CN105540707A - Evaporation system for vacuum production of salt and purified water - Google Patents

Evaporation system for vacuum production of salt and purified water Download PDF

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Publication number
CN105540707A
CN105540707A CN201510732211.9A CN201510732211A CN105540707A CN 105540707 A CN105540707 A CN 105540707A CN 201510732211 A CN201510732211 A CN 201510732211A CN 105540707 A CN105540707 A CN 105540707A
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China
Prior art keywords
water
container
evaporation
heat
exposure
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Granted
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CN201510732211.9A
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Chinese (zh)
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CN105540707B (en
Inventor
胡胜录
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Shaanxi Donghai Rizhao Technology Co.,Ltd.
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Individual
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/138Water desalination using renewable energy
    • Y02A20/142Solar thermal; Photovoltaics
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/20Controlling water pollution; Waste water treatment
    • Y02A20/208Off-grid powered water treatment
    • Y02A20/212Solar-powered wastewater sewage treatment, e.g. spray evaporation
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

Abstract

An evaporation system for vacuum production of salt and purified water comprises a container, water is contained in the container, the output of the container is provided with a gas extracting and discharging device, and a certain space exists between a horizontal plane in the container and the outlet of the container; and the system also comprises water which can be naturally heated or can receive solarization heating, and the water provides heat for evaporation of the water in the container.

Description

A kind of vacuum salt production and the vapo(u)rization system of purifying waste water
Technical field
The present invention relates to a kind of vapo(u)rization system.
Background technology
In today of social high speed development, salt manufacturing, desalination water processed and these several work of freezing all seem particularly important, now conventional vacuum salt production, and a lot of producers of desalination water processed all need to adopt a large amount of coal that burns to provide heat needed for evaporating, in its salt-making process, a lot of producer also needs to take a large amount of soil, and has the universal phenomenon that cost-effective is beneficial low due to technical scheme different salt manufacturing desalination water.In refrigeration, as air-conditioning conventional at present mostly needs use the refrigerant as fluorine Lyons thus cause very large harm to environment, add that the difference of today air-conditioning price height current consumption different from structural member due to technology used is large, the ordinary people of a lot of economic condition difference can not be widely used.
These three work above, due to technical reason, not only working effect is poor, and the environmental hazard brought is also very large.Nowadays cause the great attention of many international expert already, be also the large problem making brainstrust headache simultaneously.
Summary of the invention
The technical problem to be solved in the present invention is to overcome the deficiency existed in existing three technology, the technology providing a kind of energy-conserving and environment-protective to reduce production cost raising productivity effect and equipment.A large amount of land areas can also be saved in salt manufacturing work, change in prior art and have much as vacuum salt production and desalination water processed turnout and the phenomenon polluted and be directly proportional that consumes energy at work, reduce production cost.
The technical scheme that the present invention will solve is;
This vacuum salt production and the vapo(u)rization system of purifying waste water, comprise container, it is characterized in that: fill water in described container, and described container outlet is provided with exhaust body device, and the horizontal plane container outlet in described container has certain space; Also comprising to heat up naturally maybe can accept the water that Exposure to Sunlight heats up, and this water is that water extraction in container is for evaporation institute heat requirement.
Further solution of the present invention is; Expand the water capacity of container, the water capacity of namely described container is more than 1 ton, or more than 2 tons, or more than 3 tons, or more than 4 tons, or more than 5 tons, or more than 7 tons, or more than 10 tons, or more than 15 tons, or more than 20 tons, or more than 25 tons, or more than 30 tons, or more than 35 tons, or more than 40 tons, its water capacity tonnage is respectively more than following data, namely 45,50,55,60,70,80,90,100,200,300,400,500,600,700,800,900, or more than 1000 tons.
Another scheme of the present invention for: the above-mentioned all data done container water capacity are mainly to the restriction that seal form container water capacity is done.Here except there is vessel port in the place by dress exhaust body device, this container of other vessel port is not had all to be called sealed container by when vacuumizing again.If container body is provided with water-in and water outlet but owing to needing its good seal so closed type container also calculated by this container when vacuumizing, because be just no longer called vessel port after sealing, the sealed vessel described in current application documents can have water-in and water outlet but not illustrate in accompanying drawing.Above the water capacity that can be positioned at container also be can be understood as to the data that container water capacity is done.For the described water when vacuumizing in container can stream be while can not do the restriction of the water capacity in container to this form of outflow inwards on one side, namely these data of the above container water capacity limited do not comprise the container of the blow-by form of liquid form.Or also can be understood as the data of the water capacity that can be positioned in container.
Another scheme of the present invention is; The water surface area that water surface area in container maybe can accept Exposure to Sunlight is more than 5 square metres or more than 8 square metres, or more than 10 square metres, or more than 13 square metres, the water surface area that the water surface area in its container maybe can accept Exposure to Sunlight can be respectively following data square metre more than 15,18,20,25,30,35,40,45,50,55,60,65,70,75,80,85,90,95, or more than 100 square metres.
Another solution of the present invention is: describedly naturally can heat up that maybe to accept water that Exposure to Sunlight heats up be can the water of natural flow, and this water is that water extraction in container is for evaporation institute's heat requirement or water source.Just can not, by like device in such as lift pump etc., water just can be made automatically to enter container so at work, the water entering container in namely working or go out container can artificially consume energy and can automatically pass in and out.Thus saving energy consumption.
Another solution of the present invention is: described naturally heating up maybe can accept the water that Exposure to Sunlight rises Warm, and wherein said Exposure to Sunlight rises Warm and comprises nature Exposure to Sunlight intensification and solar facilities Exposure to Sunlight intensification, and solar facilities heats up and comprises again the intensification of solar energy greenhouse equipment.
Another scheme of the present invention is; The water heating system that salt manufacturing or system are purified waste water, comprises water, is wherein that water used is heated with solar energy greenhouse.This says that greenhouse can be used in the work of any salt manufacturing or desalination water processed and is water heating, temperature keeping, as used infiltration legal system water just needs sometimes for water is heated, existing saltpan method distillation method etc. has a lot of place all may need for water is heated in these two work, here advocates and can utilize greenhouse.
Another scheme of the present invention is: the described Warm that can naturally rise maybe can accept the water that Exposure to Sunlight heats up and forms reciprocal water cycle with the water in container, or Exposure to Sunlight circulates.
Another scheme of the present invention is: described can naturally heat up maybe can accept Exposure to Sunlight heat up water level in pond.
Another scheme of the present invention is: the described Warm that can naturally rise maybe can accept water level that Exposure to Sunlight heats up in pond, is provided with container in described pond; Can naturally heat up in other words maybe can accept the water level of Exposure to Sunlight intensification in pond, container is provided with in described pond, in container by the water that evaporation reduces temperature accept in pond again Exposure to Sunlight heat up or and intensification naturally, formed in work water circulate in pond nature heat up or Exposure to Sunlight heat up, circulating and evaporating again.
The another solution of the present invention is: it is based on the intensification naturally heated up or Exposure to Sunlight heats up that described intensification naturally or Exposure to Sunlight heat up, described naturally to heat up or the intensification of Exposure to Sunlight, be say that container has at least half or heat over half or temperature to derive from nature intensification when evaporating in evaporation institute's heat requirement used or temperature or Exposure to Sunlight rises Warm.This defines done one of heating when naturally heating up or Exposure to Sunlight heats up and artificial power consumption is heated and uses simultaneously, namely heats and can be defined in below half or half.Certainly also clod of earth of heating, with over half, is to consider that the one that the protection of patent right is done is particularly limited to here.
Another solution of the present invention is: described container is sealed vessel or blow-by container, described blow-by container comprises U-shaped pipe container for evaporation, and the water of its packing less container in the work vacuumized in container can be divided into forma fluens or immobilising form.Forma fluens be alternatively water in container simultaneously on one side inwards stream on one side to the form that container outflows.
The another solution of the present invention is; A kind of vacuum-evaporation refrigeration system, comprise container, it is characterized in that: fill water in described container, described container outlet is provided with exhaust body device, and the horizontal plane container outlet in described container has certain space; Also comprise the water outside container or air, after the water in the water outside described container or air or container is reduced temperature by container or refrigerant, be connected with many users by pipeline, refrigeration is provided.
Another solution party of the present invention is; Vacuum salt production and the vapo(u)rization system of purifying waste water or a refrigeration system, comprise container, it is characterized in that: fill water in described container, described container outlet is provided with exhaust body device, and the horizontal plane container outlet in described container has certain space; Also comprise the water outside container, it is less than 0 degree or 0 degree that the temperature of the water outside described container or the water in container can be reduced to, and is provided with to get ice and arrange or get ice port and ice can be taken away in container or system, or transports to and need use with the place of ice.Water for cooling can be that zero degree or sub-zero zero form ice by this device, and ice can desalination water processed or purify waste water, and water freezing also can condensed water and salt manufacturing or refine other material again from condensed water.Also can freeze or available device organizational system ice plant.
The present invention mainly affects two large factors of boiling speed by change and reaches good evaporation effect, namely speed of seething with excitement is relevant with the volume of original water temperature and water, the present invention proposes to expand container water capacity, recycling can Exposure to Sunlight heat up heating mode, greenhouse technology can also be utilized to heat for water, thus greatly improve working efficiency, that also can save exhaust body device uses energy.
The present invention one scheme is, comprises container 1 and the water of a lower openings, it is characterized in that: the lower openings of described container 1 is inserted in water, and be the water 41 of internal tank and the water 42 of external container by moisture, the water outside container and the water in container are connected.The plan range container outlet 43 of the water 41 of described internal tank has certain space, and this airtight space, described container outlet 43 is provided with exhaust body device.In the process vacuumizing evaporation, the lower openings of container 1 is not closed.
The another scheme of the present invention is, described vacuum salt production and the vapo(u)rization system of purifying waste water, is characterized in that: the external processing retrieving arrangement 44 of purifying waste water of described exhaust body device 5.A system for vacuum salt production in other words, it is entered again salt manufacturing Shen processing units by the water of container evaporation concentration, because the strong brine after concentrated finally just must can become salt through a few thing program.If this course of processing just in case also need complete in container sometimes, container so is at this moment because work order ground different operating program difference is so container at this moment also can be described as salt manufacturing deep processing equipment.The alternatively system of a kind of salt manufacturing of the present invention or desalination water processed, its exhaust body device pump drainage steam out enters desalination water retrieving arrangement 44, or is provided with condensed water deep processing equipment again.
The another scheme of the present invention is, described vacuum salt production and the vapo(u)rization system of purifying waste water, is characterized in that: the lower openings of described container 1 is one or more.
The another scheme of the present invention is, described vacuum salt production and the vapo(u)rization system of purifying waste water, is characterized in that: in the process vacuumized, the water 42 of external container can flow over container 1.
The another scheme of the present invention is, when vacuumizing, the water outside container flows simultaneously in container.
The another scheme of the present invention is, described vacuum salt production and the vapo(u)rization system of purifying waste water, is characterized in that: in the process vacuumized, the water 42 of external container flows in container 1, and the water 41 of internal tank outflows to container.
The another scheme of the present invention is, described vacuum salt production and the vapo(u)rization system of purifying waste water, it is characterized in that: when described lower openings is multiple, described multiple lower openings is made up of flowing water mouth 9 and water export 10, the water 42 of described external container is positioned at container 1 both sides and has certain altitude difference, to impel water to enter from flowing water mouth 9 in the process vacuumized, flow out from water export 10.
The another scheme of the present invention is, described vacuum salt production and the vapo(u)rization system of purifying waste water, it is characterized in that: described in the process vacuumized, water enters from flowing water mouth 9 and first upwards flows along container A pipeline 7 at container 1, then flow downward in container along container B pipe 8 again, finally from water export 10 flow container.
The another scheme of the present invention is, described vacuum salt production and the vapo(u)rization system of purifying waste water, is characterized in that: described in be positioned at the low water in container 1 side and rely on pumping plant 45 to be connected with pond 16.
