evaporation drive system 1 may include 46 coating of absorbent of dry channel 2, such as liquid Desiccant 46 extracts vapor out from outside air 7 (referring to Figure 13).The drying of outside air 7 can use liquid drier, Such as lithium chloride, bromide, calcium chloride, ethylene glycol, triethylene glycol etc..When being combined with the desiccant 46 in dry channel 2, this permits Permitted the dew-point temperature for being cool below outside air 7, because it reduces the water capacity of outside air 7, to increase latent heat Latent capacity.

This has the direct effect for reducing the humidity in outside air 7, allows lower temperature (higher density) and increases The cooling capacity added.Liquid drier 46 on surface 15 in dry channel 2 absorbs the vapor from outside air 7, and The evaporation liquid for transferring heat to wet channel 3 by surface 15 is mobile film 16 (such as water), the mobile film of evaporation liquid 16 are evaporated in control air 8.The continuous coo1ing of liquid drier 46 increases the drying energy of outside air 7 in dry channel 2 Power.

It thus can by generating colder and drier outside air 7 in dry channel 2 using liquid drier 46 Poor to dramatically increase pressure (or density), wherein temperature can be cooled to lower than dew-point temperature.In addition, any 46 (stone of absorbent Buck or desiccant) it is guided after it is by dry channel 2 for recycling.

The present invention provides not only from outside air 7 capture carbon dioxide and also from flue gas 31 capture carbon dioxide can It can property.Figure 14 is identical as Fig. 5, but the atmospheric evaporation drive system further includes 46 coating of absorbent of exhaust passage 30, such as Limewash 46 extracts carbon dioxide out from exhaust uptake gas 31.

In this case, limewash 46 can also be used for dry channel 2, if necessary, not only capture comes from The carbon dioxide of flue gas 31, and the carbon dioxide from outside air 7 is captured simultaneously.

Liquid drier 46 can also be used for dry channel 2 and limewash 46 is used for exhaust passage 30.This In the case of, it can be realized simultaneously two useful processes: from capture carbon dioxide in flue gas 31 and reducing in outside air 7 Humidity.

The proposed needs of atmospheric evaporation drive system 1 with liquid drier 46 pass through in liquid drier 46 The weak desiccant 46 is recycled after dry channel, liquid drier 46 extracts vapor out from outside air 7.For this purpose, using Solar generator 47 (see Figure 15) is reasonable, the design of solar generator 47 and proposed evaporation drive system 1 It is identical, and liquid drier 46 is used to substitute water 5 as the evaporation liquid 5 in wet channel 49.

The solar generator 47 includes dry channel 48 and wet channel 49.Here there is transparent wall 52, for accessing too Sun radiation is used as heat source.The transparent wall 52 is the side in wet channel 49, the other side be wet channel 49 and dry channel 48 it Between heat exchange surface 53.

Here (referring to Figure 15), weak liquid drier 46 is selected from the bottom of the dry channel 2 of evaporation drive system 1.

Weak liquid drier 46 is directed into the wet channel 49 of solar generator 47, for soaking its heat exchange surface 53.Meanwhile outside air 50 is guided to the dry channel 48 of solar generator 47 by fan 51 first and is next guided To wet channel 49.In doing so, the outside air 50 in dry channel 48 can be in the ideal case by wet logical Evaporation in road 49 is cooled to dew-point temperature, heat exchange of the evaporation between dry channel 48 and wet channel 49 Surface 53 obtains latent heat.

Solar radiation (referring to Figure 15) as heat source passes through transparent wall 52 and increases the temperature of weak liquid drier 46. This helps to evaporate water from this desiccant 46, which is become by concentrated solution.Solar radiation also increases external sky The temperature of gas 50, thus when liquid drier 46 and outside air 50 pass through the wet channel 49 of solar generator 47, outside Portion's air 50 can absorb more vapor from liquid drier 46.Meanwhile the weak liquid drier by moistening channel 49 46 reduce its temperature by evaporating cooling procedure.After solar generator 47, the cold and strong liquid with high concentration is dry Agent 46 returns to the top of the dry channel 2 of evaporation drive system 1.The dry channel 48 for first passing through solar generator 47 simultaneously Then by wet channel 49 after, a part that the wet outside air 50 of heat with low-density can be used as control air passes through Adjustable valve 54 is directed to the bottom in the wet channel 3 of evaporation drive system 1, or can be vented to atmosphere.

Outside air 50 can be guided by fan 51 to dry channel 48 and wet channel 49.In addition it is also possible to not making Process is driven with the identical atmospheric evaporation realized in the case where fan with described before for system 1, in solar power generation Down current is generated in the dry channel 48 of machine 47, and generates ascending air in wet channel 49.Therefore, using sun spoke It penetrates, production capacity can be increased by evaporation drive system 1, and can also strengthen and realize that solar generator 47 recycles weak liquid The process of soma drying prescription 46.

It is important that it is however emphasized that, proposed atmospheric evaporation drive system is available or not available build in solar energy It builds and implements the good configuration that natural air is adjusted and divulged information in object.

Figure 16 is schematically cuing open for the atmospheric evaporation drive system 1 for adjusting and divulging information for the natural air in building 49 View.Cold and dry outside air 7 is directed into wet channel 3 as control air 8 after through dry channel 2.But It is that a part of the air is extracted as cold dry air 18 and for introducing the interior space 49 by access road 50.Entrance Channel 50 is connect with the dry channel 2 of atmospheric evaporation drive system 1.The cold dry air 18 entered always has more than room air Big density, this is the reason of it enters the room space 49 by gravity-flow ventilation.

The interior space 49 (referring to Figure 16) also has exit passageway 51, exit passageway 51 and atmospheric evaporation drive system 1 Wet channel 3 connects, wherein hot wet control air 8 is by moistening channel 3.The density of the control air 8 is consistently less than Interior Space Gas, this is that a part of this room air enters wet channel 3 from the interior space 49 by gravity-flow ventilation as air-flow 52 Reason.

Using solar radiation for moistening channel 3, by reducing the density of control air 8 and increasing in wet channel 3 Cooling capacity, the natural air for helping to improve the interior space 49 adjust and divulge information.

Therefore, using proposed atmospheric evaporation drive system 1, it is cold natural process can be able to achieve by means of the sun But it and divulges information.

Atmospheric evaporation drive system 1 of the invention provides a possibility that generating cold and dry air 18, the temperature of air 18 Degree can be cooled to the dew-point temperature of outside air in the ideal case.For hot and moist climatic province, this dew point temperature Degree can be quite high.In this case, it to reduce dew-point temperature, is used for using the atmospheric evaporation drive system 1 with desiccant Natural air in building is adjusted and ventilation is reasonable, such as liquid drier 46 as shown in fig. 13 that.The liquid is dry Agent 46 extracts vapor out from outside air 7 during passing through dry channel 2.This can reduce the humidity of outside air 7 And its dew-point temperature.Therefore, these systems can be used for the adjusting of the natural air in the building in any climatic province and ventilation.

For these systems (especially for there are the heat of a large amount of solar energy and humid climate regions), sent out using solar energy Motor 47 is effectively, as shown in figure 15 by the weak liquid drier 46 after dry channel 2 to recycle.

Figure 17 shows in building natural air adjust and ventilation this atmospheric evaporation drive system 1, Comprising solar generator 47, for being returned after the dry channel 2 that weak liquid drier 46 passes through atmospheric evaporation drive system Receive weak liquid drier 46.It is identical solar generator 47 with what is be shown in FIG. 15 and describe.

Solar radiation is used for solar generator 47, the effective of liquid drier 46 and cheap time not only may be implemented Receipts process, and the efficiency of the dehumidification process of 2 outside air 7 of dry channel can be improved.This is because we are in solar energy Not only strong but also cold liquid drier 46 is obtained after generator 47, which is directed into atmospheric evaporation The top of the dry channel 2 of drive system 1.

Therefore, the present invention provides create a possibility that reasonable indoor environment is as energy conservation and environmental-friendly selection.

If in outside air 7 by 2 period of dry channel and control air 8 by the way that during wet channel 3, outside is empty Density variation between gas 7 and control air 8 is sufficiently large, then in the bottom of pipeline 1, installation turbine 4 is that reasonably, the two are logical Road connects (see Figure 16 and Figure 17) in the bottom of pipeline 1.The turbine is used to the energy of moving air being converted into useful type Power.

It can be used for providing ventilation in coal mining with identical system shown in Figure 16 and Figure 17.There are many discarded coal mine tools Have in two main channels of different level.Can be used one of two channels for enter cold with dry air 18 and be used for Enter initiation coal combustion by cold and dry air 18.The channel of higher level can be used for being discharged the combustion as thermal current 52 Burn gas.The hot combustion gas can be used for driving turbine to generate electric power.

