CN102923802A - Sea water desalting plant with fixed bar mirror combination for linear solar condensation, and desalting method thereof - Google Patents

Sea water desalting plant with fixed bar mirror combination for linear solar condensation, and desalting method thereof Download PDF

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CN102923802A
CN102923802A CN201210485388XA CN201210485388A CN102923802A CN 102923802 A CN102923802 A CN 102923802A CN 201210485388X A CN201210485388X A CN 201210485388XA CN 201210485388 A CN201210485388 A CN 201210485388A CN 102923802 A CN102923802 A CN 102923802A
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steam
seawater
bar shaped
water
minute surface
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CN102923802B (en
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马春元
周希正
李洪梅
王军旗
陈芳
宋广峰
刘正刚
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Guoneng Shandong Energy Environment Co ltd
Shandong University
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Shandong Shandong University Energy Environment Co ltd
Shandong University
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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
    • Y02A20/131Reverse-osmosis
    • 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
    • Y02A20/141Wind power
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/40Solar thermal energy, e.g. solar towers

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Abstract

The invention discloses a sea water desalting plant with a fixed bar mirror combination for linear solar condensation, and a desalting method thereof. According to the device, mixed bar reflection mirrors are applied to condensation and heat collection to generate liquid or steam at middle and high temperatures, a piston in a gas-liquid combined cylinder is used for directly driving and boosting the liquid or the steam which then enters into a reverse osmosis desalination device, exhaust steam is applied to sea water desalination again by a distillation method, and condensate water is circulated to a solar condensation collector to form semi-closed circulation. According to the sea water desalting plant, as the reflector is fixed, and an absorber is tracked, so that a tracking system is simplified, the energy consumption is reduced, and the system utilization efficiency is improved; and furthermore, sea water desalination by reverse osmosis is driven by high pressure obtained from acting with direct expansion, the exhaust steam is recycled, and energy levels are utilized in echelon and coupling manners, so that the efficiency of available energy is improved. The sea water desalting plant can be used for automatically adjusting pressure and steam temperature required by brackish water and sea water with different concentrations, and has great superiorities when being applied to desalination of the brackish water and the sea water in regions with high wind power along the coast and in a desert land.

Description

Fixedly bar shaped minute surface sun energy line optically focused makes up sea water desalinating plant and desalination method
Technical field
The invention belongs to energy technology field, particularly a kind of fixedly bar shaped minute surface sun energy line optically focused combination sea water desalinating plant and desalination method.
Background technology
Along with the development of society, industry, agricultural production industry and domestic life centering temperature demand increasing.Our times energy structure situation is more and more severeer, faces unprecedented challenge, and climate change becomes clear day by day, and environmental pollution is serious all the more, and energy-saving and emission-reduction are very urgent, is badly in need of development new forms of energy and more Freshwater resources.
The fundamental research in desalination with Solar Energy field concentrates on:
1. naturally change the passive type desalination water method that drives by sun power and envrionment conditions fully, such as traditional solar distilling pond, multiple-effect solar still etc.;
2. active desalination water method prepares fresh water and needs a small amount of power consumption, also requires to be equipped with simultaneously the extra means such as blower fan, water pump, and the heat and mass transfer enhancement effect improves system performance;
3. realize energy cascade utilization, the composite system of above-mentioned technology and other correlation technique integrated application etc. as combining with solar energy greenhouse, combine with the techniques such as distillation and flash method of calming the anger etc.
Active method for desalting seawater is owing to having improved the heat and mass effect of desalting equipment, and vaporization temperature and condensing temperature can separately be regulated and control, and extremely payes attention to.Energy in the desalting process, moisture, salinity reclaim, heat and mass transfer process is strengthened, fouling characteristic in the parts, the raising of efficiency of energy utilization and producing water ratio etc. is the emphasis of research, it mainly is the solar energy collector of middle low-temperature level that solar energy converting is utilized link, the equipment combination relevant with the techniques such as distillation, flash distillation, pressure steam distillation and various heat and mass transfer process.
China lacks systematicness and scale effect generally in the solar seawater desalination field, and major technique and process aspect research are not deep enough, particularly with world level larger gap is being arranged aspect the performance index of some representative device.Conversion realizes that desalting process is still research emphasis based on solar energy, and many links such as energy recovery, salinity recovery and moisture recovery remain further to be optimized, and manufacturing process etc. are needed further raising badly.