The another scheme of the present invention is, described vacuum salt production and the vapo(u)rization system of purifying waste water, is characterized in that: the low aqueous phase of the entrance in described pond 16 and container side connects, and the aqueous phase that the outlet in described pond 16 is high with being positioned at container 1 side connects, and makes water form circulation.
The another scheme of the present invention is, described vacuum salt production and the vapo(u)rization system of purifying waste water, is characterized in that: described pond 16 is nature intensification pond or Exposure to Sunlight intensification pond or pond of heating.Three kinds of modes with or with one or its two.
The present invention, described vacuum salt production and the vapo(u)rization system of purifying waste water, is characterized in that: the described temperature lowering water flowed out from water export 10, by pipeline and many users, reaches the effect of refrigeration cool-down, then enter container 1 by pipeline inflow flowing water mouth 9, forms circulation.
Another solution of the present invention, said container is the form of sealing, and water carries out vacuumizing evaporation in the container 1 of sealing, the water outside container or air around container or 6 li, pipe, for container for evaporation provides evaporation institute heat requirement.
Another solution of the present invention, the water outside said container, flows in the container outer circulation of seal form, and for container evaporation provides institute's heat requirement, or water circulates as evaporation provides heat in pond 16 and container surroundings or pipe 6.
Another solution of the present invention, enters in container 1 or container surroundings or pipe 6 by the water drainage lower than 45 degree, for evaporation provides institute's heat requirement, in evaporative process except the heat of water in container self except, do not need to provide extra heat to evaporating.
Another solution of the present invention, in the work of desalination water processed, owing to flowing through the water of container, comprise the water in container and the water outside container, flow out from container in work or flow out from container surroundings, the water flowed out can reclaim and also can not reclaim, and namely said recovery is the meaning being recovered to original position.
Another solution of the present invention is, can select a water level flowed, and namely water arranges container 1 from a high position to the water channel of low bit flow.During work, water can flow into container automatically, then automatically flows out, and need not reclaim, thus reduces as the using of interior like device such as lift pump are consumed energy.
Another solution of the present invention, utilize the appearance volume of water in expansion container thus improve working efficiency, also the light-receiving area that can accept Exposure to Sunlight that evaporation area expands water in other words can be expanded, expand the water light-receiving area in container in other words thus can reduce exhaust body device with can, improve evaporation effect.
Another solution of the present invention, utilize the air of the water or container surroundings reducing temperature when evaporating by container 1 to be transported to many users, provide refrigeration, wherein said water comprises the water outside container and the water in container.By water channel or pipeline, the water flowed out in container is transported to many users in other words and refrigeration is provided.The water that container B pipe 8 flows out in other words is transported to many users, and enter container from container A pipeline 7 again after providing refrigeration, in work, water constantly circulates in container and many users.
Can be found out by above technical solution, it is as interior in vacuum salt production or desalination water processed etc. like in work that the present invention changes prior art, the traditional mode that artificial power consumption must be provided to heat for container for evaporation, advocate and adopt free clean sun Exposure to Sunlight, can be evaporation and unlimited heat is provided, utilize the water temperature under normality or the water after Exposure to Sunlight to enter container, vacuum boiling can be kept under the low pressure of container completely.The water that utilization can be flowed in container provides heat endlessly for evaporation, is discharged by the low temperature in container again simultaneously.By regulating the speed of water and discharge that flow in container and the enough heats reached needed for boiling or evaporation, guarantee to evaporate normal work.The principle of work of the technology of the present invention, be also from maximum different of prior art, apparatus of the present invention can expand the evaporation area in container thus greatly improve working efficiency.This technical scheme is utilized to can be used for concentrated seawater and salt manufacturing, also can it be made to become desalination water or use of purifying waste water the steam prior art be evaporated, can also utilize by reduced in evaporative process (medium) water of temperature or air or refrigerant be transported to need cooling place for refrigeration.
Accompanying drawing explanation
Fig. 1 is a kind of container for evaporation schematic diagram of the present invention.
A kind of container schematic diagram that pipe can make the water outside container or air flow in pipe is provided with in Fig. 2 container for evaporation.
Fig. 3 is the container for evaporation schematic diagram of another form of the present invention.
Fig. 4 is the container for evaporation schematic diagram of another kind of form of the present invention.
The schematic diagram of upper and lower two-layer water around container flowing can be divided outside Fig. 5 container for evaporation.
Fig. 6 is in the U-shaped pipe container for evaporation schematic diagram had like U-shaped pipeline.
The operating diagram of Fig. 7 U-shaped pipe container for evaporation.
The inner internal organs view of U-shaped pipe evaporator of Fig. 8 multi-pipeline.
Fig. 9 is container for evaporation, water route and pond three's cooperating and position relationship schematic diagram.
Figure 10, is equipped with the schematic diagram of water in sealable container.
Figure 11, can the large and a kind of form schematic diagram that water surface space is little of water capacity in container.
Figure 12, has a kind of form schematic diagram of dividing plate in container.
Figure 13, pond is provided with the schematic diagram in greenhouse.
Figure 14, container is provided with the schematic diagram in greenhouse.
1-container 3-space 4-water 5-exhaust body device in figure
6-pipe 7-A pipeline 8-B pipe 9-flowing water mouth
10-water export 11-evaporation area 12-water channel base plate
The outer inlet channel 14-of 13-is intake outward 15-vaporizer location
The water surface in the 18-container of 17-water route, 16-pond
The outer water surface 20-water outlet 21-Xi22-Dong of 19-container
Water 43 container outlet of the water 42-external container of 41-internal tank
44-purifies waste water and processes retrieving arrangement (be connected to outside exhaust body device, do not illustrate in figure) 50 greenhouse 51 dividing plate
Embodiment
Pond 16 and container 1 is mainly used in apparatus of the present invention system, and the work relationship in container and pond, sum up the operating characteristic of pond of the present invention and container and total used technical characteristic, as pond, container, form of heating, the features such as working forms give thin young discussion:
One, pond can have multiple.1, pond is that solar energy is irradiated to as water dike supplies to say the pond of shining and heating up, the Shui Ke Fen Static only immobilising pond in pond, 2, and the water in pond has the pond of flowing or outside outflow form.3, the pond circulated that the water in pond has outflow to flow to again.4, the pond that the water in pond has outflow not return, 5, the greenhouse pool that pond has open dug reservoir also to have coverture to cover, or the daylighting greenhouse pond formed is covered with transparency material.The various combine with technique in greenhouse used or existing greenhouse also can be planted, 6 with vegetables planted in big canopy in greenhouse, and there is nature intensification pond in pond, or say and shine intensification pond, or to heat the pond of heating formed with various method feedwater.7, pond also can be made into the form separated with ground makes pond heat can not by ground absorption.8, pond also can from being sea.9, pond also can be the water stream channel or straits that can flow or like the flowing flux within river.10, pond may also be the water source needing purification.11, pond can have multiple, multiplely also can be the substantially identical multiple ponds of position place height.Also can be the form arranged from high to low, namely previous pond is on higher position, next pond is lower than previous pond, same procedure can arrange multiple pond more, in work, the water in previous pond automatically flows to again next pond after can evaporating in container and being lowered the temperature and heats up, not only flow to next but one pond and heat up after evaporation after intensification, like this can without the use of lift pump or minimizing lift pump thus minimizing energy in work.
Two, described container also can divide multiple, and 1, container is the container that can hold water, can allow the container of water evaporates.2, on container body, be provided with the vacuum-evaporation container of off-gas pump.3, sealed vessel, then the water-lute of the middle container that namely works vacuumizes and carries out reduction vaporization in container.4, blow-by container, the water in work in container and the water outside container be connected as a single entity lower vessel portion opening sealing.5, described vessel port can have an opening or multiple opening, and opening can on body or bottom or left side or right side etc. be different locally arranges, and opening can also be set to the container in having u shape pipeline or water route.6, container can be set to greenhouse container for evaporation, namely with coverture cover on pond by pond around formation greenhouse pool, just plant vegetables to plastic greenhouse similar, in other words with the solar energy light collecting greenhouse of transparent object around formation, be water heating and thermal insulation with greenhouse, the favourable evaporation of heating water temperature rise, greenhouse nappe can be provided with one or more exhaust body device and make Quick air-discharge or decompression in greenhouse, force the water rapid evaporation in greenhouse or boiling, not only this greenhouse greenhouse container for evaporation, be greenhouse not only but also be container for evaporation.Certain container for evaporation also can be located in inherent greenhouse, greenhouse and establish a vacuum-evaporation container again, greenhouse body can be provided with exhaust body device and greenhouse evaporates objective device, also exhaust body device can not be established at this moment to can be described as greenhouse, and greenhouse can arrange one or more container for evaporation and be exclusively used in water evaporates in heating water greenhouse.7, container can be that any applicable material is formed, and also can be the light transmission container that transparency material is formed, light transmission container be mainly beneficial to and carries out daylighting intensification to the water in container.8, all 6 can have been managed from being provided with in all containers of the present invention or in water, make steam or water or air from pipe 6 back warp mistake, pipe 6 also can be arranged in pond, and the water in evaporation work in pipe 6 or steam also can be the water extraction heat supplied in the water in pond or container.The feature that can produce heat when the steam that is evaporated of container for evaporation can utilize steam to become liquid by existing method again at work heats into water, and the heat that steam produces is by the water water in other words container in of existing method for heating water heating evaporation water pond in other words in other words.Container for evaporation also can condensing steam or cross condensing steam from pipe 6 back warp it can be made to become liquid or desalination water.9, spontaneous evaporation container, container is Mi envelope or packing less container, and the water in container can accelerate evaporation from exhaust body device, and exhaust body device also can not be established to make it carry out spontaneous evaporation.10, various container body of the present invention can be provided with water-in and the water outlet of container, can to intake make up water in other words from water-in when particularly sealed container water in container is not enough, can be good by inlet seal after water inlet, need can to open water outlet during water outlet to discharge water, then water outlet can be sealed again.Some does not illustrate in the water-in of container and water outlet reality in the accompanying drawings should have.
Three, the multiple set-up mode of container, 1, container can not put in pond, and heating up through saying to shine or naturally heat up according to intensification tank water in pond for saying in pond, then evaporates in container, in the process of evaporation, water can turn cold, at this moment can be said again by the water turned cold to shine in pond or transparent vessel and heat up, evaporate again after intensification, water can circulate and heat up or say according to the also Zhi ring evaporation in container simultaneously that heats up in pond or container like this.In work, container for evaporation is undertaken vacuumizing evaporation by exhaust body device, water after for some time in container turns cold or cisco unity malfunction at this time can stop, water is allowed to carry out the intensification of for some time in pond or in transparent vessel or to say solarization intensification, again carry out vacuumizing evaporation when temperature is enough, repeat equally in work.2, container also can move at work, namely after evaporation, container is removed the water surface, and then is inserted by container in the water that heated up or in new water and again evaporate.Also can be moved by container makes water enter in container, such as inserts in water with ship band upper container container, and ship can flow to container automatically to the water simultaneously that moves ahead.Container can move at work and be conducive to being gone on foot to high Warm water by water at low temperature thus can absorbing the heat of the high-temperature water outside container selectively.3, container can be arranged in water stream channel or marine, the present invention utilize normal-temperature water in other words low Warm water evaporate, sometimes container a large amount of water inlet many times and a large amount of water outlet is needed in the work of particularly desalination water processed, so conveniently or save lift pump with energy container also can be located in water stream channel, as in similar river or basin, straits or ocean current, the flowing of their wherein water is not make it flow but natural flow by lift pump or other artificial or power consumption, utilizes the water of natural flow that water also can be made naturally to flow into container or flow through container.Seawater can also can desalination water processed from salt manufacturing, container is placed in marine or ocean current passage, sea or river or water stream channel all have natural saying and shine and heat up or natural Elevated Temperature Conditions, the water temperature of himself can be utilized to evaporate in container, the water yield that also can increase in container also increases the heat content of water in container simultaneously thus provides more heats for evaporating, sharpest edges of the present invention are exactly can with the container of a high-capacity, speed of seething with excitement as everybody knows is relevant with the volume of original water temperature and water, the boiling point of water relevant with air pressure and here these three conditions do not lack, also the water in container can be released when the water temperature in container is not enough, new water can automatically flow into container not only but also start evaporation.The water flowed out in the work of salt manufacturing can reclaim intensification and enter container evaporation again, and the water flowed out in the work of desalination water processed also can not need to reclaim.4, this apparatus container also can coordinate with ship, by ship, container is placed in water or marine, and ship also can shift position as required at work, and shift position also can make container enter in different water temperatures.5, apparatus of the present invention after water enters container at work by container sealing and then vacuumize and carry out decompression evaporation.The blow-by of lower vessel portion opening also can be carried out taking out the empty evaporation of steaming, and the water at work in container also can flow to simultaneously and flow out, and also can not flow.