It is worth noting that, atmospheric evaporation drive system 1 is difficult with and safeguards sometimes, wherein there is many in the duct Dry channel 2 and wet channel 3, system have bigger height.It in this case, the use of special turbine 55 is also reasonable , special turbine 55 is also rotary regenerative heat and mass exchanger.The turbine 55 can be between outside air 7 and control air 8 It realizes the identical heat and mass exchange process with the realization (referring to Fig. 1-17) in above system, uses edge in these systems The dry channel 2 of the level configurations of pipeline 1 and wet channel 3.But use turbine 55, it is easier to application and maintenance atmospheric evaporation Drive system 1.

Figure 18 is the perspective view for generating the atmospheric evaporation drive system 1 of electric power, wherein using turbine 55, turbine 55 is also simultaneously Realize the heat and mass exchange process between outside air 7 and control air 8.

Figure 19 is the perspective view of turbine 55, and turbine 55 includes a series of disk for being divided into blades by axial groove 59.Here: 56 It is the exhaust sector of regrown material 56 for entrance sector that regrown material, 57 are regrown material 56,58,60 is regrown material 56 Wetting sector, 61 be injector, 5 be water.

Turbine 55 (referring to Figure 19) includes by a series of of axial groove 59 and regrown material 56 (heat absorption and heat extracting material) Blade.It must be the permeable evaporation liquid retaining material of air (or gas), be divided into two sectors 57 and 58.Entrance For passing through outside air 7, exhaust sector 58 is used to keep work empty after outside air 7 is by entrance sector 57 for sector 57 Gas 8 passes through.Being vented sector 58 includes wet sector 60, and wet sector 60 is soaked by water jet 61 by water 5.By making regenerated material Material 56 cyclically turns to control air stream 8 from extraneous air stream 7 after outside air 7 is by entrance sector 57, allows to connect Continuous operation.In this case, entrance sector 57 becomes exhaust sector 58 and is vented sector 58 as entrance sector 57.It is worth note Meaning, outside air 7 and control air 8 are isolation, therefore they are separated from each other.

Referring to Fig.1 9, outside air 7 flows through the regrown material 56 of turbine 55 after the dry channel 2 by pipeline 1 Entrance sector 57.Here, outside air 7 is cooled to close to its dew-point temperature without changing after contacting with Cooling-recycling material 56 Become its water capacity.Cold outside air 7 improves its density and generates inverse stack effect for sinking.Cold and dry is outer Portion's air 7 flows through a series of blades by axial groove 59 with high-speed, provides power for turbine 55, turbine 55 is connected to generator 6.This rotates regrown material 56 and increases the temperature of regrown material 56 to approach the temperature of the outside air 7 entered.

After the subsequent process that outside air 7 is pre-chilled, during outside air 7 passes through entrance sector 57 (see Figure 19), Outside air 7 is turned to by 180 °, and it flows to the exhaust sector 58 of the regrown material 56 of turbine 55 as control air 8, with It is directly contacted with the wetted surface of wet sector 60.Wet sector 60 is formed by the square of 10%-85%, and uses liquid Nozzle or injector 61 to soak wet sector 60 by evaporation liquid such as water 5.

In order to cool down purpose, the amount for the water 5 being sprayed on wet sector 60 is only the amount that can effectively evaporate, wet to ensure Profit sector 60 enter entrance sector 57 when be it is dry, to be contacted with the outside air 7 of entrance.

Using the solar generator 47 as shown in Figure 15 and Figure 17, increase the temperature of water 5 using different types of heat Degree is effective, for example, passing through heat by solar radiation water.

After contacting with the outside air 7 in entrance sector 57, turbine 55 is rotated, and regrown material 56 transmits heat Amount, heat are absorbed from outside air 7, and are transmitted to from entrance sector 57 to exhaust sector 58, and exhaust sector 58 includes wet Moisten sector 60.During the wet sector 60 by heating, cold control air 8 is heated, and is soaked and is directed into pipe later The wet channel 3 in road 1.After control air 8 is directly contacted with the wetted surface of the wet sector 60 of regrown material 56 (referring to Figure 19), moisture is from the surface evaporation into control air 8.In this case, the latent heat of evaporation is removed, this causes to regenerate The cooling of the exhaust sector 58 of material 56.After contacting with wet sector 60, control air 8 is heated and soaks and its is close Degree gets lower than the density of outside air 7.Therefore, the control air 8 for heating and soaking is relatively light, and by axial groove 59 with height Rate flows through a series of blades in ascending air, to provide power for turbine 55.Hereafter, control air 8 is flowed to from low altitude area High aititude, and will rise in the wet channel 3 of pipeline 1, generate stack effect.

After rotating turbine 55 (referring to Figure 19), cold exhaust sector 58 become with dew-point temperature, outside air 7 from Its entrance sector 57 passed through.In this case, outside air 7 can be cooled to dew-point temperature.Hereafter, as described above, making It is directed into the exhaust sector 58 of regrown material 56, for the cold outside air 7 of control air 6 with wet with wet sector 60 Surface directly contacts.

Using the turbine 55 for also realizing heat and mass exchange process between outside air 7 and control air 8, can subtract The height of small dry channel 2.

Figure 20 is identical as Figure 18 and Figure 19, but the atmospheric evaporation drive system of the generation electric power includes short dry channel 2. It provides a possibility that reduction builds and safeguards the cost of proposed atmospheric evaporation drive system.

Sometimes, the device separated using two is reasonable come the function of dividing turbine and regenerative heat and mass exchanger.

Figure 21 is identical as Figure 20, but this atmospheric evaporation drive system for generating electric power includes having the whirlpool of generator 6 Wheel 4 and the rotary regenerative heat and mass exchanger 62 with motor 63,62 conduct of turbine 4 and rotary regenerative heat and mass exchanger Two isolated systems.A part of the electric power of the generation of generator 6 of turbine 4 is connected to for motor 63.The motor 63 is used In the rotation of rotary regenerative heat and mass exchanger 62.Generator 6 is connect by electric wire 64 with motor 63.

It is worth noting that, the wet sector 60 of turbine 55 can be not only used for horizontal turbine 55 (referring to Figure 19 and figure 20), and it can be used for vertical turbine 55 (referring to fig. 2 2).Scheme for vertical turbine 55 (referring to fig. 2 2) is similar to Figure 19 With the scheme of horizontal turbine 55 shown in Figure 20.

It but the use of this atmospheric evaporation drive system that vertical turbine 55 generates electric power include to use the water 5 of fluid box 65 The wet sector 60 soaked, the rotor of vertical turbine 55 are dipped into fluid box 65.

This be generated for vertical turbine 55 another wet processes of wet sector 60 with.For this of vertical turbine 55 Kind of wet processes are simpler and cheap and good distribution that guarantee the water 5 in regrown material 56.

But it will not change heat and quality friendship between outside air 7 and control air 8 for horizontal turbine 55 Change the property of process.In this case, it is important that the correct rotation degree of selection vertical turbine 55.Slower rotation will lead to It is excessive and to lead to excessive drying due to evaporation to internal drainage, the total amount of evaporation can be reduced.Rotation faster is not The required time that is uniformly distributed can be provided, therefore the total amount of evaporation can be reduced.

As shown in figure 22, in control air 8 by bringing heat to be always advantageous for control air 8 during wet channel 3. The heat can come from any kind of exhaust gas or from solar radiation or both.

It also may include deflector 66 using the atmospheric evaporation drive system that vertical turbine 55 (referring to fig. 2 2) generate electric power, Deflector 66 is placed on the top in wet channel 3.It provides a possibility that energy using the wind 67 for blowing over wet channel 3. The energy can be used for generating air-flow in wet channel 3.The sky of the wind 67 passed through from any direction and between two surfaces Air-flow is retracted.Therefore, the speed of this air stream increases.As a result, the pressure of the stream declines.Therefore, on the top in wet channel 3 Portion generates suction.This air is pumped in wet channel 3 and generates air-flow.Therefore, it also by the partial regeneration of pressure energy come Increase the generating efficiency of proposed atmospheric evaporation drive system.

The proposed atmospheric evaporation drive system for generating electric power, cooling capacity and distilled water can have different inclinations Angle.Such as, the results showed that, for 200 millimeters of gaps and 1.5 meters of high systems, airflow rate is when system tilt angle is about 45 ° Reach maximum value, it is higher than perpendicular system by about 45% under otherwise identical conditions.Even if airflow rate is still than corresponding at 60 ° Perpendicular system is high by about 30%.Show that this flow velocity is increased the reason is that due to relatively uniform in atmospheric evaporation drive system Air speed, compared with corresponding perpendicular system, this significantly reduces the pressure losses of system entry and exit.

Figure 23 is the view for generating the atmospheric evaporation drive system 1 of electric power, and it includes turbine 4 and dew point indirect evaporative are cold But device 68 is used as two individual devices.