Summary of the invention
The objective of the invention is is providing middle high temperature to carry out application aspect seawater (brackish water) desalination in order to solve sun power, reduction system cost of manufacture, improve the utilising efficiency of the energy and the economy of system, a kind of fixedly bar shaped minute surface sun energy line optically focused combination sea water desalinating plant and desalination method are proposed, adopt fixedly bar shaped mirror surface light and heat collection, high-temp liquid or steam in the generation, adopt and enter reverse osmosis desalination device after piston directly drives supercharging in the gas-liquid combination cylinder, exhaust vapour is sharp distillation sea water desalting again, condensate water circulatory forms the semi-closure circulation device to solar concentrating collector.This device has mirror surface to be fixed, and resorber is followed the tracks of the light and heat collection system heating steam of the sun, directly drives seawater and carries out reverse osmosis seawater desalting, and its latent heat utilizes the advantage of carrying out distillation seawater desalination again; And this device is made simple, with low cost.Particularly in the larger coastland of wind-force, such as high temperature seawater desalination integrated utilization in the Salar light-gathering in the marine industrial platform construction, fixedly the bar shaped specular-reflection unit directly produces the pressure-driven reverse osmosis seawater desalting than other beam condensing unit, gas drive liquid pressurized cylinder, and the solar energy sea water desalination apparatus that latent heat utilizes again has more advantage than other devices.
The objective of the invention is to be achieved through the following technical solutions:
A kind of fixedly bar shaped minute surface sun energy line optically focused (ED+RO) combination sea water desalinating plant comprises that fixed bar shaped minute surface reflecting and condensing device, at least two steam driven seawater supercharging devices, steam coagulate device of air, suction distillation seawater desalinating device, reverse osmosis desalination device; Described fixed bar shaped minute surface reflecting and condensing device connects at least two steam driven seawater supercharging devices, the solidifying device of air of steam and suction distillation seawater desalinating device by pipeline; Described steam driven seawater supercharging device connects reverse osmosis desalination device; The solidifying device of air of described steam is connected by the resorber of pipeline with fixed bar shaped minute surface reflecting and condensing device.
Described fixed bar shaped minute surface reflecting and condensing device comprises several bar shaped specular reflective mirrors, resorber, support, inner cased type expansion link, bearing, rotational equilibrium thing and circular arc adjustment plate; Described several bar shaped specular reflective mirrors are placed side by side, the two ends of bar shaped specular reflective mirrors all are fixed to two circular arcs and adjust on the plate, the upper end that described each circular arc is adjusted the circular arc outside of plate is connected on the bearing of base by the inner cased type expansion link, the lower end that described each circular arc is adjusted the circular arc outside of plate is fixed on the support of base, the circular arc inside that described each circular arc is adjusted plate is fixed in the circular arc a bit by three supports, any is as fulcrum in each circular arc, each fulcrum is provided with a rock arm, one end of each rock arm is provided with the rotational equilibrium thing that slides along bar, connect by a support between two end points of circular arc of described each circular arc adjustment plate, the two ends of described resorber are fixed on the end points of two bars.
Described steam driven seawater supercharging device comprises pneumatic cylinder, cooling room and the hydro-cylinder that connects successively, be provided with the gas drive piston in the described pneumatic cylinder, be provided with hydraulic efficiency piston in the described hydro-cylinder, connect by piston rod between described gas drive piston and the hydraulic efficiency piston, described piston rod passes cooling room, and described pneumatic cylinder one end is provided with breather cheek valve and one-way exhaust valve, and an end of described hydro-cylinder is provided with water intaking valve, described cooling room is connected with water intaking valve by pipeline, and described pneumatic cylinder also is provided with ventage.
The solidifying device of air of described steam comprises evaporator room and solidifying air chamber, connects by hot tube heat exchanger between described evaporator room and the solidifying air chamber, and solidifying air chamber below is connected with check valve by pipeline; Described evaporator room top is provided with nozzle, and the nozzle top is connected with injector.
Described suction distillation seawater desalinating device comprises interconnective condensing chamber and solidifying air chamber, and the condensing chamber top is connected with injector,
The connecting tube of described fixed bar shaped minute surface reflecting and condensing device and two steam driven seawater supercharging devices is provided with relief valve and weather gage; Described relief valve and weather gage are used for regulating inlet steam and press;
The solidifying device of air of described steam is provided with check valve, fresh-water tank and the water circulating pump that is connected successively with the connecting tube of the resorber of fixed bar shaped minute surface reflecting and condensing device.