Four, the work relationship of pond and container, 1, container and pond are set together, and container and pond are integrated, container is arranged in pond, container evaporates in pond, and water can heat up in pond or in container in Exposure to Sunlight, can evaporate after intensification in container, can be heated up in container or in pond again by the water of the water that evaporates or the cooling after being evaporated by container or Exposure to Sunlight heats up, can working when in container, water temperature is not enough stops carries out the Exposure to Sunlight of for some time and heats up or naturally rise Warm.Working forms as described so can also be provided with in multiple such pond and container work and match.It is that water extraction in container rises Warm for saying to shine that container also can be set to the daylighting container made with light transmissive material and greenhouse lighting container.Container and pond are integrated also can have various ways, device through arranging just has water like the receptacle of a sealing sometimes, there is the part of water like being pond, container can make i.e. greenhouse container with light transmissive material, just start pump drainage gas in container when water temperature is enough in container and carry out underpressure distillation, can stop again when water temperature reduces not enough to allow water heat up in container or say to shine and heat up, in work, form circulation Exposure to Sunlight circulating and evaporating.2 containers and pond are respectively the form at a place, and the current outlet sump that container can be arranged on the middle pond that to work outside pond flows to container.The form that the water in 3 ponds circulates between container and pond, water flows to container evaporation after heating up in pond, the water by evaporative cooling again flow container enters pond and rises Warm, can carry out iterative cycles in work.The current in 4 ponds are through container or flow to container, and the water by container evaporative cooling in the work of desalination water processed can evaporate by amount discharge container from newly entering new water again, and the water at low temperature of amount discharge container also can reclaim never and namely can not return in container.
Five greenhouses, apparatus of the present invention also can be water used heating at work sometimes, and improve evaporation institute heat requirement, its heating means also can have of all kinds, and existing heating means can be used, as power consumption or burn coal or power consumption etc. method all can form can be various.And this is mainly advocated and utilizes sun Exposure to Sunlight to heat for water, or naturally heat up, everyly obtain water temperature by Exposure to Sunlight or water temperature is improved, in such water present specification, all claiming Exposure to Sunlight intensification water, in underground warm water is also included within, rising Warm water also referred to as natural intensification water or Exposure to Sunlight.Utilize underground warm water to be that the form that water used is heated is called nature intensification water or Exposure to Sunlight intensification water here by technology or existing method, just need extract its water temperature of salt solution out from underground as mineral products rock salt and rise Warm water also referred to as natural intensification water or Exposure to Sunlight here.
Said in front application in the present invention is water heating for water heats available sun Exposure to Sunlight intensification or solar facilities, said solar facilities is in fact not several as you know yet, as existing solar water heater, the utilization of solar collection element or solar energy heat collection pipe, also has a solar power plant, visible solar facilities is original also few of particularly can be just less for the solar facilities of water heating, can be heat in pond by solar facilities by knowing in the application documents of last time, also say in application documents that the pond 16 in figure can provide Exposure to Sunlight, sometimes also boiler can be become, or become solar facilities, namely can be also water heating by various ways.Also can regard solar facilities as by the pond 16 of drawing in above-mentioned known figure is water heating in pond or pond, if it is that the water of solar facilities so in pond will below this solar facilities that the pond in figure 16 depicts this block cartographic represenation of area of one piece of area, and this solar facilities from above to pond one week all by solar facilities around covering, solar facilities needs to accept Exposure to Sunlight and can heat for water below, by a technical scheme can be shown in advance above, namely in a pond, water is had, face waterborne has above pond solar facilities can around covering thus can the water of water feeder heating up by one week, pond and top in other words, by everybody is easy to associate now conventional a kind of solar energy greenhouse technology above, the greenhouse technology that particularly a kind of a kind of aquaculture utilizing solar facilities to cover to heat for the water in pond in pond is used.As there being greenhouse to plant for vegetables planted in big canopy in the prior art for a long time, aquiculture green house is also had to be pond heating, temperature keeping.Here the greenhouse said mainly says that namely the greenhouse that water feeder is heated is exactly the equipment heated up around intensification in covering Neng Shi covering chamber or Exposure to Sunlight in pond with coverture, similar with existing aquiculture green house, existing greenhouse has a lot of year history existing a lot of experience technically, existing greenhouse is having a lot of innovation with on material with textural, existing greenhouse can also be given to increase temperature again with method for distinguishing except utilizing Exposure to Sunlight simultaneously, the greenhouse that particularly aquiculture green house is used to the present invention is very similar has a lot of spiral technology can learn to utilize more, also can therefrom learn from other's strong points to offset one's weaknesses so the present invention's greenhouse each side technology used all can learn existing greenhouse technology.
The present invention mainly says in said greenhouse and utilizes greenhouse technology for water heating, temperature keeping, then for salt manufacturing or desalination water processed purify waste water or from condensed water other material of refine etc. work in.Having the method for a variety of salt manufacturing or desalination water processed at present and having in these methods much all needs to heat for water, as present saltpan method salt manufacturing also, it is also utilize the sun to shine to allow the water evaporation concentration in salt field carry out salt manufacturing, if add that on salt pan namely greenhouse can cover transparent object and make daylighting greenhouse on salt pan, it is water heating that sunlight can inject indoor, indoor can exceed more than twenty or thirty degree than the temperature of outdoor due to Greenhouse effect, so just more be conducive to feedwater heat up thus improve evaporation effect, accelerate evaporation, the steam be evaporated can flow out in greenhouse from ventage automatically, also steam can be discharged by gas barrier or the equipment such as fan or off-gas pump.The above is that existing saltpan method adds that greenhouse technology carrys out a practical example of salt manufacturing, can find out that greenhouse not only substantially increases velocity of evaporation in conjunction with saltpan method salt manufacturing and also solves saltpan method salt manufacturing simultaneously and be afraid of most to rain and the situation of strong wind by this example, for many years area, salt pan always wind and rain have a strong impact on more Salt Production also give salt pan workman bring very large operating pressure, nowadays by increase greenhouse not only can heat and also rainwater can not enter salt pan thus to salt pan work bring convenience.If existing distillation method and reverse osmosis method are also the technology comparatively commonly used in the multiple method of salt manufacturing or desalination water processed, they also all need for water heating in fact, as reverse osmosis technology also can bring unfavorable to work so sometimes also need for water heating because temperature is too low, so the greenhouse described in this is not limited in the method for that a kind of salt manufacturing or desalination water processed, but may be used for needing in all salt manufacturing and desalination water processed or similar work for can be that water is heated or preheating with greenhouse or daylighting greenhouse when water is heated.Purposes can should there be each various kinds in greenhouse by the water for energy-conservation the heating of water and after heating, in society, existing greenhouse is just applied to some extent in very limited field, and in life, in fact have a lot of place to utilize, such as need the place of heating for water to use greenhouse.Also swimming pool is can be or bathing pool is heated as greenhouse.Swimming pool or bathing pool can be flow to after greenhouse heating water.Water also can circulate between greenhouse and swimming pool.Swimming pool or bathing pool also can be that swimming pool or bathing pool can be provided with greenhouse in greenhouse, such swimming pool not only can heat pond water can also heat whole indoor make people in water or in indoor winter people also can not feel a sense of cold.Can only need, with the heat energy of the sun, also can give again to heat in greenhouse while utilizing the sun.
What more than say is also can keep off the rain for salt pan simultaneously keep out the wind as saltpan method salt manufacturing can arrange the temperature that can improve warm indoor water in greenhouse on salt pan, the water vapour be evaporated in greenhouse can be also warm indoor exhaust or decompression by fan or off-gas pump or vacuum pump, decompression can form low-pressure distillation, water in greenhouse reduces temperature and exhaust decompression can be stopped to evaporate when water temperature is not enough by evaporating, allow water intensification for some time in greenhouse.Greenhouse heats up also can greatly strengthen heat absorption capacity because the temperature difference outside in greenhouse and greenhouse is very large, and again heating up to the water in greenhouse has brought condition.Exhaust body device can be located on greenhouse body and also can not be located at greenhouse body by exhaust body device from greenhouse to outdoor pump drainage gas, exhaust body device also can in greenhouse, also can establish one or more container for evaporation in greenhouse, container for evaporation can to emission gases outside greenhouse.A large greenhouse Inner can establish one or more container for evaporation, and greenhouse can have one or more, has the greenhouse of container for evaporation also to can be and one or morely carries out work.Water can evaporate and can Exposure to Sunlight heat up or naturally heat up in greenhouse in greenhouse, and the ramp cycle that can circulate in work is evaporated.
The various ways in six greenhouses, 1, can coverture around covering the greenhouse made, or greenhouse same or analogous with existing greenhouse.2, the daylighting greenhouse made with light-permeable Fu Gai Wu Gou or Exposure to Sunlight greenhouse, or the greenhouse that naturally heats up.3, to heat greenhouse, that is described greenhouse of heating heats Ke Gei Ponds room again, its method can with can be water heating can be maybe Greenhouse Heating various method or existing can heating means can, particularly existing greenhouse and greenhouse gardening greenhouse or aquiculture green house have a lot of year history, the various technology in its greenhouse and add temperature technique and can be combined on the greenhouse that the present invention is used or improve use.It need be only that water heats up by day be also the method for most convenient like this that certain the present invention greenhouse used can not need to heat.4, greenhouse container for evaporation, namely with coverture, water can be provided with on this greenhouse body the device of pump drainage gas around the greenhouse covering formation, namely said container for evaporation is similar or identical so this greenhouse can be described as greenhouse container with the present invention.When one or more container for evaporation established by needs in a large greenhouse, also can there be exhaust body device in said greenhouse with No, steam can be discharged greenhouse by container for evaporation.5, combine with the technology of various or existing various salt manufacturing or desalination water processed the greenhouse utilized, namely existing salt manufacturing or desalination water processed also have a variety of method but they have many times also need for water heating or preheating, such as used distillation method salt manufacturing or desalination water processed or condensed water need have in the work such as refine thing from water much all to be needed to heat for water, also have reverse osmosis method sometimes also to need feedwater to heat, etc. need in work as such to heat can use greenhouse.And all can utilize greenhouse to above-mentioned similar work.
Seven air-conditionings, true container of the present invention needs to absorb heat in evaporative process, the water in container can be made to turn cold, the water be connected with container in other words or air are absorbed heat by container and turn cold, and water mentioned here also can be that the water of the outer flow path container of container is turned cold by container heat absorption through the water of container.Water in other words in the outer water that is connected with container of container or air or container can be evaporated or container for evaporation and turning cold, and the water turned cold or air can be used for refrigeration or when air-conditioning uses.