Sometimes it uses by Maisotsenko et al. in U.S. Patent No. 6,497,107；6,581,402；6,705,096 Described in dew point indirect evaporative cooler 68 come the (ginseng of rotary regenerative heat and mass exchanger 62 that replaces working together with turbine 4 See Figure 19) it is reasonable.The dew point indirect evaporative cooler 68 is comprising the dry channel 69 of oneself and wet channel 70 (referring to figure 23)。

Outside air 7 is guided to the dry channel 69 of dew point indirect evaporative cooler 68 by fan 71 first and is then drawn Lead wet channel 70.In this way, the outside air 7 in dry channel 69 can be in the ideal case by wet channel 70 Evaporation be cooled to dew-point temperature, heat exchange surface of the evaporation between dry channel 69 and wet channel 70 obtains Take latent heat.After through dry channel 69, a part of cold outside air 7 is extracted, and the rest part of the air-flow is made Continue in the wet channel 70 of dew point indirect evaporative cooler 68 for control air 8.By moistening channel 70, using from water 5 The moisture of evaporation gets wet control air 8, increases the humidity in its temperature and wet channel 70.It is extracted out from dry channel 69 cold Outside air 7 have high density, and in this case, it is directed into the evaporation drive system 1 before turbine 4 Dry channel 2.The control air 8 of warm saturation have after through the wet channel 70 of dew point indirect evaporative cooler 68 compared with Small density, and it is directed to the wet channel 3 of the evaporation drive system 1 in air movement direction after turbine 4.

The main drive of the electric power generated by atmospheric evaporation drive system 1 is directed to the cold external sky of turbine 4 Extra pressure of the gas 7 compared with the smaller pressure of the control air 8 of the warm saturation come out from the outlet of turbine 4.

Figure 23 a is identical as Figure 23, but this atmospheric evaporation drive system for generating electric power is also that consumer produces distilled water. The system includes additional condenser 100 for this purpose, and wet channel 70 is soaked by seawater 5.Cold outside air 7 exists First by dry channel 69 and then by being directed into condenser 100 after turbine 4.Here, cold outside air 7 with Heat exchange contact is carried out indirectly by the control air 8 of the wetting after drive system 1.Because of the temperature of cold outside air 7 Degree is always sufficiently below the temperature of the control air 8 of wetting, thus moisture from the control air 8 of the wetting in condenser 100 with The form of distilled water 37 condenses, and distilled water 37 is selected for consumer.After through condenser 100, the external sky of heating Gas 7 is conducted through turbine 4 and reaches drive system 1, and control air 8 is discharged into atmosphere.

It is proposed generate electric power, the atmospheric evaporation drive system of cooling capacity and distilled water have the advantages that it is very big, can Simply to adjust the distribution of final products according to its consumption.Electricity needs is with daily different time and difference weekly Date and change.Held very much when electricity needs is less, such as at night using proposed atmospheric evaporation drive system Cooling capacity more more than electric power easily generated or distilled water (or both).In this case it is advantageous to be driven using atmospheric evaporation The turbine 4 of system 1 is used as fan, for outside air 7 to be transported to wet channel 3 from dry channel 2 as control air 8 (for example, with reference to Fig. 3, Fig. 4 and Fig. 7).Under this effect, the generator 6 connecting with turbine 4 is used as the rotation electricity consumption of turbine 4 Motivation.

Carry out revolving wormgear 4 using in night cheap electric power, the dry channel 2 of atmospheric evaporation drive system 1 can be increased With the air-flow in wet channel 3.It improve atmospheric evaporation drive system 1 export cold (air or water) or distilled water (or both) Productivity.

It the use of the atmospheric evaporation drive system for generating electric power and distilled water is simultaneously that effectively, which utilizes natural force (gravity and atmospheric pressure) generates the vacuum for vacuum distillation.This scheme has the advantages that vacuum distillation, without Additional energy come make compressor generate vacuum.

This concept is proposed by Sharma and Goswami (referring to publication: Al-Kharabsheh and Yogi Goswami, " Analysis of an innovative water desalination system using low-grade Solar heat ", Desalination, 156,2003, p.323-332).Publication explanation: " atmospheric pressure is equivalent to by about The hydrostatic pressure that 10 meters (m) high of water column generates.Therefore, if a height is more than 10 meters and is full of from pillar with a closed top Water, and water is allowed to fall under gravity, it will fall on about 10 meters of height, generates vacuum in part above." However, although the water distillation system generates vacuum in the case where no compressor, realize here be not evaporation and it is cold Solidifying effective procedure.In addition, the system is needed using thermal energy needed for evaporation process, because it does not recycle the condensation of distillate Heat.Moreover, this traditional water distillation system for generating vacuum in the case where no compressor may not generate electric power.

Proposed invention passes through while using the energy source (also referred to as Psychrometric Energy) from atmosphere and natural air pressure To improve this known Distallation systm and enhance evaporation and condensation process.In addition, a possibility that the present invention provides uniquenesses, phase Natural engineering is used only in system mentioned-above for the application, generates more effectively for generating electric power and distilled water Atmospheric evaporation drive system.

Figure 24 is the flow chart for generating the atmospheric evaporation drive system 75 of electric power and distilled water 37 simultaneously.The system has two A separated part, they have heat exchange relationship: air part and water vapor portion.Here, wet in dry channel 2 and channel Moisten between 3 (air parts), is placed with 73 and of vacuum passage with salt water 5 being connected between adjacent and their own Condensation channel 74 (water vapour part), so that 73 one side of vacuum passage is in heat exchange relationship via plate 78 and dry channel 2, On the other hand heat exchange relationship is in via plate 80 and condensation channel 74.Meanwhile 74 one side of condensation channel via plate 79 with it is wet Profit channel 3 is in heat exchange relationship, is on the other hand in heat exchange relationship via plate 80 and vacuum passage 73.Atmospheric evaporation driving System 75 is also containing saline solution cassette for supplying 87 and its for the connecting tube of salt water 5；Case 83 and its connection is discharged in concentrated salt solution Pipe 84；Distilled water tank 85 and its connecting tube 86.

It is important that it is however emphasized that proposed atmospheric evaporation drive system 75 (referring to fig. 2 4) is by using natural force Vacuum is generated in vacuum passage 73 in the case where no compressor.The system includes more than ground at the height of about 10m Their own between (pass through steamturbine 4) between the vacuum passage 73 being connected and condensation channel 74 and their own The dry channel 2 and wet channel 3 that (passing through air turbine 4) is connected.In addition, vacuum passage 73 and condensation channel 74 are also corresponding Saline solution cassette for supplying 87, concentrated salt solution of the ground by pipeline 5,84 and 86 and all on the ground discharge case 83 and distilled water tank 85 connections.Balance supply pipe 5 and hydrostatic pressure in delivery pipe 84 and atmospheric pressure can generate vacuum.If the vacuum containing water Channel 73 and condensation channel 74 link together, then water will be from the distillation of the side of high steam pressure to the other side.At 0-100 DEG C Within the temperature range of, such as the steam pressure lower than the steam pressure of fresh water about 1.84% of seawater.This means that if vacuum is logical Road 73 (having salt water 5) connects while keeping mutually synthermal from top with condensation channel 74 (having distilled water 37), then water It will distill from dilute side to brine side.It (is being condensed to keep water to distill from salt water 5 (in vacuum passage 73) to distilled water 37 In channel 74), the steam pressure of the salt water 5 in vacuum passage 73 preferably must be held in the steam of the distilled water 36 in condensation channel 74 On pressure, method is that the salt water 5 in vacuum passage 73 is maintained at higher temperature.In known conventional method and system In, this can be completed by using additional heat, for example, using solar energy.Proposed invention does not need this Additional heat, and can effectively work in the case where no additional heat.In this case, in outside air 7 By the way that necessary heat is discharged from outside air 7 (passing through plate 78) during dry channel 2, (pass through plate 80) simultaneously from condensation channel 74 are discharged necessary heat to vacuum passage 73 for salt water 5 with distilled water 37.These heat rejection process guarantee vacuum passage 73 In the steam pressure of salt water 5 will remain on the steam pressure of the distilled water 37 in condensation channel 74.It is of course also possible to make With additional heat, for example, using solar energy by solar collector.The efficiency of the system can be improved in this, but needs volume Outer cost of equipment.

Outside air 7 is directed to dry channel 2 (referring to fig. 2 4).Across the dry channel of the drying side contacts with plate 78 When 2, air-flow 7 is cooled, and the temperature for the vapor 76 for being reduced to its temperature from environment temperature in substantially vacuum passage 73 is (low In dew-point temperature), while reducing the absolute humidity of air-flow 7.In subsequent 7 precooling process of air-flow, entire air-flow 7 leads to from dry Road 2 is reintroduced through air turbine 4 and reaches wet channel 3 as control air 8.

Cold air 7 by dry channel 2 from High aititude Doenward flow to low altitude area because cold air is heavier and its density Greater than the density of outside air.Cold air 7 improves its density and sinks, and generates inverse stack effect.Cold outside air 7 is with high speed Rate flows in dry channel 2, provides power to be connected to the air turbine 4 of generator 6, and escape into as control air 8 Wet channel 3.Hereafter (referring to fig. 2 4), control air 8 flow to High aititude from low altitude area rising by wet channel 3.Work Air 8 is contacted with moist surface 79 and 81, and moist surface 79 and 81 is, for example, to wick plastics or capillary porous material, is evaporated Liquid (such as water 72 or distilled water 37) or saline solution 5 soak.When control air 8 along wet channel 3 by when, it is heated, Wetting and its density get lower than the density of outside air.Therefore, the control air 8 for heating and soaking is lighter and will be wet Moisten in channel 3 and rise, generates stack effect.