The connecting tube of described steam driven seawater supercharging device and reverse osmosis desalination device is provided with hydraulicefficiency pressure gauge.
All control valves all adopt battery valve and Access Control circuit.
The quantity of described hot tube heat exchanger is determined according to heat.
Below the described solidifying air chamber water discharge valve is housed.
All be provided with thermal insulation layer in the middle of described gas drive piston and the hydraulic efficiency piston.
The desalination method that above-mentioned fixedly bar shaped minute surface sun energy line optically focused combination sea water desalinating plant adopts, the specific works step is:
Step 1: first fresh-water tank and pipeline are full of pure water and Exhaust Gas before starting, are full of seawater in two hydro-cylinders;
Step 2: to glass metal valve tube resorber, resorber is followed the tracks of sun line optically focused to the stripe-shape plane speculum of fixed bar shaped minute surface reflecting and condensing device with the sun power line reflection; Behind the resorber of pure water through sun energy line optically focused, be heated to form 110-150 ℃ of saturated wetting vapour, reach the vapor pressure about 1.43-4.76bar;
Step 3: the breather cheek valve of opening a steam driven seawater supercharging device, close one-way exhaust valve and the water intaking valve of this steam driven seawater supercharging device, steam enters the pneumatic cylinder of this steam driven seawater supercharging device, expand and do work, promote hydraulic efficiency piston by piston rod, the hydro-cylinder rate of supercharging is 36:1; When steam reaches certain pressure, Steam Actuation gas drive piston, thus promote hydraulic efficiency piston compression seawater through the intermediate piston bar, enter reverse osmosis desalination device through the seawater after the supercharging and produce fresh water and strong brine; When the hydraulic efficiency piston of steam driven seawater supercharging device moves to the cylinder body right-hand member, steam off drives the breather cheek valve of seawater supercharging device, open one-way exhaust valve and the water intaking valve of steam driven seawater supercharging device, steam enters solidifying air chamber and condenses into water through hot tube heat exchanger, forms negative pressure and makes seawater be easy to again be full of hydro-cylinder; Another steam driven seawater supercharging device was started working when hydro-cylinder was filled, and the method for work of another steam driven seawater supercharging device is consistent with the method for work of above-mentioned steam driven seawater supercharging device; Alternate cycles like this.
Step 4: the steam of discharge is condensed into water through the hot tube heat exchanger between solidifying air chamber and the evaporator room, arranges to fresh-water tank by the check valve of pipeline, and the water of fresh-water tank enters resorber by water circulating pump and again is heated into steam by optically focused; Evaporator room makes seawater obtain rapid evaporation through the heat exchange of hot tube heat exchanger, spray and the injector suction of nozzle simultaneously, and secondary steam enters condensing chamber and is condensed into the fresh water discharge; Cooling room obtains pre-hot sea water by the warm air cooling to gas drive piston the right in piston rod and the pneumatic cylinder.
Described hot tube heat exchanger produces negative pressure to the steam of discharging in solidifying air chamber condensation, and seawater automatically refills hydraulic cylinder body, flashes to secondary steam in the heat absorption of evaporator room seawater.
Described injector produces vacuum tightness to the evaporator room gas injection, accelerates evaporation; The injector injection forms saturated low-pressure steam, enters cooling room through seawater condensing, produces fresh water and discharges, and seawater preheating enters evaporator room.
The present invention contrasts prior art and has following innovative point:
1, Salar light-gathering makes and adopts fixed bar shaped mirror reflection spotlight, follows the tracks of resorber, and cost performance is good, stable performance;
2, direct heating vapor expansion driven plunger seawater is pressurized to the required reverse osmosis pressure of reverse osmosis desalination device, slowly promotes, and then reaches running balance, and efficiency of conversion is higher;
When 3, expanding into the cylinder body right-hand member, steam is discharged condensation and is produced negative pressure, makes seawater need not pump and just can refill the liquid pressurized cylinder;
4, adopt sprayer pumps to produce vacuum tightness and accelerate the evaporator room evaporation of seawater, improved rate of evaporation and producing water ratio, whole system does not have power set, all is to adopt steam driven.