Apparatus of the present invention to have in three kinds of functions and salt manufacturing water refrigeration work and three kinds of functions can use simultaneously and also can select one or more.Also air-conditioning can be specifically designed to, namely not necessarily have to salt manufacturing or desalination water processed when idle call.It can freeze and also can heat, need heat when being also can by the compressed vapour steam that produces of compression container thus can obtain heat in other words, the heat obtained not only may be used for air-conditioning and namely to wither temperature, also may be used for heating water or air, also can be used for heating salt manufacturing or desalination water processed water used, the heat produced when steam being become liquid by prior art is in other words used for again to container heating or heat to water used.This device is used for air-conditioning can one one, also many users a device can be shared, such as the water or air that are reduced temperature by container for evaporation can be inputted many users by pipeline and be used for refrigeration, its method also can as the water-cooling system in central air-conditioning.Also can be delivered to by the air of absorbing and cooling temperature the place needing cold air by being connected with cold water pipe by blower fan, above said water can be water outside container owing to being connected with container so can by container for evaporation absorbing and cooling temperature, said water also can be the water in container, and the air heat absorption outside coupled air and container also can turn cold by same container.Also have in existing central air-conditioning and chilled water inputted many users, air-conditioning plant of the present invention due to very similar with central air-conditioning so a lot of component and using method all can be combined with central air-conditioning and improve.Because apparatus of the present invention can not need to heat or Exposure to Sunlight intensification at the water for using during air-conditioning, so normal-temperature water or Natural Water can being used in work even to use by sending into user after container for evaporation cooling with underground water, not needing the water of Exposure to Sunlight process by this or do not need the water of heating also referred to as natural intensification water or Exposure to Sunlight intensification water herein.Only make up water need be given when water is not enough when this air-conditioning plant also can simply work than the few structure of existing common idle call electricity.Due to air conditioner energy saving of the present invention so its purposes also can be used for multiple, such as also may be used for low temperature plantation or cold temperature culture, can indoor plantation or cultivation with the refrigerating function of this device be room temperature lowering or adjust Warm, namely by present method can plant some extremely frigid zones growth rare medicinal herbs plant some species needing to grow in cold environments in other words, also can cultivate the animal or plant grown under some need cold environment.Existing chamber planting vegetables also useful greenhouse cultivation, existing also can plant or cultivate some animals and plants higher to temperature requirement with this device to indoor temperature control or cooling.Also can claim above is low temperature breeding.
Eight ice, can be reduced to zero degree by water temperature at work according to known apparatus of the present invention described in the application documents of last time.Evaporated by water or seethe with excitement and the outer water be connected with container of the water in container or container can be made to reduce its temperature of temperature can be reduced to zero degree, certainly can also be low again.As you know the temperature of water be down to zero degree will Cheng Bing.Apparatus of the present invention are the equipment that can have three kinds of purposes, and the steam be namely evaporated can desalination water processed, and the water concentrated by evaporating can salt manufacturing, and the water turned cold because of evaporation or air can be used to provide cooling or refrigeration.From application documents, it can also be seen that this device is that energy salt manufacturing simultaneously desalination water freezes the multifunctional equipment that three kinds of work is integrated, three kinds of work can be carried out and mutually unaffected simultaneously, certain three functions also can optionally one or its=.Temperature at work as water said in application documents can be down to zero degree that is water can become ice, three kinds of functions of this device are not affected when water becomes ice yet, namely ice can freeze, water becomes ice also can concentrated seawater or salt solution and salt manufacturing, as existing cold method salt manufacturing, ice also can be used for desalination water processed.
Container for evaporation of the present invention can freeze, namely be no matter water in container or the outer water be connected with container of container can be turned cold by heat absorption because evaporating, when water temperature be reduced to can freeze time water just can become ice, just can concentrate water if at this moment ice is taken out, this feature is utilized to can be used for concentrated brackish water or seawater and salt manufacturing, or utilize this feature be used for condensed water from condensed water again refine go out in useful matter etc. and all can use like in work, this method is very similar with existing cold method salt manufacturing, water can be made in work repeatedly to freeze and repeatedly to get ice again.Also ice can be used in the work such as refrigeration or desalination water processed.This device also can be ice-making machine, namely water temperature reduction finally makes water become ice because of the cooling of container evaporation endothermic by the water in container or the water outside container, container also can being provided with and getting facility needed for ice or ice porthole is got in setting, namely the ice in container can be taken out from getting ice porthole.Certain ice also can be outer as also the water outside container or the water be connected with container become ice by container at container, also can utilize this device organizational system ice plant.Be transported to by ice and need to use ice place, ice can be mainly used in millworker's cooling and fresh-keeping two aspects of product, the especially market of farm produce, and Shang Changhe hotel is larger in order to ensure the fresh demand to ice cube of fishes and shrimps crab.Transformation can also to be carried out to equipment with the ice making of this device can also arrange ice taking-out mouth as container or be designed with the technological facilities required for taking-up ice.Namely this device also the water in container can be become ice then open ice taking-out mouth or open container take out ice, the water for cooling that also outside can be connected with container and become ice, said ice of getting also comprises from getting ice container, and this ice-making machine can be more energy-conservation than common ice-making machine.
Nine heat,
Also mentioning water used in work in the present invention can be nature intensification water or Exposure to Sunlight intensification water, nature intensification water also can be underground water, brackish water itself as released from deep under ground in rock salt salt manufacturing work have certain temperature here this water also referred to as natural intensification water or Exposure to Sunlight intensification water, for also may underground water be used during refrigeration air-conditioner.In addition also propose can be varied certainly for water its heating mode of heating, as long as can be able to use for the method for water heating or existing method, wherein also include said solar facilities to heat up, solar facilities has the utilization of solar water heater or solar collection element, also have sun power Warm room etc., existing solar facilities also few of kind can seek to utilize from existing installation.Said for water heat also comprise people for heat or artificially power consumption heat, if only say that in this claim water used is nature intensification water or Exposure to Sunlight intensification water, so there is people to be fed water again by power consumption or other method to water used again and add the scope that some temperature just may exceed claim like this, so want herein to draw a boundary line to heating, 1, said water used is that nature intensification water or Exposure to Sunlight rise Warm water and can be defined as water used here and be mainly nature intensification water or Exposure to Sunlight intensification water herein, there is provided evaporation institute's heat requirement for container or water source is provided.2, more than be defined as water used and be mainly nature intensification water or Exposure to Sunlight rises Warm water, may be defined as again in the water temperature in the water Warm when water of evaporation institute heat requirement or evaporation are provided or when evaporating in container and have at least half or temperature over half to derive from nature intensification or Exposure to Sunlight intensification, its Exposure to Sunlight heats up to comprise and utilizes sunlight heat up for water or utilize solar facilities for water intensification etc., naturally heating up to comprise variously does not need people for heating or do not need artificial power consumption and can utilize various natural condition and heat up yet, alternatively add Warm without people for heating or artificially consuming energy, also comprising the temperature recycling that produces when steam becomes liquid into water the form such as to heat.In above 2 definition, said water sometimes also comprises the water that need enter container and also can be included in the outer water be connected with container of container, provides evaporate institute's heat requirement because the water sometimes outside container is connected with container or flows through container to container.Here intensification or Exposure to Sunlight rise Warm and mainly say that all can not need people to be the water that naturally can obtain temperature of heating of heating or artificially consume energy naturally.
Heat heating of saying here of feeding water of saying below is generally say to feed water the form of heating with power consumption or artificial power consumption, and artificial power consumption generally refers to the heat form being required to be energy consumption and paying a price.
The explanation of fist example, in the work of one producer, the water temperature of container for evaporation when evaporating in container is 35 degree, the water temperature of 18 degree is wherein had to be naturally heating up or Exposure to Sunlight intensification not before heating, after be heat that to make water temperature turn improve 17 degree of final water Warm altogether when evaporating be 35 degree by people again, the half that this situation is described just or water Warm over half are from intensification or Exposure to Sunlight rise Warm naturally, if instead people be heat be 18 degree heat before original water temperature be 17 degree, so just can not be counted as half or water temperature over half from naturally to heat up or Exposure to Sunlight heats up.Certainly the Warm of adding mentioned here is mainly said and to be heated for water by artificial power consumption or artificially power consumption is direct heats for water, such as the steam utilizing container for evaporation to be evaporated when becoming liquid producible heat again with thinking that water is heated, or above-described greenhouse heats up and solar facilities heats up utilizes underground Warm water or ground temperature to be that water used is heated in other words, this several form of heating artificially consumes energy at last or artificially power consumption, directly for water is heated, can only calculate nature intensification or Exposure to Sunlight intensification.Besides steam heat because above-mentioned power consumption heating water time can consume energy again when can produce steam and utilize steam to reheat water, even if be the composition that the temperature have to said in steam has artificial power consumption, also can only calculate half or temperature over half in the temperature of the steam when adding Warm 17 degree so described above from naturally to heat up or Exposure to Sunlight rises Warm, the heating of this form can not be said, and to be that artificial power consumption is direct heat for water.Having that many naturally can to heat up or not need to pay energy penalty be that the method that water heats up all may be used in present device in daily life, wherein can understanding water temperature in described half or half one from naturally heating up or Exposure to Sunlight intensification by above given example.Present device said can for water heat that yes arbitrarily heating mode how many degree water temperature of also no matter having heated all be fine, be not be only limited to water temperature in half or half one from naturally to heat up or Exposure to Sunlight heats up this condition, this saying is just striven considering this singularity of patent document.In order to the protection being more conducive to patent right here can also say another scheme of apparatus of the present invention be evaporate time water temperature can be less than 40 degree or 40 degree, temperature when steaming in other words can be less than 45 degree or 45 degree, less than 50 degree or 50 degree in other words.Certainly this device is not limited to stating of above table in can working at any temperature.
Ten, can increase container water capacity, liquid boiling speed is relevant with original temperature with the volume of liquid as you know, and the boiling point of liquid is relevant with the air pressure of fluid surface.The two large factors affecting water boiling speed are exactly the original temperature of the volume of water and water, an important inventive point of the present invention is exactly the appearance volume of water expanding container, the free energy that recycling can heat up naturally or Exposure to Sunlight heats up, thus the two large factors that change affects water boiling speed improve a liter product benefit with reaching required order.That also can save exhaust body device uses energy.Use in the clear file in the Shen of last time in the character express expanding evaporation area raising working efficiency work and needed to expand evaporation area, wherein expand and to refer on original basis and expand so what said in application documents last time is expand a kind of scheme that evaporation area have also been enlarged the heat content of water simultaneously again, saidly expand the volume that evaporation area also can expand water simultaneously as seen, apparatus of the present invention can be that to evaporate also can be the no matter water that seethes with excitement be that evaporation or boiling can expand evaporation area at work, expand evaporation area and be conducive to evaporation, expand the favourable water boiling of volume of water.Present device only has step-down of feed water to need people for paying energy penalty with relevant three factors of boiling, and expand the volume of water and feedwater heat up both can not need to pay pay in other words little.Expand the volume of water can make a larger container or make a larger container that can seal, feedwater heats up also can use solar facilities or greenhouse, or the various favourable conditions of occurring in nature can be utilized to be that water used is heated with nature intensification water or with not needing artificial power consumption, even can utilize underground water or underground warm water, or the underground brackish water of saltern also has certain temperature, can artificially consume energy in a word for water heats up.
To have also been enlarged due to the heat content in the expansion container of volume of water and original water Warm is lower also can have more greatly and equally extraordinary boiling effect due to the volume of water in container, so the another scheme of this equipment propose also can not millpond or need not Heating system again, only with seawater or the water of natural flow directly can enter container and carry out work, such benefit is that the land used can saving intensification pond also saves the time of heating up again in pond simultaneously.This form be generally independent for the work of water processed or desalination water processed in can use, because desalination water processed can without recycle-water, not only after the water of the water or water temperature deficiency that reduce temperature in container can being released container in working but also from newly entering new water again, the water of releasing can return in container.This working forms generally can with the larger container of a water capacity, the water yield entering or release container in work also can be very large, water inlet and the releasing water of container also may be very frequent, the a large amount of water of container may be entered and may release after water-cooled 80 percent water, so an applicable position can be looked for arrange container for evaporation in order to energy-conservation thus the water entering container and release container can be made can artificially to consume energy container of just automatically coming in and going out, namely can be the water power passing in and out container as the similar energy facilities such as lift pump or human factor consumption energy consumption masterpiece, the water that just water can be made automatically to flow to container flow container that can artificially consume energy in this work is claimed Natural Water or natural flow water by the present invention.Advocate and container is arranged at and can reaches energy-conservation in the water of natural flow.