When across dry channel 2 (referring to fig. 2 4), outside air 7 is that vacuum passage 73 brings heat by plate 78.This has Help the evaporated vapor 76 from the saline solution 5 in vacuum passage 73.By the pressure of the steam 76 in Raise vacuum channel 73, Its saturation temperature also increases and the density of steam 76 is lower.Therefore, steam 76 is lighter and will rise in vacuum passage 73, Generate stack effect.

Steam 76 flow to High aititude from low altitude area rising with high-speed by vacuum passage 73, to be connected to generator 6 Steamturbine 4 power is provided, and escape into condensation channel 74 as steam 77, steam 77 is condensed in condensation channel 74.

The condensation heat of steam 77 is discharged into wet channel 3 via plate 79 from condensation channel 74 by control air 8, and work is empty Gas 8 is by evaporation latent heat by moistening channel 3.Meanwhile the condensation heat of steam 77 passes through evaporated salt water solution 5 from condensation channel 74 Vacuum passage 73 is discharged into via plate 80.Therefore, condensation channel 74 has dual-cooled process, this is improved in condensation channel 74 Steam 77 cooling and condensation process efficiency.These processes reduce the pressure in condensation channel 74, and due to steam 77 is heavier, it is from High aititude Doenward flow to low altitude area.Steam 77 improves its density and sinks, and generates inverse stack effect.

Because the control air 8 and above-mentioned condensation channel 74 in wet channel 3 are in heat exchange relationship, thus moisture is cold It is condensed in the form of distilled water 37 from steam 77 in solidifying channel 74, distilled water 37 is selected for consumer.

It therefore, the use of advanced air evaporation cooling procedure (air part) is that effectively, the process by being mentioned herein Method and system and water steam (water vapor portion) out combines, and generates electric power and distillation simultaneously using vacuum distillation process Water.It is generated by the more cold and dry air-flow 7 of the generation in dry channel 2 and in wet channel 3 warmer and wet Control air 8, a possibility that it provides uniqueness, to dramatically increase in air part in dry channel 2 and wet channel 3 Density variation between air-flow, temperature can be cooled to lower than dew-point temperature in dry channel 2.Therefore, it, which is increased, passes through It can transport electric power obtained by air turbine 4.

Meanwhile it can produce in water vapor portion using proposed system by generating cooling capacity and distilled water 37 Density contrast in vacuum passage 73 in vapor 76 and condensation channel 74 between steam 77.This provides raw by steamturbine 4 At the chance of obtainable additional transportable electric power and generation distilled water 37.The vacuum evaporation of salt water 5 in vacuum passage 73 is cold But process (generating cooling capacity) and the condensation process (generating condensation heat) of the steam 77 in condensation channel 74 also increase air part Density contrast between middle air-flow 7 and 8.

Only by keeping the vapor in condensation channel 74 cooling to make by the low-temp low-pressure surrounding air under High aititude There is vapor to be condensed into liquid water, partial vacuum can be completed in vacuum passage 73 at High aititude.

Therefore, the height of proposed atmospheric evaporation drive system is higher, the electric power of generation, cooling capacity and distilled water It measures bigger.

Described atmospheric evaporation drive system is also used as thermoelectric generator, for being based on the temperature difference in day and night Additional electric energy is generated simultaneously.Herein, there is the temperature difference always between the dry-bulb temperature and dew-point temperature of outside air.Therefore, It is warm that proposed atmospheric evaporation drive system, which always has some positions, and other positions are then cold.If will Thermoelectric material is arranged in these positions, then thermal gradient is converted directly into electric energy by Seebeck (thermoelectricity) effect.The electricity of generation Pressure and power are proportional to the Seebeck coefficient of temperature difference and thermoelectric material.Big thermal gradient for generate practicability voltage and Power level is essential (for example, with reference to U.S. Patent number 6,613,972 and 6,673,996).

The present invention provides by generating cold and dry air in dry channel come a possibility that dramatically increasing temperature difference, Temperature can be cooled to dew-point temperature in the ideal case in dry channel, and the dew-point temperature is than the wet bulb temperature in known devices Spend much lower (especially for dry climate).

Thermocouple configuration is to be more suitable for the method for power generation.Such configuration includes the N-shaped and p being connected electrically at hot end Profile material.Commonly used in thermoelectric energy conversion some thermoelectric materials include Sb2Te3, Bi2Te3, Bi-Sb, PbTe, Si-Ge, Polysilicon, BiSbTeSe compound and InSbTe.

As described above, when control air and/or evaporating liquid before the wet channel for entering pipeline or passing through pipeline When being heated during wet channel, system is effective.The source of this heat is also possible to underground heat or/and soil heat source.

Figure 25 is the schematic cross sectional views for generating the atmospheric evaporation drive system of electric power, uses underground heat or/and Soil Thermal Source.One advantage of the system is in winter, when the soil moisture of some depth of underground is higher than the temperature of outside atmosphere.This In the case of, proposed atmospheric evaporation drive system 1 is inserted into soil 93 (soil) to use underground heat or/and Soil Thermal Source.Here, entire outside atmosphere cold airflow 7 is by after dry channel 2, is reintroduced as control air 8 as from dry Dry channel 2 passes through turbine 4 to wet channel 3, for generating electric power.

The atmospheric evaporation drive system (referring to fig. 2 5) may include that external heat sink 94 (has temperature T₁), dew point radiator 95 (have temperature T_dp) and soil radiator 96 (have temperature T_s), they are placed in corresponding region.

Here: T₁For the temperature of outside atmosphere；T_dpFor the dew-point temperature and T of outside atmosphere_sFor soil (soil) temperature.

Due to T₁/T_dp/T_sThe temperature difference can fluctuate between summer and winter and between night and daytime, therefore hardly It is zero.Therefore always there are some energy for harvest.

Here it is this atmospheric evaporation drive system is reasonably used as thermoelectric generator to generate simultaneously additionally annual The reason of electric energy (referring to fig. 2 5).For this purpose, it is necessary to which thermoelectric material is arranged in these radiators 94,95 and 96.Herein The thermoelectric device proposed will use the natural temperature differential between the dry-bulb temperature of atmospheric air and dew-point temperature and the soil moisture To collect electric energy.Different from photovoltaic cell, process proposed herein and system can operate in the case where no sunlight.This The main attractive for the system that text is proposed is characterized in high reliability, because it does not include moving parts.Either atmosphere ratio Soil warm (such as summer) or soil are warmer than air (such as winter): simply by the presence of the T of non-zero₁/T_dp/T_sThe temperature difference [may It is (T₁-T_dp) or (T_s-T_dp) or (T₁-T_s)], heat will pass through system and generate electric power.

The proposed method for generating electric power to being required in the consumption of water because it to realize evaporation cooled Journey.For this purpose, any kind of water can be used, including waste water or seawater, it, can be by it by proposed invention It is converted into the drinking water of distillation.

But, if it is possible that proposed invention is used to generate electric power without the climate zone of any water at all?

Water forever with we, water is all over the world.Any cloud is all perfect water source.

In fact, being assessed according to feasibility study, the cross section that cloud may generate a large amount of water-usually cloud is about 1 Square kilometre, it can supply water for up to 1,000,000 people.For the proposed method for generating electric power, it is reasonable to directly The wet processes in the wet channel 3 of pipeline 1 are carried out using the water of cloud from sky.

Figure 26 is by the schematic sectional of the atmospheric evaporation drive system of the generation electric power of the water realization directly from cloud Figure.

In such a case it is necessary to add such top on pipeline 1, which will collect cloud water in mesh 18 Drop.Water droplet will flow downwards to reservoir 19 and hose 20, reach the wet channel 3 of pipeline 1.In order to support cloud collector (netted Object 18), use captive balloon 21 and rope 22.Therefore, the surface 15 inside channel 3 is moistened by the water wetting directly from cloud. The water is moved as the mobile film 16 of liquid along surface 15 from the top to the bottom.

Solar column is also applied for using the concept that solar radiation generates electricity.Solar column is run with following simple principle: Hot-air rises；The movement of the hot-air of rising is used to driving turbine generation.

Solar column is by converting electricity for the thermal energy of the sun, thus with competitive renewable energy price next life At electric power.

The radiation of the sun under the collecting region of expansion for heating a large amount of air, then by physical law (on hot-air Rise) force the air being heated as the mobile turbine that passes through of hot wind to generate electricity.Solar column power station will create conditions, and make hot wind Pressure classification turbine is continued to flow through to generate electricity.