The present invention contrasts prior art and has following remarkable advantage:
1, adopts fixed bar shaped specular reflective mirrors line optically focused, the angle of inclination can be adjusted twice in 1 year, the same day adjusted by angle (angle of latitude+11.75) by angle (angle of latitude-11.75) and the Autumnal Equinox Spring Equinox, be divided into summer and use in winter, optically focused ratio and optical property have been improved, obtain more solar irradiation, and adopt heat collector to maintain static the tracking resorber, tracking system is simplified and reduces energy consumption;
2, adopt Salar light-gathering to be heated into steam and directly drive the liquid supercharging, enter reverse osmosis desalination device and produce fresh water, process is the water heat temperature raising, and the supercharging of saturation water heat absorption vaporized expanding drives, and is adiabatic expansion acting process.Do not have the several times conversion of energy, energy consumption is lower, than steam-electric power and employing Lang Ken circular work, drives high pressure pump drive reverse osmosis seawater desalting efficient again and wants high;
3, this device only needs simple gas drive cylinder, liquid pressurized cylinder, injector and heat-exchanger rig just can provide stable pressure to reverse osmosis, heat is provided and produces vacuum tightness to distillation seawater desalination.System does not have other power set, and cost is lower, stable, safety economy;
4, the specific yield and the energy consumption that need by reference and other various sea water desaltinations of analysis contrast, this research device has good water production rate and required low-down energy consumption, need not change and just can be applicable to different salinity solubility seawater and brackish water, especially brackish water is had higher water production rate.Be that a kind of good sea water desaltination is selected in remote districts (desert and island), have good economic benefit and environmental benefit.
Description of drawings
Fig. 1 is Salar light-gathering combined type sea water desalination system structure iron;
Fig. 2 is fixed bar shaped minute surface reflecting and condensing device schematic diagram of the present invention;
Fig. 3 is steam driven seawater supercharging device schematic diagram of the present invention;
Wherein: 1, the stripe-shape plane speculum, 2, resorber, 3, the first gas drive piston, 4, the first hydraulic efficiency piston, 5, evaporator room, 6, solidifying air chamber, 7, hot tube heat exchanger, 8, reverse osmosis desalination device, 9, the first breather cheek valve, 10, the first one-way exhaust valve, 11, the second breather cheek valve, 12, the second one-way exhaust valve, 13, the first water intaking valve, 14, the second water intaking valve, 15, the first piston bar, 16, condensing chamber, 17, injector, 18, nozzle, 19, relief valve, 20, weather gage, 21, hydraulicefficiency pressure gauge, 22, water circulating pump, 23, fresh-water tank, 24, check valve, 25, the first ventage, 26, the first pneumatic cylinder, 27, the first hydro-cylinder, 28, the second piston rod, 29, cooling room, 30, the second ventage, 31, the second gas drive piston, 32, the second hydraulic efficiency piston, 33, support, 34, the inner cased type expansion link, 35, bearing, 36, the rotational equilibrium thing, 37, circular arc is adjusted plate, 38, the second pneumatic cylinder, 39, the second hydro-cylinder.
Embodiment
The invention will be further described below in conjunction with accompanying drawing and embodiment.
Basic thought of the present invention is to merge fixation reflex minute surface solar energy light gathering and heat collecting to drive the sea water desaltination that hot method combines with embrane method.
As shown in Figure 1, a kind of fixedly bar shaped minute surface sun energy line optically focused (MED+RO) combination sea water desalinating plant comprises that fixed bar shaped minute surface reflecting and condensing device, at least two steam driven seawater supercharging devices, steam coagulate device of air, suction distillation seawater desalinating device, reverse osmosis desalination device; Described fixed bar shaped minute surface reflecting and condensing device connects at least two steam driven seawater supercharging devices, the solidifying device of air of steam and suction distillation seawater desalinating device by pipeline; Described steam driven seawater supercharging device connects reverse osmosis desalination device; The solidifying device of air of described steam is connected by the resorber 2 of pipeline with fixed bar shaped minute surface reflecting and condensing device.
Described fixed bar shaped minute surface reflecting and condensing device comprises several stripe-shape plane speculums 1, resorber 2, support 33, inner cased type expansion link 34, bearing 35, rotational equilibrium thing 36 and circular arc adjustment plate 37; Described several stripe-shape plane speculums 1 are placed side by side, the two ends of stripe-shape plane speculum 1 all are fixed to two circular arcs and adjust on the plate 37, the upper end that described each circular arc is adjusted the circular arc outside of plate 37 is connected on the bearing 35 of base by inner cased type expansion link 34, the lower end that described each circular arc is adjusted the circular arc outside of plate 37 is fixed on the support 33 of base, the circular arc inside that described each circular arc is adjusted plate 37 is fixed in the circular arc a bit by three supports 33, any is as fulcrum in each circular arc, each fulcrum is provided with a rock arm, one end of each rock arm is provided with the rotational equilibrium thing 36 that slides along bar, connect by a support 33 between two end points of circular arc of described each circular arc adjustment plate 37, the two ends of described resorber 2 are fixed on the end points of two bars.