The present invention by sea water desaltination also referred to as purifying waste water, no matter be can use larger container in the similar work such as salt manufacturing or desalination water processed, the container for evaporation that water capacity is large is favourable to work, be described to container size used or water capacity size here, owing to considering that the singularity of patent document is so the size of the size water capacity in other words having used multiple data to express container below, namely the container water capacity of present device can be more than 1 ton, or more than 2 tons, or more than 3 tons, or more than 4 tons, or more than 5 tons, or more than 7 tons, also can be more than 10 tons or 10 tons, also can be more than 15 tons or 15 tons, also can be more than 20 tons or 20 tons, also can be more than 25 tons or 25 tons, also can be more than 30 tons or 30 tons, also can be more than 35 tons or 35 tons, also can be more than 40 tons or 40 tons, also can be more than 45 tons or 45 tons, also can be more than 50 tons or 50 tons, also can be more than 55 tons or 55 tons, its water capacity also can be more than 60, or more than 70 tons, or more than 80 tons, or more than 90 tons, or more than 100 to 200 tons, or more than 200 to 300 tons, more than 300 to 500 tons, or 600 tons, or 700 tons, or 800 tons, or 900 tons, or 1000 tons, container used can also be not limited to more greatly above data by water capacity, the container that should be arbitrary size can, container water capacity can its water capacity very large also can be that hundreds of ton or a few kiloton or several ten thousand tons are even more than hundreds of thousands of ton in the application, certainly want container hour also can very I flexible Application as required.
Appearance water water surface area in container used greatly i.e. evaporation area is conducive to greatly evaporation.Water surface area is greatly also conducive to accepting Exposure to Sunlight and heats up, the water that Exposure to Sunlight that what this device was said can accept heats up can be also can be in container for evaporation in pond, such as transparent vessel just can heat up in container in Exposure to Sunlight, container can also can in pond outside pond, and what also can say as said greenhouse container for evaporation is exactly that water in the container made of available transparent object can heat up by thoroughly entering the sunlight of container.Present device water used be no matter in the pond that can accept Exposure to Sunlight and rise Warm or in container below by its water surface area in other words evaporation area to a statement, namely its water surface area can be more than 5 square metres, numeral conveniently by such as 5 square metres to save with more than upper square metre several word and only write numeral, namely its water surface area is more than 5 square metres or 8, 10, 13, 15, 18, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 100, 120, 140, 160, 180, 200, 230, 260, 300, 350, 400, 450, 500, 600, 700, 800, 1000, 1500, more than 2000 square metres, several word more than should having after each numeral above square metre, individual or word also should be had before numeral, consider the singularity of patent document so just write multiple data like this to have carried out thinner description to the water surface area of water used.Certain water surface area also can be that arbitrary size also very littlely can be not limited to above data very greatly.Pond used in work or container can be generally multiple can certainly be one, and the number plays of above water surface area are the water surface area in one of them described pond water surface area or a container.
Sum up Partial Feature of the present invention, 1, container evaporation is entered in the water drainage of energy natural flow, releases container after water-cooled and can return container again.Indicate the water of natural flow referring to and artificially need not consume energy at work and can automatically flow to or pass in and out the water of container of saying here, to make the water entering container or turnover container in work artificially consume energy, as can without water pump or similar energy device in work its order.Above as being an inventive features of the present invention, certainly also the devices such as water pump can be used at work.2, water can first heat up in greenhouse before container, first carries out nature intensification or Exposure to Sunlight heats up or heats in other words, and the water after intensification evaporates in container, and the cold water after evaporative cooling can flow out and not return.3, first heat up and evaporate in container again, evaporate the water turned cold and heat up again, evaporate in container again after intensification and namely form circulation intensification or circulating and evaporating.Described intensification can heat up and also can heat up in container in pond, also can heat up in any water position, and after can heating up in pond, flow to container evaporation, after evaporation turns cold, flow container enters pond intensification again.The water that also pond and container can be integrated in the i.e. container water that to be also the water in the water pond in pond be also in container, its water also can not need shift position in circulation temperature-rise period.Dated said intensification can be nature intensification or Exposure to Sunlight intensification or solar facilities and rises Warm or solar energy greenhouse intensification or heat, various heating mode can apply simultaneously also can appoint one or its=namely it third-class 4 use according to condition, the said evaporation of device in the present patent application also comprises boiling form, the said intensification naturally heated up as not needing artificial power consumption.4, the said container of the present invention can be the various containers that can hold water, is provided with the container of exhaust body device outside container in vessel port, and its form not to be limit in figure drawn several.Said container divides sealed vessel and blow-by container, and blow-by container comprises the u shape pipe container for evaporation in there being u shape pipe.Sealed vessel mainly say in container except arrange exhaust body device vessel port and except hold No in device when vacuumizing and have other vessel port.And blow-by container also has other vessel port and this mouth blow-by in the mistake vacuumized except the mouth of exhaust body device.Blow-by container as this container having flowing water mouth 9 of Fig. 3 Fig. 4 Fig. 6 Fig. 8, when vacuumizing flowing water mouth 9 can blow-by and water in container can simultaneously inwards stream limit flow inwards, the water in certain container also can not flow.Flowing water mouth 9 is had namely also a kind of sealed vessel can be become by flowing water mouth 9 also being made when putting to be connected with appearance basin bottom make flowing water mouth 9 to be sealed by pool bottom in blow-by container.Also can blow-by the water in container and the aqueous phase outside container can be made to connect.5, expand container water capacity and utilize and can naturally to heat up or Exposure to Sunlight heats up for water, change two large factors affect boiling speed, raising working efficiency thus also can save exhaust body device use energy.Expand evaporation area in container and also can improve evaporation effect, as water Exposure to Sunlight in transparent vessel heats up the water surface area thus raising Exposure to Sunlight effect that also can expand in container.6, this device also can be used for refrigeration or ice making, and ice making also can concentrate brackish water and salt manufacturing, also can with ice desalination water, and also ice can be passed to many places need be that this device also can be ice-making machine with the place of ice.7, greenhouse, the greenhouse said in the application can be identical with the identical using method of existing greenhouse principle same configuration, utilizes as existing planting greenhouse and aquatic products greenhouse have a lot of experience can be combined with the greenhouse that the present invention says.Greenhouse technology is not limited to just for the said device of the present invention, and greenhouse can be used in all salt manufacturing or desalination water processed or the work of purifying waste water, and from seawater, refine goes out salt and being operated in identical principle of other many kinds of substance can utilize greenhouse.8, exhaust body device institute pump drainage steam out can be utilized in the container of the form of ownership that the present invention is used or in pond of heating to heat again, and the heat produced when namely utilizing the heat of steam to utilize steam to become liquid in other words heats or water feeder heating to container heating or feedwater again.Also pipe 6 as said in Fig. 2 can be provided with in various container or pond.6 li, pipe can have steam to pass through.
See Fig. 1, water 4 is filled in container for evaporation 1, container 1 can there is space 3, upper vessel portion is provided with to the device volume of external container pump drainage gas, as exhaust body device 5 etc., water in container and leave certain space between exhaust body device 5, when vacuumizing, water can not be drawn out of container, owing to making air pressure reduce under vacuumizing in container, to such an extent as to makes water 4 keep boiling or rapid evaporation.Can make air or water outside container at container 1 ambient dynamic for evaporation provides heat, the air outside container or water can be described as and carries warm body or heat-eliminating medium.Intake when container 1 also can have water-in need, can seal after water inlet.Container 1 can not have space 3, space 3 also can be set more water or the air heat transfer water be beneficial to in container that flows between space can be made to provide heat energy.This device may be used for salt manufacturing, or desalination water processed or purify waste water, and also may be used for refrigeration.Salt manufacturing is exactly reprocessed after evaporation concentration by the seawater of 1 li, container, finally obtains salt composition or salt crystal.Desalination water processed or purify waste water, namely becomes water by the steam prior art of extraction exactly and makes it purify.Or make sea water desaltination for people.Refrigeration is exactly utilize in evaporative process the refrigeration needing to absorb air or water reduction temperature that the hot feature causing temperature to reduce makes to flow through container surroundings to be used.In this device refrigeration, the patent No. can also submitted to reference to me is the application material of 201410004375.5, both can be in conjunction with, can improve, can with reference to utilization, the container 1 described in this and the patent No. are that in the material of 201410004375.5, said container 1, principle and technology all can be identical.Also can utilize this device refrigerating function due in the work that sea water desaltination in the technology described in this is purified waste water in other words, the steam extracted out by off-gas pump is lowered the temperature after also can flowing through and around container for evaporation 1 or another container 1, steam being inhaled to be temperature and is finally formed water (desalination water or purify waste water).So the refrigerating function of this device is done more detailed explanation in conjunction with 2014100043755 (below referred to as patent last time) patent document below.
As said container 1 in last time patent can be put in outer case 6, air is made to enter to go out from venting port 8 from inlet mouth 7 (with reference to patented material last time) again by blower fan.Certainly wind is out cool breeze, and this device just can work as air-conditioning use, can again to make up water in container during water deficiency in container.In order to room air too wet can not be allowed, also can the steam extracted out be discharged outdoor by pipeline.When the space that the water that container is 1 li and off-gas pump keep certain makes to bleed, water can not be drawn out of, and does not fly when seething with excitement to make water in off-gas pump, also can arrange one this can the applicable material of block water, make it water can not be extracted out.This device is when air-conditioning uses in summer, and refrigeration is fine, and as summer is indoor, temperature is all at about 30 DEG C, and this temperature can be seethed with excitement completely under vacuum low-pressure to make the water of 1 li, container.The water that container is 1 li has superpower heat absorption capacity in boiling, and the water and air through container surroundings can reduce temperature very soon.To such an extent as to water temperature can be reduced to 0 degree.Just more easily play good cooling-down effect as the water in container becomes 0 degree, and only need room temp to reach for 20 several years as enjoyed the cool summer just very pleasantly cool.This device due to very similar to existing air-conditioning, as the vaporizer in existing air-conditioning is all very similar with the container as described in condenser and this device, so parts on this dress and existing air-conditioning or construct and can utilize or make it more perfect with its combination.The space 3 of container 1 can be The more the better, or as common air-conditioning, outside refrigerant container, add some be beneficial to the material inhaling temperature or loose temperature, on refrigerant container or official road, add some tinsels better pass temp effect as used in existing air-conditioning to reach, etc. method can have multiple, carry out being combined with present air-conditioning technical processing to this device, improve.
After air-conditioning technical combines design too now, this device also can have power control, as power switch, or the large mini controller of electricity.In various containers in this material, the device of pump drainage gas also can reach by controlling electricity size the object controlling refrigerant evaporation or boiling speed, certainly also just can play the effect regulating temperature height.This device also can have the device of Temperature displaying, and power switch also can have the class of different stage, thus reaches the object of different class temperature adjustment.The heat-eliminating medium of this device can be air also can be water, namely water temperature can be reduced this water in water cooling medium after utilizing the water that can flow to be absorbed heat by the flowing of 6 li, the pipe around container for evaporation or shown in Fig. 2, also water medium can be transported to when doing heat-eliminating medium with water at a distance as on multi-story, namely a container can be at a distance many local coolings, also can by blower fan circulation blowing, make air by the container of heat-eliminating medium or pipeline, also can play the effect reducing room temp.Also cold water or freezing air can be inputted as in caliduct, namely winter is for the pipe-line equipment that heats etc., can be used for refrigeration to summer, this device not only can make it become water for being used for condensed steam during desalination water processed, can also have multiple use comprising in the work such as air-conditioning, refrigerator, freezer commercial refrigeration.The above combine the patent No. be 201410004375,5 content carried out thinner this content of explanation be also this application in summary of the invention.