Solar column technology is taught by the leading structural engineer of GermanyDesign (referring to his book,The Solar Chimney, Edition Axel Menges, Stuttgart, 1995),It is also that the original of famous Structural Engineering company Schlaich Bergermann and Partners is formed a partnership People (more information in relation to Schlaich Bergermann and Partners, please access their website: www.sbp.de).

EnviroMission, Ltd. are the maximum cleaning green regenerative energy sources manufacturers using solar column technology. Solar column technology is developed to business level by the said firm, and the viable alternatives as fossil fuel power (access theirs Website: www.enviromission.com.au)

But there are following critical defects for existing solar column technology:

1. solar column possibly can not daytime and evening continuous work, and can only be in sun-drenched time service.

2. driving turbine generation using the movement of the hot-air of rising in solar column.Certainly, the density of the hot-air Less than the density of outside air, but this density contrast is too small and turbine on pressure drop (between the entrance and exit of turbine Pressure difference) also very little.

3. using known solar column, it is impossible to efficiently and economically realize and capture carbon dioxide and simultaneously from air Generate electric power, cooling capacity and distilled water.

4. next emphasizing that the monthly energy output of traditional solar column is different, and depend on the temperature of solar radiation Degree.This species diversity (such as between January and June) may differ by more than 10 times.This is serious disadvantage.

The proposed atmospheric evaporation drive system for generating electric power has stable monthly energy output in whole year.? Summer can obtain lesser air in wet channel when solar radiation is high and the absolute humidity of outside air is also high Density.In winter, it when solar radiation very little and the absolute humidity also very little of outside air, can be obtained in dry channel Bigger atmospheric density.Under any circumstance, the pressure on turbine (or density) difference will not actually change.

The advantages of in order to illustrate proposed atmospheric evaporation drive system, the system realize disclosed generation electricity The method of power, cooling capacity and distilled water, applicant compare system claimed and known energy herein using air line chart Source tower (for example, with reference to Dan Zaslavsky et al., United States Patent (USP) No.6,647,717) and known solar column.

Proposed atmospheric evaporation drive system is named as by we "Tower ".

Figure 26 show it is disclosed "The air line chart of the process of tower " and known energy tower and solar column.

The main drive of tower, energy tower or solar column power generation (E) is the list of air between turbine inlet and outlet The function of bit density difference Δ ρ or unit bodies product moment Δ v:

E=F (Δ ρ)=Fi (Δ v).

?All under the same conditions, we will be in air line chart for the outside air parameter of tower, energy tower and solar column It is middle to establishThe process (referring to fig. 2 6) realized in tower, energy tower or solar column.

For example, the temperature of outside air is 95 °F, absolute humidity is 0.04W (lbm/lbm) -1,5 and 7.

“Tower " realizes Maisotsenko circulation: process 1-2-3-4 (red), middle line 1-2 are heating process, example Such as, pass through solar radiation；Line 2-3 is the cooling procedure in dry channel, and line 3-4 is in wet channel while to be added Wet and heating process.

Solar column realizes process (blue), and middle line 5-6 is heat by solar radiation process.

Energy tower realizes process (black), and middle line 7-8 is adiabatic humidiflcation process.

ForTower, the air unit bodies product moment between turbine inlet and outlet are as follows: Δ v=V₄-V₃；

For solar column, air unit bodies product moment is: Δ v=V₆–V₅；

For energy tower, air unit bodies product moment is: Δ v=V₇–V₈；

As can be seen from Figure 26, proposedAir unit bodies product moment between the turbine inlet and outlet of tower (Δ v=V₄–V₃) air unit bodies product moment (the Δ v) greatly (many times larger) more than solar column and energy tower.In addition, this Kind advantage is with entranceThe raising of the temperature of the outside air of tower and the reduction of moisture and increase.

In addition, proposedTower can not only produce electric power, can also produce cheap cooling capacity and distilled water.It passes The solar column and energy tower of system then cannot.

1. a kind of method for generating electric power using atmospheric evaporation drive system, comprising: atmosphere air-flow is made to pass through the dry of pipeline Dry channel, wherein air-flow is pre-chilled by the drying side contacts with surface in the case where not changing the absolute humidity of air-flow, Another wet side evaporated liquid (such as water) on the surface in wet channel or saline solution wetting, and then in the atmosphere Its temperature is reduced to substantially by air-flow in the advance Doenward flow in dry channel from High aititude to low altitude area from environment temperature The upper dew-point temperature for outside air；

Wherein, in subsequent air-flow precooling process, entire atmosphere cold airflow is reintroduced with logical from the drying of pipeline Road generates electric power by turbine to wet channel, and evaporation liquid is directly contacted as control air, evaporates liquid as thin Film or mobile film, are covered by the wicking layer of the wet side on surface, wherein control air with the moisture of evaporation liquid evaporation and It moisturizes；Between atmosphere air-flow and same airflow as control air, the air-flow first pass through dry channel pass through again it is wet The process in channel, indirect heat exchange respectively occurs via surface, to then improve in wet channel from low altitude area to height The advance of height above sea level rises the temperature and water capacity of control air in flowing, is then discharged into heating and moist control air greatly Gas；And

Wherein, control air and/or evaporation liquid before the wet channel for entering pipeline or are passing through the wet of pipeline It is for example heated by solar radiation during channel.

2. the method according to claim 1 for generating electric power and cold air simultaneously using atmospheric evaporation drive system, Wherein after through turbine, a part of atmosphere cold airflow is extracted and is used as the cold source of consumer.

3. the side according to claims 1 and 2 for generating electric power and cold liquid simultaneously using atmospheric evaporation drive system Method wherein evaporation liquid such as water covers the wet side on surface as mobile film, and is taken out after it is by wet channel Out and be used as consumer cold source.

4. the method according to claim 1 to 3 for generating electric power and cooling capacity simultaneously using atmospheric evaporation drive system, Wherein if the absolute humidity of exhaust uptake gas is less than or equal to the absolute humidity of outside air, control air and/or evaporation Liquid is directly heated before the wet channel for entering pipeline or during the wet channel by pipeline by exhaust uptake gas.

5. the method according to claim 1 to 3 for generating electric power and cooling capacity simultaneously using atmospheric evaporation drive system, Wherein if the absolute humidity of exhaust uptake gas is greater than the absolute humidity of outside air, control air and/or evaporation liquid exist Into before the wet channel of pipeline or during through the wet channel of pipeline by exhaust uptake gas indirect heating.

6. the side according to claim 1 to 3 for generating electric power and distilled water simultaneously using atmospheric evaporation drive system Method, wherein wet channel is soaked by saline solution, and the system includes condensation channel, and the one of the control air of heating and humidity Part is extracted after through wet channel and is directed to the condensation channel as condensation air；This condensation air is logical in condensation It is cooled to substantially in advance Doenward flow in road from High aititude to low altitude area by the drying side contacts with surface Another wet side of the dew-point temperature of outside air, the surface is soaked by saline solution, since condensation air is moistened with above-mentioned There is heat exchange relationship in channel, and moisture is condensed in the form of distilled water from the condensation air inside condensation channel, and the distilled water is Consumer's selection, and the condensation air is conducted through turbine to generate electric power later.

7. the method according to claim 6 for generating electric power and distilled water simultaneously using atmospheric evaporation drive system, Wherein condense the cold source that air and/or distilled water were extracted and were used as consumer after through condensation channel.

8. the method for generating electric power and cooling capacity using atmospheric evaporation drive system described in -7 according to claim 1, wherein These systems be made into connection, thin-walled, expandable rising ring pipe, dry channel and wet logical is placed inside the pipe Road, and heat exchange mechanism is constantly present between dry channel and wet channel.

9. generating the side of electric power, cooling capacity and distilled water described in -8 using atmospheric evaporation drive system according to claim 1 Method, wherein these systems be made into connection, thin-walled, expandable rising ring pipe, placed inside the pipe dry channel, Wet channel and condensation channel, in addition, any wet channel is all located between dry channel and condensation channel, and between them It is constantly present heat exchange mechanism.

10. generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system according to claim 8 and 9 Method, wherein evaporation drive system includes balloon and connection cables, for keep and support at High aititude have dry channel, The pressurization in wet channel and condensation channel may expand tedge.

11. the side according to claim 10 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system Method, wherein balloon has double wall, is used to form condensation space, which has the heat exchanger with external atmospheric air System；And it heats and the control air of wetting is directed into the condensation space after through wet channel, therefore, moisture is to distill The form of water is condensed from the control air in condensation space, which is conveyed downwardly through hydroturbine and is supplied to consumption Person.

12. generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system according to claim 8 and 9 Method, wherein connect, thin-walled, expandable tedge be set and be attached to the side on mountain, the upper end is located on mountain At High aititude, and at the low altitude area that is situated at the foot of a hill of its lower end, or be set or be attached to any kind of building or The side of tower.

13. generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system described in -12 according to claim 1 Method, wherein having more than one set of dry channel, wet channel and condensation channel in the duct, in addition, any wet channel all positions Between dry channel and condensation channel, and between any wet channel and any dry channel and any wet channel There is heat exchange mechanism always between any condensation channel.

14. generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system described in -13 according to claim 1 Method, wherein evaporation drive system includes water jacket, the water jacket is for heating water or saline solution by solar radiation, water Or saline solution is assigned to the top in wet channel 3 from water jacket, wet channel 3 is moistened from top to bottom by the mobile moisture film of heat It is wet.

15. the side according to claim 14 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system Method, wherein the outer surface of water jacket is covered or covered using other materials by black coating, these materials good can absorb too The heat of sun radiation.

16. generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system described in -13 according to claim 1 Method, wherein evaporation drive system includes separated solar water heater, for water-soluble to water or salt by solar radiation Liquid is heated, and water or saline solution are assigned to the top in wet channel 3 from solar water heater, is moistened channel 3 and is moved by heat Hydrodynamic body thin film is soaked from top to bottom.

17. generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system described in -16 according to claim 1 Method, wherein evaporation drive system includes water jacket and separated solar water heater, for by solar radiation to water or Saline solution is heated, and water or saline solution are assigned to the top in wet channel 3 from water jacket and solar water heater, is moistened Channel 3 is soaked from top to bottom by the mobile fluid film of heat.

18. generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system described in -17 according to claim 1 Method, wherein evaporation drive system includes the absorber coatings of dry channel, such as limewash, the absorber coatings are by dry logical Extract carbon dioxide during road out from outside air.

19. generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system described in -17 according to claim 1 Method, wherein evaporation drive system includes the absorber coatings of dry channel, such as liquid drier, the absorber coatings are by dry Vapor is extracted out from outside air during dry channel.

20. the side according to claim 5 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system Method, wherein evaporation drive system includes the absorber coatings of exhaust passage, such as limewash, the absorber coatings are passing through exhaust passage Period extracts carbon dioxide out from exhaust uptake gas.

21. generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system described in 9 and 20 according to claim 1 Method, wherein evaporation drive system includes the absorber coatings of dry channel, the absorption of such as liquid drier, dry channel is applied Layer by extract vapor out from outside air during dry channel, and evaporate drive system also include exhaust passage suction Coating, such as limewash are received, dioxy is discharged from exhaust uptake gas during through exhaust passage in the absorber coatings of exhaust passage Change carbon.

22. generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system described in 9 and 21 according to claim 1 Method, it is weak to this after dry channel for passing through in weak absorbing agent wherein evaporation drive system includes solar generator Absorbent is recycled.

23. the side according to claim 22 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system Method, wherein solar generator include:

Make dry channel of the atmosphere air-flow by solar generator, air-flow passes through dry with surface in the dry channel Dry side contacts and be pre-chilled, another wet side on the surface in wet channel is by the weak of the bottom of the dry channel from pipeline Absorbent wetting, is then reduced to substantially dew-point temperature from environment temperature for absorbent temperature, then by air-flow from solar energy The dry channel of generator is re-directed to the wet channel of solar generator, directly to contact absorbent, absorbent conduct Mobile film is covered by the wicking layer of the wet side on surface, and wherein air-flow is got wet with the moisture evaporated from absorbent, wet Profit increases its temperature and humidity in channel, and air-flow in wet channel by heat by solar radiation, then, will heating and moist Air-flow be discharged in atmosphere or the wet channel of guide duct, strongly with cold absorbent after through wet channel back to pipe The top of the dry channel in road.

24. generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system described in -23 according to claim 1 Method adjusts and is divulged information for the natural air in building, and certain parts of outside air are in the drying by pipeline Behind channel, be extracted and be used for through the access road introducing interior space as cold and dry air, room air certain A little parts are retracted to the wet channel of pipeline by gravity-flow ventilation from the interior space.

25. generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system described in -24 according to claim 1 Method, wherein evaporation drive system includes the water jet for turbine, which is made into rotary regenerative heat and mass exchanger, The heat and mass exchange process between outside air and control air are realized at the turbine, also to transmit between these air-flows Heat and cooling capacity.

26. the side according to claim 25 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system Method, wherein turbine is mounted on the bottom of pipeline, for the entrance outside air of heat exchange and the dry channel of export air It is connected at the bottom of pipeline with wet channel, and turbine includes rotor, rotor is continuous by outside air and control air Ground rotation, and outside air and control air flow through a series of blades by axial groove with high-speed, to be connected to generator Turbine provide power, and rotor include regrown material, and these channels rotor either end have opening, for drawing For the outside air and control air for leading separation by regrown material, regrown material includes point for outside air and control air From entrance sector and exhaust sector, wherein regrown material evaporated liquid (such as water) wetting wet sector be added to row Gas sector, and entrance outside air is guided first by entrance sector, and export is used as after turning to 180 ° Air passes through the wet sector of regrown material.

27. generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system according to claim 25 and 26 Method, wherein dry channel is more shorter than wet channel.

28. generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system according to claim 25-27 Method, wherein evaporation drive system includes the turbine with generator and the rotary regenerative heat and mass exchanger with motor As two individual devices.

29. generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system according to claim 25-28 Method, wherein evaporation drive system includes turbine, which is made into vertical rotary regenerative heat and mass exchanger, at the turbine The heat and mass exchange process between outside air and control air are realized, to transmit heat and cold between these air-flows Amount.

30. the side according to claim 29 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system Method, wherein vertical turbine includes wet sector, soaks the wet sector by water using fluid box, the rotor of vertical turbine immerses liquid In body case.

31. generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system according to claim 25-30 Method, wherein control air during wet channel by being heated.

32. the side according to claim 31 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system Method, wherein control air passes through heat by solar radiation.

33. generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system described in -32 according to claim 1 Method, wherein wet channel includes wind deflector.

34. generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system described in -33 according to claim 1 Method, wherein evaporation drive system can be made with different inclinations angle.

35. the side according to claim 34 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system Method, wherein the inclination angle of evaporation drive system is about 45 °.

36. generating electric power, cooling capacity using atmospheric evaporation drive system described in -24,27 and 30-35 according to claim 1 With the method for distilled water, individually filled wherein evaporation drive system includes turbine and dew point indirect evaporative cooler as two It sets, furthermore the cooler realizes the humidification that outside air is down to the substantially cooling procedure of its dew-point temperature and control air Process, and after this, cold outside air is directed into the evaporation driving on the direction of air movement before the turbine The dry channel of system, and warm saturation control air is directed into the wet logical of the evaporation drive system after turbine Road.

37. the side according to claim 36 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system Method wherein evaporation drive system carries out the wet processes of dew point indirect evaporative cooler using seawater, and includes additional condensation Device, in the condenser, the control air of cold outside air and wetting is guided as a result to condense for indirect heat exchange contact Distilled water be directed to consumer.

38. the method for generating cooling capacity and distilled water using atmospheric evaporation drive system described in -35 according to claim 1, Wherein the turbine of atmospheric evaporation drive system is used as to be transported to as the outside air of control air from dry channel wet The fan in channel, the generator connecting thus with turbine are used as the motor of turbine rotation.

39. the method for generating electric power using atmospheric evaporation drive system described in -38 according to claim 1, wherein evaporating Liquid evaporates liquid, such as ammonia or water-ammonia mixture using low boiling point, and it is wet as mobile film covering that low boiling point evaporates liquid The wet side on the surface in channel.

40. the method according to claim 39 for generating electric power using atmospheric evaporation drive system, wherein wet After channel interior low boiling point evaporates liquid evaporation into control air, control air is guided so that steam is cold from the air It is solidifying, return to condensed fluid then to soak wet channel.

41. the method for generating electric power using atmospheric evaporation drive system according to claim 39 and 40, wherein making It is located at the High aititude on mountain with the upper end of the side of balloon or mountain at high tower or High aititude, system, what lower end was situated at the foot of a hill At low altitude area, for condensing low boiling point evaporation liquid.

42. according to claim 6-18,24 and 31-37 using atmospheric evaporation drive system simultaneously generate electric power and The method of distilled water, wherein using the vertical downward flow of the distilled water from condensation channel to drive hydroturbine to generate additional electricity Power.

43. generating electricity simultaneously using atmospheric evaporation drive system according to claim 6-18,24,31-37 and 42 The method of power and distilled water, outside air is by being reintroduced after dry channel, so as to from dry channel to wet Channel generates electric power by air turbine, wherein saline solution is added in vacuum passage, vacuum passage is adjacent with condensation channel And connect via steamturbine with condensation channel, in addition, the two channels are all placed between dry channel and wet channel, make It obtains vacuum passage to be used for there are heat exchange mechanism to vacuum passage heat supply via plate and dry channel, and vacuum passage passes through There are heat exchange mechanism, condensation channel is in heat exchange simultaneously also by third plate and wet channel for another block of plate and condensation channel Relationship, for heat to be discharged from condensation channel；In addition, vapor is evaporated from the saline solution inside vacuum passage, and Advance inside vacuum passage from low altitude area to High aititude and rise flowing, is then rebooted vapor from true by creating vacuum Empty channel to condensation channel by steamturbine to generate electric power, the vapor in condensation channel from High aititude to low altitude area before Into Doenward flow, the vapor is decreased its temperature and is condensed in the form of distilled water in condensation channel, thus to disappear The person's of expense selection.