Described steam driven seawater supercharging device comprises pneumatic cylinder, cooling room 29 and the hydro-cylinder that connects successively, be provided with the gas drive piston in the described pneumatic cylinder, be provided with hydraulic efficiency piston in the described hydro-cylinder, connect by piston rod between described gas drive piston and the hydraulic efficiency piston, described piston rod passes cooling room 29, described pneumatic cylinder one end is provided with breather cheek valve and one-way exhaust valve, one end of described hydro-cylinder is provided with water intaking valve, described cooling room 29 is connected with water intaking valve by pipeline, and described pneumatic cylinder also is provided with ventage.
The solidifying device of air of described steam comprises evaporator room 5 and solidifying air chamber 6, connects by hot tube heat exchanger 7 between described evaporator room 5 and the solidifying air chamber 6, and solidifying air chamber 6 belows are connected with check valve 24 by pipeline; Described evaporator room 5 tops are provided with nozzle 18, and nozzle 18 tops are connected with injector 17.
Described suction distillation seawater desalinating device comprises interconnective condensing chamber 16 and solidifying air chamber 6, and condensing chamber 16 tops are connected with injector 17,
Described fixed bar shaped minute surface reflecting and condensing device is provided with relief valve 19 and weather gage 20 with the connecting tube of at least two steam driven seawater supercharging devices; Described relief valve 19 and weather gage 20 are used for regulating inlet steam and press;
The solidifying device of air of described steam is provided with check valve 24, fresh-water tank 23 and the water circulating pump 22 that is connected successively with the connecting tube of the resorber 2 of fixed bar shaped minute surface reflecting and condensing device.
The connecting tube of described steam driven seawater supercharging device and reverse osmosis desalination device is provided with hydraulicefficiency pressure gauge 21.
All control valves all adopt battery valve and Access Control circuit.
The quantity of described hot tube heat exchanger 7 is determined according to heat.
Below the described solidifying air chamber 6 water discharge valve is housed.
All be provided with thermal insulation layer in the middle of described gas drive piston and the hydraulic efficiency piston.
The desalination method that above-mentioned fixedly bar shaped minute surface sun energy line optically focused combination sea water desalinating plant adopts, the specific works step is:
Step 1: first fresh-water tank 23 and pipeline are full of pure water and Exhaust Gas before starting, are full of seawater in two hydro-cylinders;
Step 2: to glass metal valve tube resorber 2, resorber 2 is followed the tracks of sun line optically focused to the stripe-shape plane speculum 1 of fixed bar shaped minute surface reflecting and condensing device with the sun power line reflection; Behind the resorber 2 of pure water through sun energy line optically focused, be heated to form 110-150 ℃ of saturated wetting vapour, reach the vapor pressure about 1.43-4.76bar;
Step 3: the first breather cheek valve 9 of opening the first steam driven seawater supercharging device, close the first one-way exhaust valve 10 and first water intaking valve 13 of the first steam driven seawater supercharging device, steam enters the first pneumatic cylinder 26 of the first steam driven seawater supercharging device, expand and do work, promote the first hydraulic efficiency piston 4 by first piston bar 15, the hydro-cylinder rate of supercharging is 36:1; When steam reaches certain pressure, Steam Actuation the first gas drive piston 3, thus promote the first hydraulic efficiency piston 4 compression seawater through first piston bar 15, enter reverse osmosis desalination device 8 through the seawater after the supercharging and produce fresh water and strong brine; When the first hydraulic efficiency piston 4 of steam driven seawater supercharging device moves to the cylinder body right-hand member, steam off drives the first breather cheek valve 9 of seawater supercharging device, open the first one-way exhaust valve 10 and first water intaking valve 13 of steam driven seawater supercharging device, steam enters solidifying air chamber 6 and condenses into water through hot tube heat exchanger 7, forms negative pressure and makes seawater be easy to again be full of hydro-cylinder; The second steam driven seawater supercharging device was started working when hydro-cylinder was filled, open the second breather cheek valve 11 of the second steam driven seawater supercharging device, close the second one-way exhaust valve 12 and second water intaking valve 14 of the second steam driven seawater supercharging device, steam enters the second pneumatic cylinder 38 of the second steam driven seawater supercharging device, expand and do work, promote the second hydraulic efficiency piston 32 by the second piston rod 28, the hydro-cylinder rate of supercharging is 36:1; When steam reaches certain pressure, Steam Actuation the second gas drive piston 31, thus promote the second hydraulic efficiency piston 32 compression seawater through the second piston rod 28, enter reverse osmosis desalination device 8 through the seawater after the supercharging and produce fresh water and strong brine; When the second hydraulic efficiency piston 32 of steam driven seawater supercharging device moves to the cylinder body right-hand member, steam off drives the second breather cheek valve 11 of seawater supercharging device, open the second one-way exhaust valve 12 and second water intaking valve 14 of steam driven seawater supercharging device, steam enters solidifying air chamber 6 and condenses into water through hot tube heat exchanger 7, forms negative pressure and makes seawater be easy to again be full of hydro-cylinder; The method of work of the second steam driven seawater supercharging device is consistent with the method for work of the first steam driven seawater supercharging device; Alternate cycles like this.