Figure 2 shows that the schematic diagram that heat-eliminating medium can be flowed in container 1 by pipe 6, wherein a pipe injects 1 li, container from container 1, to spiral in container distribution, bend is arranged in container more, make the Rong Shuichu in container can have pipe 6 branch, the water that pipe is 6 li or air can flow to the water extraction heat supplied in container, also can make the water in pipe or air cooling simultaneously.Also the cooling air in pipe can be enjoyed the cool by blower fan behaviour of producing by boasting in summer, also the device shown in this Fig. 2 can be loaded in the outer case 6 as described in last time patent, from venting port 8, discharge cold air.Pipe 6 in container can be plastics tubing, and the various material such as rubber hose or metal tube can.The two ends of pipe 6 are at container place, and rest part is in container, and the part in container can be fixed by support, and heat-eliminating medium flows to and flows out from another port from the Single port of pipe 6.For the water extraction be close in the container of pipe 6 supplies evaporation heat.This method is than simple during structure fabrication shown in Fig. 1, and cost is low, easy to use.Pipe when going out container, can by elasticity preferably as the sealing of the material-mix such as plastics or rubber makes it keep the water in container can not flow out from intersection in the intersection of container.
Having fallen warm water or air because of evaporation and also can drain into many users for refrigeration of 6 li, pipe, its method also can as the heating plant in winter and steam heating, be used for freezing to summer, user is inputted by cold water or freezing air pipeline, also can air be forced to move from cold pipeline or cold dish pipeline upper reaches with blower fan and reach the order ground reducing air themperature, this form is very similar with the water machine system of existing central air-conditioning so can in conjunction with the water machine structure in central air-conditioning, or water circulation system of central air conditioning.Also can learn from other's strong points to offset one's weaknesses.
Fig. 3 and Fig. 4 Figure 5 shows that container for evaporation 1 bottom has flowing water mouth 9 not need the form sealed, water when container for evaporation in fig. 1 and 2 works in container is sealed, and Fig. 3 and Fig. 4 lower vessel portion has flowing water mouth and need not close, during work, flowing water mouth 9 is inserted in water, water flows into container from flowing water mouth 9, make the space that the water surface in container and off-gas pump keep certain, this space is seal cavity, the outer water surface 19 of container is had shown in figure, the flowing water mouth 9 of container is inserted under the outer water surface 19 of container deeply, the water surface when off-gas pump is bled outside container in container can to rising one segment distance because of draught head, as illustrated in the drawing in container shown in the water surface 18, but can keep at a distance with exhaust body device 5, when bleeding, water can not be drawn out of.Fig. 4 is the container 1 that the form revealing multiple pipe is removed in bottom by sealed vessel 1 as shown in Figure 1, namely many connect together as Fig. 3 tubular vessel 1, top has between each pipe of exhaust body device 5 and has space 3, the same with the container 1 shown in Fig. 3 during work, but the water of the structure shown in Fig. 4 operationally outside container can flow and is conducive to evaporation transferring heat between space 3.Packing less its benefit of container 1 in this bottom of Fig. 3 and Fig. 4 the water in container and outside container can be connected, and than convenient during the water inlet of this sealed container of Fig. 1 and Fig. 2, and can evaporate the water of more multicapacity, the water namely outside container simultaneously.Water outside container can also flow and be conducive to like this draining time anxious for the water reducing temperature because of evaporation, the water come with stylish stream can also provide heat to evaporation, this structure as salt manufacturing can in concentrate container with the water outside container, water wherein used also can by Exposure to Sunlight or with burning coal and burn other can combustionmaterial, maybe can with the means such as power consumption be water heating, thus for evaporation heat is provided.Container 1 can in a channel, and the water come from upstream flow also can provide heat for container for high-temperature water flows through container 1, and water flows to downstream after being lowered the temperature by evaporating.The water flowing to downstream can reclaim, and repeatedly circulates like this, reach repeatedly the object of condensed water as it carried out Exposure to Sunlight or again flowing to container after artificially heating.If for desalination water processed, also can not reclaim, circulating and evaporating can certainly be reclaimed as above-mentioned saying.The wherein water channel identical with Fig. 3 of container 1 shown in Fig. 5 base plate 12, its effect be because vacuumize evaporate time, the water surface in container can higher than the water surface outside container, so temperature can not be passed better with the water outside container higher than the part of the outer water surface of container in container absorb heat, in this case also water channel base plate 12 can be set, namely water channel base plate 12 also can have flowing water above, exceeds the part heat transfer of the outside water surface to internal tank.Water channel base plate also can be channel lower shoe, or pipeline bottom etc..
Container 1 shown in Fig. 6 Fig. 7 is the container for evaporation of a kind of form with two pipelines and A pipeline 7 and container B pipe 8, and the lower end of two pipelines is divided separately flowing water mouth 9 and flowing water mouth A10.
To Figure 7 shows that when utilizing this container work can by water from flowing water mouth 9 flow to container then again can from water export 10 operating diagram of flow container 1, in figure water from outer inlet channel 13 by the drainage influent stream mouth of a river 9, can again can along container B pipe 8 to dirty after A pipeline 7 flows upward to certain altitude after water enters A pipeline 7, finally can water export 10, we can be described as U-tube container for evaporation, just as letter U is squeezed by the container in upper and lower two water routes of first up and then down formation this water in container.
From shown in Fig. 7, see that the water i.e. water surface site of outer water inlet 14 outside container is high, and the position going out the water of container and water outlet 20 is lower, so can see water outlet can flow in automatic streamline mouth 9 container not only automatic rise then in A pipeline 7 but also automatically in container B pipe 8 to dirty so that last flow container, this process can complete completely automatically.This form is also the improvement made for the deficiency in Fig. 3 and Fig. 4 work, can find out that after this improvement the water of the operationally disengaging surface of the container shown in Fig. 6 can flow fast, more effective than Fig. 3 and Fig. 4, be conducive to timely disengaging surface being evaporated the water having fallen warm low temperature like this to drain, the water simultaneously also carrying out new high temperature to timely vaporize water surface current is with supplementary evaporation institute energy requirement.The benefit that in view of this U-tube container is maximum can make the water quick travel of disengaging surface thus bring favourable condition to evaporation.
Figure 8 shows that U-tube vaporizer, be wherein made up of many pipes have two A pipelines 7 and a container B pipe 8 as shown in FIG., during work, water can enter container 1 again from container B pipeline out from two container A pipelines simultaneously.Method also can be made on a container 1 thus more A pipeline 7 and more container B pipe 8.As long as the said U-tube container of multiple exhaust body device 5 also can be had on a container 1 to be to have at least one container A pipeline and a container B pipeline, namely in a pipe, can claim U-tube container in another root pipe of upper reaches to dirty such container after water enters container, said container A pipeline and container B pipeline can be that what to justify also can be the different shape such as flat.Evaporation area 11 in figure refers to the disengaging surface in container 1, and in this device, the velocity of flow speed of water also determines the speed providing heat, and the size of the vaporize water area in evaporation effect and container is also relative.So expanding evaporation area is well improve the method for evaporation effect.In the prior art as in existing vacuum salt production technology, owing to limit by provided limited (steam) heat in work, so expand evaporation area not have good effect.Namely its evaporation effect is subject to provided (steam) heat how much relevant, and consuming how many coals, to provide how many heat of vaporization to go out how many water vapors be all definite, does not increase consumption coal heat supplied also do not have much meanings if expand evaporation area.And the present invention's U-tube container used as shown in Figure 7 at work, can with the water not stopping to flow in container for evaporation provides heat, the water at low temperature flowed out not only but also can flow to container, water cycle Exposure to Sunlight circulating and evaporating again after Exposure to Sunlight heats up, and the heat in visible U-tube vaporizer is unlimited.Utilizing circulation Exposure to Sunlight to provide evaporation heat, can be not the complete inexhaustible free energy of use, and evaporating in container by regulating water flow velocity flow needs how many heats just to have how many heats.
The off-gas pump that same container 1 is onesize, the steam can extracted out because the evaporation area in vaporizer varies in size is how many also different, namely the steam of the larger extraction of evaporation area is more, the steam of the less extraction of evaporation area is fewer, so can greatly improve evaporation and working efficiency by the means expanding evaporation area in apparatus of the present invention, that can also save off-gas pump uses energy simultaneously.
This advantage of the present invention is rare in the prior art, as used vacuum salt production technology, if want, with the off-gas pump many extractions steam expanding evaporation area, coal must be burnt more or supply steam thermal energy more, namely pay more with can money be opened, on raising working efficiency, do not play much effects thus.And apparatus of the present invention expansion evaporation area not only more can extract steam out, and because employ the free energy so the energy consumption that energy consumption spending can also save off-gas pump need not be paid more, apparatus of the present invention can improve evaporation effect thus, also improve working efficiency simultaneously.
Fig. 9 is as pond 16 in Fig. 7 device busy and water route 17, vaporizer location 15 is arranged between water route 17, wherein water heats up in pond 16 after Exposure to Sunlight, drained into vaporizer location 15 again by water route 17 and entered container for evaporation 1, again flow into pond 16 by water route 17 again from container 1 water out and carry out Exposure to Sunlight, Exposure to Sunlight flows to again container evaporation after heating up, cycle operation like this.From figure, see that water can flow out from west 21 1 side in pond 16 enter container 1, pond 16 is entered again from east 22 1 side in pond 16, can see in outlet sump 16 and lean on the water-cooled of east 22 one side but become high temperature again, so can ensure there are enough heats in container for evaporation through Exposure to Sunlight water when it slowly flows to west 21 one side.It can also be seen that the water flowed in pond is more volatile than the originally static water capacity, fallen warm water by container and more easily absorb heat in pond.
The above may be used for salt manufacturing, namely the water in pond 16 can be concentrated, also can be again concentrated until make salt crystal in salt field by condensed water as the workman's method of work of salt pan after concentrated, as vacuum salt production conventional now, concentrated water can be entered used vacuum salt production program again, last that yet directly can enter existing vacuum salt production does not imitate evaporator room yet.The program of entering makes finished product salt.Also whizzer can be adopted the solid part in saturated salt solution to be isolated, finally obtain salt or other useful thing.This method can reduce a large amount of salt pan lands used, also can shorten working hours, and has waited multiple benefit, condensed water can certainly be entered the container 1 as this closing forms such as Fig. 1 and Fig. 2, it be become in container highly enriched salt body.Container 1 working forms shown in 7 figure is more suitable for building large-scale salt manufacturing factory or large-scale system desalination water factory or water purification plant.And also can be suitable on family or ship shown in Fig. 1 and Fig. 2. Che Shang. wait little form purposes.
During work as shown in Figure 7, exhaust body device 5 can not be drawn out of to the water of the outer pump drainage gas container of container 1, water can be high due to the water level of outer water inlet 14, and the water level of water outlet and water export 10 or water outlet 20 low (in figure, the water surface of the low outer water inlet 14 of the water surface of water outlet 20 is high) thus work time water automatically can flow to container flow container, the water of flow container also can above with lift pump water being pumped to as pond 16 in make its water can be equally high with the water level of outer water inlet, thus ensure that again automatically flowing into container 1 carries out circulating and evaporating.Again enter container carry out circulating and evaporating because the water of flow container can reclaim in the work of desalination water processed, if so choose the position of outer water inlet, can arrange container 1 so works from a position of upstream toward downstream flowing as selected a water and just without lift pump, thus power consumption can be reduced.Certain desalination water processed also can as shown in Figure 9 by Water Sproading circulating and evaporating, can also in the sea when container 1 in Fig. 7 needs, or arrange in pond, as A pipeline 7 is inserted in marine or pond, again container B pipe 8 is inserted one as in the spill environment of basin, with lift pump the water in basin can will be flow in container automatically to basin extracardiac pumping during work and normally work.The place that yet can be discharged to the water of extraction from container 1 is farther by pipeline when needing is not low to ensure the water temperature of container surroundings.