44. the side according to claim 43 for generating electric power and distilled water simultaneously using atmospheric evaporation drive system Method, wherein, using the distilled water from condensation channel, the distilled water is capped as film or mobile film for moistening channel Wicking layer in the wet side of plate, these plates form wet channel.

45. generating electric power and distilled water simultaneously using atmospheric evaporation drive system according to claim 43 and 44 Method, wherein saline solution is selected and used as the cold source of consumer after through vacuum passage.

46. generating electric power and distilled water simultaneously using atmospheric evaporation drive system according to claim 42-44 Method, wherein selecting the distilled water from condensation channel and being used as the cold source of consumer.

47. generating electric power and distilled water simultaneously using atmospheric evaporation drive system according to claim 43-46 Method, wherein the vacuum passage with saline solution is connect by steamturbine with condensation channel, the vacuum in vacuum passage is logical Crossing will generate at all channels arrangement above ground level about 10 meters of height, these channels are connected to vacuum passage by pipeline Saline solution source and concentrated salt solution discharge at and condensation channel distilled water tank, saline solution source, concentrated salt solution row Place and distilled water tank are put all on ground level.

48. generating electric power, cooling capacity and distillation simultaneously using atmospheric evaporation drive system described in -47 according to claim 1 The method of water, wherein entire atmosphere cold airflow is used as the cold of consumer after passing through dry channel first and passing through turbine again Source, then the atmosphere air-flow after entire heating is re-directed to the wet channel of pipeline as control air.

49. generating electric power, cooling capacity and distillation simultaneously using atmospheric evaporation drive system described in -48 according to claim 1 The method of water, wherein the system includes the individual turbine for being used to generate electric power for being directed to outside air and control air respectively.

50. generating electric power, cooling capacity and distillation simultaneously using atmospheric evaporation drive system described in -49 according to claim 1 The method of water, wherein passing through after dry channel passes through turbine again first in atmosphere cold airflow, a part of atmosphere cold airflow is made It is re-directed to wet channel from dry channel for control air, and another part of the air-flow is extracted and draws as cold air It leads to consumer.

51. generating electric power, cooling capacity and distillation simultaneously using atmospheric evaporation drive system described in -50 according to claim 1 The method of water, wherein a part of atmosphere cold airflow is drawn as control air from dry channel again after through dry channel Wet channel is led, moistening channel includes oneself independent turbine, and another part of the atmosphere cold airflow is extracted and is used for Atmosphere is discharged into after generating electric power by turbine.

52. generating electric power, cooling capacity and distillation simultaneously using atmospheric evaporation drive system described in -51 according to claim 1 The method of water, wherein the system is inserted into soil, using underground heat or/and soil heat source to generate thermoelectricity and using earth atmosphere In air as working fluid.

53. generating electric power, cooling capacity and distillation simultaneously using atmospheric evaporation drive system described in -52 according to claim 1 The method of water, wherein including mesh and storage for conveying the water directly from cloud to soak the system in the wet channel of pipeline Device, reservoir are connect by hose with wet channel, which further includes the balloon and rope for supporting the system in the sky.

Claims

1. a kind of method for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, comprising:

A) make dry channel of the atmosphere air-flow by pipeline, wherein the air-flow in the case where not changing the absolute humidity of air-flow It is pre-chilled by the drying side contacts with surface, another wet side on the surface in wet channel is by the evaporation comprising water Liquid or saline solution wetting, and the then advance decline in the atmosphere air-flow in dry channel from High aititude to low altitude area Its temperature is reduced to the dew-point temperature of substantially outside air in flowing from environment temperature；

B) wherein, in subsequent air-flow precooling process, entire atmosphere cold airflow is reintroduced with from the dry channel of pipeline Electric power is generated by turbine to wet channel, and directly contacts evaporation liquid as control air, evaporates liquid as film Or mobile film, it is covered by the wicking layer of the wet side on the surface, wherein the control air is steamed with evaporation liquid The moisture of hair and moisturize；Between atmosphere air-flow and same airflow as control air, which first passes through dry channel Again by moistening channel, the process of indirect heat exchange respectively occurs via surface, thus then improve in wet channel from Low altitude area rises the temperature and water capacity of control air in flowing to the advance of High aititude, then by heating and the moist work Atmosphere is discharged into as air；And

C) wherein, the control air and/or evaporation liquid before the wet channel for entering pipeline or are passing through the wet of pipeline Profit is heated during channel by heat source, and the heat source includes solar radiation.

2. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, wherein After through turbine, a part of atmosphere cold airflow is extracted and is used as the cold source of consumer.

3. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, wherein Liquid such as water is evaporated, as mobile film, covers the wet side on surface, and be extracted simultaneously after it is by wet channel Cold source as consumer.

4. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, wherein If the absolute humidity of exhaust uptake gas is less than or equal to the absolute humidity of outside air, the control air and/or evaporation Liquid is directly heated before the wet channel for entering pipeline or during the wet channel by pipeline by exhaust uptake gas.

5. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, wherein If the absolute humidity of exhaust uptake gas is greater than the absolute humidity of outside air, the control air and/or evaporation liquid exist Into before the wet channel of pipeline or during through the wet channel of pipeline by exhaust uptake gas indirect heating.

6. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, wherein Wet channel is soaked by saline solution, and the system includes condensation channel, and a part of heating and moist control air exists By being extracted behind wet channel and being directed to the condensation channel as condensation air；This condensation air in condensation channel from High aititude is cooled into the advance Doenward flow of low altitude area by the drying side contacts with surface substantially external empty Another wet side of the dew-point temperature of gas, the surface is soaked by saline solution, since condensation air has with above-mentioned wet channel Heat exchange relationship, moisture are condensed in the form of distilled water from the condensation air inside condensation channel, and the distilled water is consumer Selection, and the condensation air is conducted through turbine to generate electric power later.

7. the method according to claim 6 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, wherein The condensation air and/or distilled water are extracted and are used as the cold source of consumer after through condensation channel.

8. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, wherein These systems be made into connection, thin-walled, expandable rising ring pipe, dry channel and wet logical is placed inside the pipe Road, and heat exchange mechanism is constantly present between dry channel and wet channel.

9. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, wherein These systems be made into connection, thin-walled, expandable rising ring pipe, dry channel, wet logical is placed inside the pipe Road and condensation channel in addition, any wet channel is all located between dry channel and condensation channel, and are always deposited between them In heat exchange mechanism.

10. the method according to claim 8 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle evaporation drive system includes balloon and connection cables, is used to keep and support at High aititude have dry channel, moisten and lead to The pressurization of road and condensation channel may expand tedge.

11. the method according to claim 10 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle balloon has double wall, is used to form condensation space, which has the heat exchange mechanism with external atmospheric air；And And the control air of heating and wetting is directed into the condensation space after through wet channel, therefore, moisture is with distilled water Form is condensed from the control air in condensation space, which is supplied to consumer by hydroturbine is conveyed downwardly through.

12. the method according to claim 8 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle connection, thin-walled, expandable tedge be set and be attached to the side on mountain, the upper end is located at the High aititude on mountain Place, and at the low altitude area that is situated at the foot of a hill of its lower end, or it is set or is attached to the side of any kind of building or tower Face.

13. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, In have more than one set of dry channel, wet channel and condensation channel in the duct, in addition, any wet channel be all located at it is dry logical Between road and condensation channel, and between any wet channel and any dry channel and any wet channel and any cold There is heat exchange mechanism always between solidifying channel.

14. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle evaporation drive system includes water jacket, the water jacket for being heated by solar radiation to water or saline solution, the water or Saline solution is assigned to the top in the wet channel 3 from the water jacket, which moves moisture film from top to bottom by heat It is soaked.

15. the method according to claim 14 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, The outer surface of middle water jacket is covered or covered using other materials with the heat for absorbing solar radiation by black coating.

16. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle evaporation drive system includes separated solar water heater, for being added by solar radiation to water or saline solution Heat, the water or saline solution are assigned to the top in the wet channel 3, the wet channel from the solar water heater 3 are soaked from top to bottom by the mobile fluid film of heat.

17. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle evaporation drive system includes water jacket and separated solar water heater, for passing through solar radiation to water or saline solution It is heated, the water or saline solution are assigned to the wet channel 3 from the water jacket and the solar water heater Top, the wet channel 3 are soaked from top to bottom by the mobile fluid film of heat.

18. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle evaporation drive system includes the absorber coatings of the dry channel, and such as limewash, the absorber coatings are by described dry Carbon dioxide is extracted out from outside air during dry channel.

19. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle evaporation drive system includes the absorber coatings of the dry channel, such as liquid drier, and the absorber coatings are passing through Vapor is extracted out from outside air during stating dry channel.