Step 4: the steam of discharge is condensed into water through the hot tube heat exchanger 7 between solidifying air chamber 6 and the evaporator room 5, arranges to fresh-water tank 23 by the check valve 24 of pipeline, and the water of fresh-water tank 23 enters resorber 2 by water circulating pump 22 and again is heated into steam by optically focused; Evaporator room 5 makes seawater obtain rapid evaporation through the heat exchange of hot tube heat exchanger 7, spray and injector 17 suctions of nozzle 18 simultaneously, and secondary steam enters condensing chamber 16 and is condensed into the fresh water discharge; Cooling room 29 obtains pre-hot sea water by the warm air cooling to gas drive piston the right in piston rod and the pneumatic cylinder.
The steam of 7 pairs of discharges of described hot tube heat exchanger produces negative pressure in solidifying air chamber 6 condensations, and seawater automatically refills hydraulic cylinder body, flashes to secondary steam in the heat absorption of evaporator room 5 seawater.
17 pairs of evaporator room 5 gas injections of described injector produce vacuum tightness, accelerate evaporation; Injector 17 injections form saturated low-pressure steam, enter cooling room 29 through seawater condensing, produce fresh water and discharge, and seawater preheating enters evaporator room 5.
Although above-mentionedly by reference to the accompanying drawings the specific embodiment of the present invention is described; but be not limiting the scope of the invention; one of ordinary skill in the art should be understood that; on the basis of technical scheme of the present invention, those skilled in the art do not need to pay various modifications that creative work can make or distortion still in protection scope of the present invention.

Claims (10)

1. fixing bar shaped minute surface sun energy line optically focused combination sea water desalinating plant, it is characterized in that, comprise that fixed bar shaped minute surface reflecting and condensing device, at least two steam driven seawater supercharging devices, steam coagulate device of air, suction distillation seawater desalinating device, reverse osmosis desalination device; Described fixed bar shaped minute surface reflecting and condensing device connects at least two steam driven seawater supercharging devices, the solidifying device of air of steam and suction distillation seawater desalinating device by pipeline; Described steam driven seawater supercharging device connects reverse osmosis desalination device; The solidifying device of air of described steam is connected by the resorber of pipeline with fixed bar shaped minute surface reflecting and condensing device.
2. a kind of fixedly bar shaped minute surface sun energy line optically focused as claimed in claim 1 makes up sea water desalinating plant, it is characterized in that, described fixed bar shaped minute surface reflecting and condensing device comprises several bar shaped specular reflective mirrors, resorber, support, inner cased type expansion link, bearing, rotational equilibrium thing and circular arc adjustment plate; Described several bar shaped specular reflective mirrors are placed side by side, the two ends of bar shaped specular reflective mirrors all are fixed to two circular arcs and adjust on the plate, the upper end that described each circular arc is adjusted the circular arc outside of plate is connected on the bearing of base by the inner cased type expansion link, the lower end that described each circular arc is adjusted the circular arc outside of plate is fixed on the support of base, the circular arc inside that described each circular arc is adjusted plate is fixed in the circular arc a bit by three supports, any is as fulcrum in each circular arc, each fulcrum is provided with a rock arm, one end of each rock arm is provided with the rotational equilibrium thing that slides along bar, connect by a support between two end points of circular arc of described each circular arc adjustment plate, the two ends of described resorber are fixed on the end points of two bars.