The above is vacuum desalination water of the present invention, and its process of salt manufacturing is all make container internal gas pressure reduce by exhaust body device 5 to pump drainage gas outside container, thus reduction boiling point reaches the evaporation of ultralow boiling point, all can produce steam in a large number in the process of evaporation.Namely again steam is become water by existing technology is exactly that system is purified waste water or desalination water.In the process of desalination water processed, also by the container condensed steam as described Fig. 1 and Fig. 2 Fig. 4 etc. at work, steam can be drained into container 1 ambient dynamic or is incorporated into flowing in the pipe 6 shown in Fig. 2, thus make vapor condensation finally become water when needing.Certainly described in this as condensed steam can be used in the various forms of container works such as Fig. 7.
Pond 16 shown in Fig. 9, above-mentioned by the feedwater of Exposure to Sunlight in pond heating, also can be that Heat artificially becomes boiler by pond when needing, with burning coal or other combustiblematerials be water heating, evaporate for container for evaporation or provide heat to carry out evaporation work for device as shown in Figure 7, also can by prior art as heliotechnics equipment, the principles such as solar water heater carry out heating water, the mode of this artificial heating water is generally can use when water temperature is too low in the winter time, during heating not will water temperature add too high, as long as water temperature water more than 0 degree can not freeze and just can enter container work theoretically, but we also can had better heat slightly in terribly cold winter, make temperature can not too low time enter container carry out evaporating such effect can be better.Vaporizer location in figure can be the container for evaporation shown in Fig. 1 Fig. 2 Fig. 3 Fig. 4 Fig. 7 Figure 10 Figure 11 Figure 12 etc., the water after intensification can to enter in container also can the such as container surroundings shown in Fig. 1 Fig. 2 around or in pipe 6 for container for evaporation provides heat.Can certainly be air for container provides heat.Can heat up through Exposure to Sunlight in pond 16 at the water shown in Fig. 9, flow to container and evaporate after intensification, the water of flow container is that the water of low temperature can flow to again pond 16 and heats up.Also two ponds 16 i.e. current direction container in a pond can be prepared, another pond 16 of the current direction of the low temperature flowed out from container, so just cold water and warm water can be separated the more favourable water temperature in pond that makes can not reduce, after water sky in this pond 16, the water in another pond 16 also also will rise because of the Exposure to Sunlight water temperature of a rapid lapse of time, at this time can enter container with the water in this pond again, then heat up in the previous empty pond 16 that the water going out the low temperature of container enters again, in work, two ponds can recycle.(pond 16 in figure, can provide Exposure to Sunlight, sometimes also can become boiler, or become solar facilities, can be also namely water heating by various ways, circulating and evaporating.
Figure 10, be a kind of container of seal form, have water 4 in container, upper vessel portion has exhaust body device 5.
Figure 11, for a kind of container contents water yield is large and form that water surface space below exhaust body device is little, this form is less than the water surface space in the container in Figure 10.Utilize this form sometimes at work pump drainage gas time favourable.
Figure 12 is the form that dividing plate 51 can be had in a kind of container the water section in container to be separated, and this form also can have container water capacity large and the little feature in water surface space below exhaust body device.
Figure 13, for pond 16 is provided with the schematic diagram in greenhouse, has water 4 in its medium temperature chamber 16, this greenhouse is provided with and can covers and the greenhouse 50 of formation with transparency material, also can be provided with pump drainage gas dress to greenhouse efflux gas.Can be sealing in greenhouse, this form also can be called greenhouse container.Also can have dividing plate 51 in container, also can have one or more dividing plate in container, can certainly not have dividing plate, container also can be the container that pond is formed, and pond also can be container.
Figure 14, for container is provided with the schematic diagram in greenhouse 50, can heat for the water in pond in greenhouse, and container used also can be that transparency material is formed, and also can be other applicable thing formation or metal object formation etc.And the container that opaque material is formed also can conduct heat because the water surface in container can be connected with container, the heat transfer water in container will be given on container, if the heat of this container in greenhouse so in greenhouse will pass to the water that can be connected by container when solar radiation.Container used also can be the container that any one described in the application is applicable to, and steam can be discharged greenhouse by pipeline by the exhaust body device 5 in container.One or more container can be had in greenhouse simultaneously, container also can have one or more exhaust body device.Also can have multiple greenhouse in work, or multiple Warm rooms container matches, and also can form large-scale.
In all embodiments of the present invention, simply describe invented intention, this certainly should be wherein a more complete scheme in each device busy, such as Energy control. flow cavitation result. and water lev el control. and how the water after concentrated carries out next step crystallization later or how steam is become water etc. details here all need not carefully saying again.Everything can utilize prior art or similar techniques to combine, as a lot of parts in vacuum salt production technical equipment. structure. and principle. wait and much can combine with the present invention.The equipment of present desalination water processed can be combined with the present invention too, to learn from other's strong points to offset one's weaknesses.Also can be combined with existing refrigeration equipment in refrigeration and improve.The cardinal principle of the steam system of invention has mainly been said in this application material, can not be interpreted as that apparatus of the present invention are a simple structure as described in Figure, it also should have a lot for the treatment of of details certainly, and more multi-part, make it more perfect, simple describe do not mention can not be interpreted as that the present invention does not have.The container of seal form mainly may be used in actual applications some more, but need to consider more many factors in this special file of patent document, so the thin son that a lot of problem of present specification is write is more numerous and diverse.
Fill water 4 in visible container for evaporation 1 in sum, container is provided with exhaust body device 5, the water surface in container 1 and off-gas pump keep certain space length.When exhaust body device 5 to outside container during pump drainage gas water can not be drawn out of, the water surface in container can keep sealing, can be in vacuum environment.Container 1 can be sealing, also can be Rong Shui place, the bottom form that do not need seal this just like flowing water mouth 9, utilize exhaust body device 5 to the outer pump drainage gas of container 1, reduce air pressure and make the water 4 in container under low pressure seethe with excitement or volatilize in container 1.With this device salt manufacturing, or desalination water processed, also can freeze.Salt manufacturing is concentrated by water after explosive evaporatoin 4 exactly, and condensed water can enter salt manufacturing deep processing device again and enter salt manufacturing deep processing program in other words, finally can obtain salt body.Desalination water processed or to purify waste water be exactly say that the steam pumped out makes water by existing technology, makes sea water desaltination or makes Water warfare for people.Refrigeration is then utilize evaporation the feature of lowering the temperature to be used, make the air of container surroundings or water by absorbing and cooling temperature with air or water at container for evaporation ambient dynamic in several containers as shown in Fig. 1 Fig. 2 Fig. 3 Fig. 4 Fig. 7 etc., the air or water that reduce temperature are used to reach the object of refrigeration.As Fig. 7 Fig. 3 Fig. 4 also can utilize the water extraction flowed out from container for refrigeration, also can be sent to temperature lowering water or air and use at a distance.
All need for evaporation provides heat energy in the evaporative process of this device, the heat energy needed for evaporation can with artificially consuming energy as coal combustion or other combustiblematerials, or the means such as power consumption provide heat energy for evaporating, and sun Exposure to Sunlight also can be utilized to provide heat energy for it.Or solar facilities heating, adopt the same with desalination water processed power plant can certainly be utilized to provide heat with power plant cooperation as now conventional vacuum salt production.Preferred plan of the present invention advocates only to utilize sun Exposure to Sunlight to provide heat energy for evaporating.Generally the most of regional average temperature of seawater can reach tens degree to more than 30 degree, and the water temperature of seawater is from the several years to more than 30 degree can seethe with excitement under vacuum conditions (or volatilizations).And the effect that water evaporates in boiling is best, also can make simultaneously the water fast cooling in container and cooling-down effect also best, this device can salt manufacturing thus, desalination water processed, the multiple uses such as refrigeration.
Said need utilize sun Exposure to Sunlight to provide heat energy for evaporation, mainly say that only need enter container with the water drainage after positive Exposure to Sunlight heats up carries out vacuum-evaporation.Water in the process of evaporation in container can be lowered the temperature and at this moment the water reducing temperature be drained container, and the water simultaneously heated up through Exposure to Sunlight flows to again container evaporation.Water is entering container and the process that goes out container can be carried out simultaneously, and whole process of its evaporation does not need to provide the heat beyond Exposure to Sunlight to evaporation again.
If generally all can want that entering container with the water of 20 to 30 degree left and right evaporates, the heat energy provided beyond Exposure to Sunlight is not provided again, how can keep normal evaporation, if the water so at the beginning in container can because self also have the water temperature of 20 or 30 degree so can also there be the evaporation of a bit of time, but the time very shortly can will have been grown and can not normally will carry out having evaporated because the water temperature in container is too low the time, all need by artificial power consumption in the work such as the vacuum salt production below also why commonly used now just or evaporation desalination water processed, as burnt coal or other combustiblematerials, even the method such as power consumption provides the reason of heat for evaporation.And also result in a large amount of environmental pollutions Just because of this, according to social demand now, also having a large amount of system desalination water factories or the appearance of similar producer from now on, serious problem of environmental pollution may be caused therefrom, nowadays having caused the great attention of many international expert.
In order to solve the deficiencies in the prior art, the evaporation that the present invention proposes only need provide evaporation heat energy with Exposure to Sunlight, utilizes the water that can flow in container during evaporation to provide heat to get rid of low temperature for evaporating simultaneously.Not only the water after Exposure to Sunlight heats up enters water simultaneously by evaporative cooling of container evaporation but also amount discharge container so circulates, it is temperature-resistant that water as can be seen here in the process of evaporation in container can remain into during water, intake as container for evaporation provides heat energy endlessly endlessly, water in such container just can remain on always and not stop boiling on boiling point during water, and evaporation boiling institute's heat requirement (as long as water has the water temperature in several years to work) is unlimited from container energy now known described in Fig. 8 Fig. 9 to regulate flooding quantity and speed to determine.Sun Exposure to Sunlight is utilized to provide heat energy to be free clean infinite energy source for evaporating.Apparatus of the present invention can also combine with prior art at work, also can with prior art mutually by or cooperation, in the hope of learning from other's strong points to offset one's weaknesses.In container 1, also can stick plastic film or analogue, plastic film can also be taken off when container inner wall residue is too many like this and stick new again.In the work of the most applicable salt manufacturing of this method.Apparatus of the present invention are that salt manufacturing or desalination water processed all need to pump out steam to greatest extent, and circulate because evaporation of the present invention can only need utilize the water after Exposure to Sunlight heats up to enter container, so the method for expansion evaporation area can be utilized thus greatly improve productivity effect and evaporation effect, this point is seen also be the disadvantage changing prior art.Vacuum salt production as prior art is just not suitable for improving productivity effect in this way.Apparatus of the present invention are that salt manufacturing or desalination water processed or refrigeration all have the place more superior with prior art.If with apparatus of the present invention refrigeration so its refrigeration be very good, everybody knows when boiling water, the water boiling in pot, temperature can keep always 100 degree constant, and the flame being close to pot can be the temperature of the thousands of degree of hundreds of.Water as can be seen here in pot can by thousands of for hundreds of even higher temperature instantaneously dissolving by boiling, so water in pot always 100 degree temperature-resistant.If same principle apparatus of the present invention refrigeration, the water (in other words refrigerant) so in container equally can because of boiling by water temperature instantaneously dissolving even higher for thousands of for hundreds of degree.By finding out that utilizing apparatus of the present invention to freeze has good cooling-down effect above, if be used for freezing to huge numbers of families by tuber drainage by the water 4 of 1 li, container, or to enjoy the cool in summer will be good technical scheme.Such as utilize working routine U-shaped pipe evaporator 1 described in Fig. 7 wherein water that flows out of flowing water mouth A10, be transported to many user places, also can utilize as now conventional steam heating, by the equipment that winter heats to user with hot water, can be used for for cold water to summer is enjoy the cool summer, or other industrial refrigeration purposes.Principle of work as described in Figure 7, water 4 flow container in container turns around finally to flow to again in container and repeatedly circulates, the water flowed out in water export 10 then can be transported to many users for refrigeration by refrigeration equipment, equipment used can be identical with used steam heating, can provide refrigeration by changing cold water in former caliduct to user.The water of flow container 1 to provide after cooling water also can raised temperature through each user place, and the water of raised temperature can flow back to container 1 again by evaporative cooling, water also can circulate and ensure that normally carrying out of work a lot of user locates circulation while in container 1 like this.In working process, one end of a water channel or pipeline connects water export 10, or the water that flowed out by 1 li, container of water flowed out passes through each user of this root pipeline flow-direction (power also can by the strength of lift pump), not only pipeline is connected with each user this root pipeline last but also get back to container 1 place and be connected with the flowing water mouth 9 of container 1, or enters the aqueous phase company of container.The water flowed back to is transported to again 1 li, container to carry out circulating in sweat cooling work carrying out like this.This refrigeration plant also can be provided with power-supply controller of electric, grasps the vacuum tightness of 1 li, container, thus can play the object controlling temperature required height by controlling size of current.Said is above be transported to by the water flowed out in container to freeze everywhere, can certainly be being transported to many user places with the water being reduced temperature by container or refrigerant flowed through around container 1 or air refrigeration is provided as described in Fig. 1 Fig. 2 Fig. 3 Fig. 4, method of work can with above-mentioned just the same, namely also can by Cemented filling to each user and then get back to container surroundings cooling and recycle equally.