20. the method according to claim 5 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle evaporation drive system includes the absorber coatings of exhaust passage, such as limewash, and the absorber coatings are logical by the exhaust Carbon dioxide is extracted out from the exhaust uptake gas during road.

21. the method according to claim 19 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle evaporation drive system includes the absorber coatings of the dry channel, such as liquid drier, and the absorption of the dry channel applies Layer extracts vapor out during through the dry channel from outside air, and the evaporation drive system also includes exhaust The absorber coatings in channel, such as limewash, the absorber coatings of the exhaust passage by during the exhaust passage from exhaust Carbon dioxide is discharged in flue gas.

22. the method according to claim 19 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle evaporation drive system includes solar generator, is used for after weak absorbing agent is by the dry channel to the weak absorbing agent It is recycled.

23. the method according to claim 22 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Described in solar generator include: to make dry channel of the atmosphere air-flow by solar generator, the institute in the dry channel It states air-flow to be pre-chilled by the drying side contacts with surface, another wet side on the surface in wet channel is by from pipe The weak absorbing agent of the bottom of the dry channel in road soaks, and is then reduced to absorbent temperature substantially from environment temperature Then air-flow is re-directed to the wet of solar generator from the dry channel of solar generator by the upper dew-point temperature Channel, directly to contact absorbent, absorbent is covered as mobile film by the wicking layer of the wet side on the surface, Described in air-flow got wet with the moisture evaporated from absorbent, increase its temperature and humidity in wet channel, and described Air-flow, by heat by solar radiation, then, heating and moist air-flow is discharged in atmosphere or guide duct in wet channel The wet channel strongly returns to the top of the dry channel of pipeline with cold absorbent after through wet channel.

24. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, is used Natural air in building adjusts and ventilation, and certain parts of outside air are in the dry channel for passing through pipeline Afterwards, it is extracted as cold and dry air and is used to introduce the interior space, certain portions of room air by access road Divide the wet channel for being retracted to pipeline from the interior space by gravity-flow ventilation.

25. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle evaporation drive system includes the water jet for turbine, and the turbine is made into rotary regenerative heat and mass exchanger, described The heat and mass exchange process between the outside air and control air are realized at turbine, also to pass between these air-flows Pass heat and cooling capacity.

26. the method according to claim 25 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Described in turbine be mounted on the bottom of the pipeline, for the entrance outside air of the heat exchange and the institute of export air It states dry channel and is connected at the bottom of the pipeline with wet channel, and the turbine includes rotor, the rotor passes through The outside air and control air continuously rotate, and the outside air and control air pass through axial groove with high-speed A series of blades are flowed through, provide power to be connected to the turbine of generator, and the rotor includes regrown material, and described Channel has opening in the either end of the rotor, for guiding isolated outside air and control air to pass through the regenerated material Material, the regrown material includes the isolated entrance sector and exhaust sector for outside air and control air, wherein described The wet sector of regrown material evaporated liquid (such as water) wetting is added to the exhaust sector, and outside the entrance Air is guided first by the entrance sector, and passes through regeneration as the export air after turning to 180 ° The wet sector of material.

27. the method according to claim 25 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Described in dry channel it is more shorter than the wet channel.

28. the method according to claim 25 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle evaporation drive system includes the turbine with generator and the rotary regenerative heat and mass exchanger with motor as two A individual device.

29. the method according to claim 25 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle evaporation drive system includes turbine, and the turbine is made into vertical rotary regenerative heat and mass exchanger, real at the turbine Heat and mass exchange process between the existing outside air and control air, to transmit heat and cold between these air-flows Amount.

30. the method according to claim 29 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle vertical turbine includes wet sector, soaks the wet sector by water using fluid box, the rotor of the vertical turbine immerses In the fluid box.

31. the method according to claim 25 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Described in control air by being heated during the wet channel.

32. the method according to claim 31 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, In pass through control air described in heat by solar radiation.

33. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Described in moisten channel include wind deflector.

34. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle evaporation drive system includes different inclination angle.

35. the method according to claim 34 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, The inclination angle of middle evaporation drive system is about 45 °.

36. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle evaporation drive system includes the turbine and dew point indirect evaporative cooler as two individual devices, the furthermore cooling Device realizes the humidification that the outside air is down to the substantially cooling procedure of its dew-point temperature and the control air, And after this, cold outside air is directed into the evaporation driving system on the direction of air movement before the turbine The dry channel of system, and warm saturation control air is directed into the evaporation drive system after turbine The wet channel.

37. the method according to claim 36 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle evaporation drive system carries out the wet processes of dew point indirect evaporative cooler using seawater, and includes additional condenser, In the condenser, the control air of cold outside air and wetting is guided the steaming as a result condensed for indirect heat exchange contact Distilled water is directed to consumer.

38. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Described in atmospheric evaporation drive system the turbine be used as will as the control air outside air from the drying Channel is transported to the fan in wet channel, and the generator connecting thus with the turbine is used as the electronic of the turbine rotation Machine.

39. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle evaporation liquid evaporates liquid using low boiling point, and such as ammonia or water-ammonia mixture, the low boiling point evaporation liquid is as mobile thin Film covers the wet side on the surface in the wet channel.

40. the method according to claim 39 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, In the low boiling point described in the wet channel interior evaporation liquid evaporation into the control air after, the control air quilt It guides so that steam is from the air setting, then return condensed fluid is to soak the wet channel.

41. the method according to claim 39 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, The upper end of the side of middle balloon or mountain using at high tower or High aititude, system is located at the High aititude on mountain, and lower end is located at the foot of the hill Under low altitude area at, for condense low boiling point evaporation liquid.

42. the method according to claim 6 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, The vertical downward flow of distilled water of the middle use from condensation channel drives hydroturbine to generate additional electric power.

43. the method according to claim 6 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Outside air is reintroduced after through the dry channel, to pass through from the dry channel to the wet channel Air turbine generates electric power, wherein saline solution is added in vacuum passage, the vacuum passage is adjacent with condensation channel and passes through Connect by steamturbine with condensation channel, in addition, the two channels be all placed on the dry channel and the wet channel it Between so that the vacuum passage via plate and the dry channel there are heat exchange mechanism, for the vacuum passage heat supply, And by another block of plate and the condensation channel there are heat exchange mechanism, the condensation channel also leads to the vacuum passage simultaneously It crosses third plate and the wet channel is in heat exchange relationship, for heat to be discharged from the condensation channel；In addition, vapor from It is evaporated in saline solution inside the vacuum passage, and on advancing from low altitude area to High aititude inside the vacuum passage Up-flow is dynamic, then passes through steam whirlpool by creating vacuum and rebooting vapor from the vacuum passage to the condensation channel Wheel to generate electric power, the vapor in the condensation channel from High aititude to low altitude area advance Doenward flow, in the condensation The vapor is decreased its temperature and is condensed in the form of distilled water in channel, to select for consumer.

44. the method according to claim 43 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, In for the wet channel, using the distilled water from the condensation channel, the distilled water is as film or mobile film quilt It is covered on the wicking layer of the wet side of plate, these plates form the wet channel.

45. the method according to claim 43 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle saline solution is selected and used as the cold source of consumer after through the vacuum passage.

46. the method according to claim 42 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Middle distilled water of the selection from the condensation channel and the cold source for being used as consumer.

47. the method according to claim 43 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, In the vacuum passage with saline solution connect with the condensation channel by the steamturbine, in the vacuum passage Vacuum pass through and generate all channels arrangement at about 10 meters of height above ground level, these channels are connected to by pipeline At the saline solution source of the vacuum passage and concentrated salt solution discharge and the distilled water tank of the condensation channel, the salt At aqueous solution source, concentrated salt solution discharge and distilled water tank is all on ground level.

48. the method according to claim 47 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, In passing through after dry channel passes through turbine again first, entire atmosphere cold airflow is used as the cold source of consumer, then entirely Atmosphere air-flow after heating is re-directed to the wet channel of pipeline as control air.

49. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, Described in system include respectively for outside air and control air for generating the individual turbine of electric power.

50. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, In pass through after the dry channel passes through turbine again first in atmosphere cold airflow, a part of atmosphere cold airflow is as the work Make air and be re-directed to wet channel from dry channel, and another part of the air-flow is extracted and as guiding cool air to Consumer.

51. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, In by the way that after the dry channel, a part of atmosphere cold airflow is re-directed to as control air from dry channel wet Channel, the wet channel includes oneself independent turbine, and another part of the atmosphere cold airflow is extracted and is used to pass through Turbine is discharged into atmosphere after generating electric power.

52. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, It is middle that the system is inserted into soil, the air in thermoelectricity and application earth atmosphere is generated using underground heat or/and soil heat source As working fluid.

53. the method according to claim 1 for generating electric power, cooling capacity and distilled water using atmospheric evaporation drive system, In for convey water directly from cloud with the system for soaking the wet channel of pipeline include mesh and reservoir, the storage Device is connect by hose with the wet channel, which further includes the balloon and rope for supporting the system in the sky.