3. a kind of fixedly bar shaped minute surface sun energy line optically focused as claimed in claim 1 makes up sea water desalinating plant, it is characterized in that, described steam driven seawater supercharging device comprises the pneumatic cylinder that connects successively, cooling room and hydro-cylinder, be provided with the gas drive piston in the described pneumatic cylinder, be provided with hydraulic efficiency piston in the described hydro-cylinder, connect by piston rod between described gas drive piston and the hydraulic efficiency piston, described piston rod passes cooling room, described pneumatic cylinder one end is provided with breather cheek valve and one-way exhaust valve, one end of described hydro-cylinder is provided with water intaking valve, described cooling room is connected with water intaking valve by pipeline, and described pneumatic cylinder also is provided with ventage.
4. a kind of fixedly bar shaped minute surface sun energy line optically focused as claimed in claim 1 makes up sea water desalinating plant, it is characterized in that, the solidifying device of air of described steam comprises evaporator room and solidifying air chamber, connect by hot tube heat exchanger between described evaporator room and the solidifying air chamber, solidifying air chamber below is connected with check valve by pipeline; Described evaporator room top is provided with nozzle, and the nozzle top is connected with injector.
5. a kind of fixedly bar shaped minute surface sun energy line optically focused combination sea water desalinating plant as claimed in claim 1 is characterized in that, described suction distillation seawater desalinating device comprises interconnective condensing chamber and solidifying air chamber, and the condensing chamber top is connected with injector.
6. a kind of fixedly bar shaped minute surface sun energy line optically focused as claimed in claim 1 makes up sea water desalinating plant, it is characterized in that, described fixed bar shaped minute surface reflecting and condensing device is provided with relief valve and weather gage with the connecting tube of at least two steam driven seawater supercharging devices; Described relief valve and weather gage are used for regulating inlet steam and press;
The solidifying device of air of described steam is provided with check valve, fresh-water tank and the water circulating pump that is connected successively with the connecting tube of the resorber of fixed bar shaped minute surface reflecting and condensing device.
7. a kind of fixedly bar shaped minute surface sun energy line optically focused combination sea water desalinating plant as claimed in claim 1 is characterized in that, the connecting tube of described steam driven seawater supercharging device and reverse osmosis desalination device is provided with hydraulicefficiency pressure gauge.
8. a kind of fixedly bar shaped minute surface sun energy line optically focused combination sea water desalinating plant as claimed in claim 1 is characterized in that, all control valves all adopt battery valve and Access Control circuit; The quantity of described hot tube heat exchanger is determined according to heat; Below the described solidifying air chamber water discharge valve is housed; All be provided with thermal insulation layer in the middle of described gas drive piston and the hydraulic efficiency piston.
9. the desalination method that adopts such as the arbitrary described a kind of fixedly bar shaped minute surface sun energy line optically focused combination sea water desalinating plant of claim 1-8 is characterized in that, the specific works step is:
Step 1: first fresh-water tank and pipeline are full of pure water and Exhaust Gas before starting, are full of seawater in two hydro-cylinders;
Step 2: to glass metal valve tube resorber, resorber is followed the tracks of sun line optically focused to the stripe-shape plane speculum of fixed bar shaped minute surface reflecting and condensing device with the sun power line reflection; Behind the resorber of pure water through sun energy line optically focused, be heated to form 110-150 ℃ of saturated wetting vapour, reach the vapor pressure about 1.43-4.76bar;
Step 3: the breather cheek valve of opening a steam driven seawater supercharging device, close one-way exhaust valve and the water intaking valve of this steam driven seawater supercharging device, steam enters the pneumatic cylinder of this steam driven seawater supercharging device, expand and do work, promote hydraulic efficiency piston by piston rod, the hydro-cylinder rate of supercharging is 36:1; When steam reaches certain pressure, Steam Actuation gas drive piston, thus promote hydraulic efficiency piston compression seawater through the intermediate piston bar, enter reverse osmosis desalination device through the seawater after the supercharging and produce fresh water and strong brine; When the hydraulic efficiency piston of steam driven seawater supercharging device moves to the cylinder body right-hand member, steam off drives the breather cheek valve of seawater supercharging device, open one-way exhaust valve and the water intaking valve of steam driven seawater supercharging device, steam enters solidifying air chamber and condenses into water through hot tube heat exchanger, forms negative pressure and makes seawater be easy to again be full of hydro-cylinder; Another steam driven seawater supercharging device was started working when hydro-cylinder was filled, and the method for work of another steam driven seawater supercharging device is consistent with the method for work of above-mentioned steam driven seawater supercharging device; Alternate cycles like this;
Step 4: the steam of discharge is condensed into water through the hot tube heat exchanger between solidifying air chamber and the evaporator room, arranges to fresh-water tank by the check valve of pipeline, and the water of fresh-water tank enters resorber by water circulating pump and again is heated into steam by optically focused; Evaporator room makes seawater obtain rapid evaporation through the heat exchange of hot tube heat exchanger, spray and the injector suction of nozzle simultaneously, and secondary steam enters condensing chamber and is condensed into the fresh water discharge; Cooling room obtains pre-hot sea water by the warm air cooling to gas drive piston the right in piston rod and the pneumatic cylinder.