Of the present invention so the electricity size of the device 5 of pump drainage gas can be controlled in container 1 thus reach the speed of evaporation, the object regulating temperature height or boiling point height also can be played.Mainly only want in the present invention to be described the important principle of this invention and to protect; sum up the cardinal principle of this invention; namely exactly container 1 is improved to the container that the not closing form of intake-outlet is left in bottom; in the working process of evaporating or seethe with excitement; the water of outside can flow to container, same flow container again.The above such form has a lot of benefit, as can be that water in container for evaporation has endless, also facilitate into water, can also by can flow in container and the water flowed out for evaporation additional heat, the water reducing temperature can be got rid of outside container again simultaneously, thus make can remain in container the good effect that in evaporative process, in container, temperature can not reduce.Here it is important inventive point of the present invention.If certainly utilize this scheme of the invention, in this device or in allied equipment, multiple change can also be made, as device or the exhaust body device 5 of said pump drainage gas, only be used in the present invention illustrate that this container for evaporation needs to reduce the air pressure in container in evaporative process, can to the device of pump drainage gas outside container so need one, and this device can be vacuum pump 5, this positive empty pump 5 just can not be interpreted as that the present inventor only refers to the device this device can only being used vacuum pump by name here, be construed as in container of the present invention and need to reduce air pressure.Because be only the real meaning of the present inventor like this, it is also the real meaning of expressing in claim.As everybody knows in similar prior art also just like sliding vane rotary vacuum pump group, water ring topping-up pump group, hydro-steam ejector pump group, hydrojet vacuum unit, vapor jet vacuum device, for vacuum salt production novel high vacuum combination technique, bittern spray etc., do with apparatus of the present invention as seen a little combine or change not so difficult in prior art.This device also can carry out combining or improving with similar techniques, so need step-down when the container said of the present inventor has its meaning of lift pump can only be and say and work in container, certainly specifically using which type of dropping equipment, is diversified.Can not say it can only is with off-gas pump (can certainly be off-gas pump).In evaporation work described in the present invention, water can flow to container by simultaneously flow container again after evaporative cooling, and when only can not be interpreted as separately the just evaporation work that contriver says here, water flows in container and flows out again simultaneously.Be construed as contrive equipment at work, water can be utilized to flow to container and evaporate institute's heat requirement for evaporation provides, can absorb heat in a large number when evaporating in container or seething with excitement and cause temperature reduction in container, what will affect evaporation work like this enters work.And the present invention propose at this moment can by outside the low temperature amount discharge container in container, its method can utilize in container, reduced the water amount discharge container of water temperature in evaporative process thus make the temperature in container can not be too low.Again can only flow container simultaneously from seeing the meaning of contriver does not say that water can only flow to after container above.Be construed as and real be meant to water in evaporative process and flow to container and can supplement heat needed for evaporation for container, also can utilize water that the low temperature in container is got rid of container.Visible contriver just hopes that protecting apparatus of the present invention water in evaporation or boiling work can flow to container in the claims supplements institute's heat requirement; simultaneously again can by the low temperature amount discharge container in container, and can not be interpreted as that the said water of the present invention can only flow to after container at work can only flow container simultaneously.Illustrate, also the mode sprayed by water is had in similar prior art, thus volatilization can be accelerated, if in device busy of the present invention, after water flows to container, in container, there is water bottom and water surface top also has living space, as being provided with water jet device thus can making jet of water out in this space, so just more easily volatilizing this device also can be like this.Can find out that from this example the present inventor will say that apparatus of the present invention can only to flow to after container simultaneously flow container again by water at work, but to express apparatus of the present invention evaporation or boiling process in can by flow in container water for evaporation heat is provided, can utilize again water that low temperature is got rid of container, make in container, to keep temperature to reduce.Also can some which type of process or variation in container as water, the present inventor does not say, but and is not equal to the water entered in container and just can not has other form process.Water owing to entering container in this device can become steam and discharge a part, remaining water flow container, also can become and is all evaporated by the water entering container, so just only enter the water of container and do not go out the water of container if certainly regulate flooding quantity and flow velocity.Visible form can be various, can not singlely understand.
In life, the work of similar apparatus of the present invention also has much, as used vacuum salt production technology, lot of advantages also can be used combination, in existing salt making technology, also have and adopt steam band water ring vacuum pump that the non-condensable gas produced in evaporation unit is discharged system to maintain the vacuum tightness of system, hydrojet vacuum unit, can have in the work of vapor jet vacuum device etc. the present inventor in all similar prior aries and also can, can improve, also can be in conjunction with.The seawater that apparatus of the present invention concentrate out can enter in used vacuum process sequence, and the steam evaporated also can enter in the working routine of now conventional desalination water processed and finally become desalination water.Reduced the water of temperature by evaporation or air can enter in now conventional refrigeration equipment program, or in device program for heating installation, enter many users for refrigeration by cold water or the existing conventional caliduct of cold air input.Certainly can also extract multiple useful matter in seawater after being concentrated by this device, only say salt manufacturing in this application, certainly neither say and can only use condensed water salt manufacturing.
In this device, the steam be evaporated, also can as conventional air-conditioning, and the feature can generated heat when utilizing steam to become liquid, provides and heat, and heating water or air can send into many users, or be the water in this apparatus container or the water extraction heat supplied outside container.
The water that water export 10 flows out, in order to save the use energy of lift pump, can also be introduced in the bowl-shaped ring border compared with low level by the present invention, raises basin position again, make water automatically can flow into container again after basin is full by methods such as similar screw block.
The said artificial power consumption heating water of this device, can be that after Heating pool 16, circulation flows into container again, also can be direct heating container for evaporation 1.
Apparatus of the present invention are utilized not only can greatly to increase work efficiency, and energy-conserving and environment-protective, greatly reduce production cost, as a large amount of land areas can also be saved in the work of salt manufacturing.

Claims (10)

1. vacuum salt production and a vapo(u)rization system of purifying waste water, comprise container, it is characterized in that: fill water in described container, described container outlet is provided with exhaust body device, and the horizontal plane container outlet in described container has certain space; Also comprising to heat up naturally maybe can accept the water that Exposure to Sunlight heats up, and this water is that water extraction in container is for evaporation institute heat requirement.
2. vacuum salt production and the vapo(u)rization system of purifying waste water according to claim 1, the water capacity of described container is more than 1 ton, or more than 2 tons, or more than 3 tons, or more than 4 tons, or more than 5 tons, or more than 7 tons, or more than 10 tons, or more than 15 tons, or more than 20 tons, or more than 25 tons, or more than 30 tons, or more than 35 tons, or more than 40 tons, its water capacity tonnage is respectively more than following data, and namely 45,50,55,60,70,80,90,100,200,300,400,500,600,700,800,900, or more than 1000 tons; The water surface area that water surface area in other words in container maybe can accept Exposure to Sunlight is more than 5 square metres or more than 8 square metres, or more than 10 square metres, or more than 13 square metres, the water surface area that the water surface area in its container maybe can accept Exposure to Sunlight can be respectively following data square metre more than 15,18,20,25,30,35,40,45,50,55,60,65,70,75,80,85,90,95, or more than 100 square metres.
3. vacuum salt production and the vapo(u)rization system of purifying waste water according to claim 1, is characterized in that: describedly naturally can heat up that maybe to accept water that Exposure to Sunlight heats up be can the water of natural flow, and this water is that water extraction in container is for evaporation institute's heat requirement or water source.
4. vacuum salt production and the vapo(u)rization system of purifying waste water according to claim 1, is characterized in that: described naturally heating up maybe can accept the water that Exposure to Sunlight heats up and form reciprocal water cycle with the water in container, or Exposure to Sunlight circulates.
5. vacuum salt production and the vapo(u)rization system of purifying waste water according to claim 1 or 4, is characterized in that: described can naturally intensification maybe can accept water level that Exposure to Sunlight heats up in pond.
6. vacuum salt production and the vapo(u)rization system of purifying waste water according to claim 5, is characterized in that: described naturally heating up maybe can accept water level that Exposure to Sunlight heats up in pond, is provided with container in described pond; Can naturally heat up in other words maybe can accept the water level of Exposure to Sunlight intensification in pond, container is provided with in described pond, in container by the water that evaporation reduces temperature accept in pond again Exposure to Sunlight heat up or and intensification naturally, formed in work water circulate in pond nature heat up or Exposure to Sunlight heat up, circulating and evaporating again.
7. according to claim 1, or 3, or 4, or 5, or 6, described vacuum salt production and the vapo(u)rization system of purifying waste water, it is characterized in that, described naturally heat up or Exposure to Sunlight to heat up be based on intensification naturally heated up or Exposure to Sunlight heats up, described naturally to heat up or the intensification of Exposure to Sunlight, be say that container has at least half or heat over half or temperature to derive from nature intensification or Exposure to Sunlight intensification when evaporation in evaporation institute's heat requirement used or temperature.
8. according to claim 1, or 3, or 4, or 5, or 6, or 7 arbitrary described vacuum salt productions and the vapo(u)rization system of purifying waste water, it is characterized in that: described naturally heating up maybe can accept the water that Exposure to Sunlight heats up, wherein said Exposure to Sunlight heats up and comprises nature Exposure to Sunlight intensification and solar facilities Exposure to Sunlight intensification, and solar facilities heats up and comprises again the intensification of solar energy greenhouse equipment; The water heating system that salt manufacturing in other words or system are purified waste water, comprising water is wherein that water used is heated with solar energy greenhouse.
9. according to claim 1, or 2 or 3, or 4, or 6, or 7 arbitrary described vacuum salt production and the vapo(u)rization system of purifying waste water, it is characterized in that: described container is sealed vessel or blow-by container, described blow-by container comprises U-shaped pipe container for evaporation, the water of its packing less container in the work vacuumized in container can be divided into flowing or immobilising form, the steam that exhaust body device on its container is extracted out can enter purified water recovering apparatus, or it can be entered salt manufacturing deep processing equipment again by the condensed water after container evaporation concentration.
10. a vacuum-evaporation refrigeration system, comprises container, it is characterized in that: fill water in described container, and described container outlet is provided with exhaust body device, and the horizontal plane container outlet in described container has certain space; Also comprise the water outside container or air, after the water in the water outside described container or air or container is reduced temperature by container or refrigerant, be connected with many users by pipeline, refrigeration is provided; Vacuum salt production and the vapo(u)rization system of purifying waste water or a refrigeration system in other words, comprise container, it is characterized in that: fill water in described container, described container outlet is provided with exhaust body device, and the horizontal plane container outlet in described container has certain space; Also comprise the water outside container, it is less than 0 degree or 0 degree that the temperature of the water outside described container or the water in container can be reduced to, and is provided with to get ice and arrange or get ice port and ice can be taken away in container or system, or transports to and need use with the place of ice.
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