10. a kind of fixedly bar shaped minute surface sun energy line optically focused as claimed in claim 9 makes up method for desalting seawater, it is characterized in that, described hot tube heat exchanger produces negative pressure to the steam of discharging in solidifying air chamber condensation, and seawater automatically refills hydraulic cylinder body, flashes to secondary steam in the heat absorption of evaporator room seawater; Described injector produces vacuum tightness to the evaporator room gas injection, accelerates evaporation; The injector injection forms saturated low-pressure steam, enters cooling room through seawater condensing, produces fresh water and discharges, and seawater preheating enters evaporator room.
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CN103265140A (en) * 2013-05-17 2013-08-28 山东大学 Solar line focusing-wind energy synergetic ultrasonic sea water desalting device and method
CN105936520A (en) * 2016-06-12 2016-09-14 河海大学常州校区 Electric heating piston reciprocating type seawater desalination system
CN107720863A (en) * 2017-11-13 2018-02-23 华北电力大学 A kind of groove type solar sea water desalinating unit based on film distillation
CN108892299A (en) * 2018-06-26 2018-11-27 东营市农业科学研究院 A kind of combined type salt separation water-fertilizer integral device
CN108910998A (en) * 2018-07-24 2018-11-30 王利利 A kind of multifuctional solar vacuum fresh water generator
CN110272161A (en) * 2019-07-31 2019-09-24 江西科技师范大学 Bar shaped mirror surface collection thermoelectric energizes microwave heating desalination plant and desalination method
CN112815538A (en) * 2021-01-15 2021-05-18 南京索乐优节能科技有限公司 Reflection fixed type line focusing heat collection unit and reflection fixed type line focusing heat collection device

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CN103112927A (en) * 2013-03-06 2013-05-22 陈大千 Transmitting system powered by compressed air and seawater desalination method and system
CN103112927B (en) * 2013-03-06 2015-04-15 陈大千 Transmitting system powered by compressed air and seawater desalination method and system
CN103265140A (en) * 2013-05-17 2013-08-28 山东大学 Solar line focusing-wind energy synergetic ultrasonic sea water desalting device and method
CN103265140B (en) * 2013-05-17 2014-08-06 山东大学 Solar line focusing-wind energy synergetic ultrasonic sea water desalting device and method
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CN105936520B (en) * 2016-06-12 2019-01-08 河海大学常州校区 A kind of electric heating piston reciprocating type seawater desalination system
CN107720863A (en) * 2017-11-13 2018-02-23 华北电力大学 A kind of groove type solar sea water desalinating unit based on film distillation
CN108892299A (en) * 2018-06-26 2018-11-27 东营市农业科学研究院 A kind of combined type salt separation water-fertilizer integral device
CN108892299B (en) * 2018-06-26 2023-09-22 东营市农业科学研究院 Combined salt separation water and fertilizer integrated device
CN108910998A (en) * 2018-07-24 2018-11-30 王利利 A kind of multifuctional solar vacuum fresh water generator
CN110272161A (en) * 2019-07-31 2019-09-24 江西科技师范大学 Bar shaped mirror surface collection thermoelectric energizes microwave heating desalination plant and desalination method
CN112815538A (en) * 2021-01-15 2021-05-18 南京索乐优节能科技有限公司 Reflection fixed type line focusing heat collection unit and reflection fixed type line focusing heat collection device

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