CN1656021A - Distillation generating system - Google Patents
Distillation generating system Download PDFInfo
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- CN1656021A CN1656021A CNA038114364A CN03811436A CN1656021A CN 1656021 A CN1656021 A CN 1656021A CN A038114364 A CNA038114364 A CN A038114364A CN 03811436 A CN03811436 A CN 03811436A CN 1656021 A CN1656021 A CN 1656021A
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- Prior art keywords
- steam
- exchanger
- distillation
- solenoid valve
- valve control
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/007—Energy recuperation; Heat pumps
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/045—Treatment of water, waste water, or sewage by heating by distillation or evaporation for obtaining ultra-pure water
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
The present invention discloses a sort of distilling power generation system, which is comprised of a distilling electric generating apparatus, a drying device, a heat-energy recoving apparatus and an automatic controlling device, concretely it can be joint with one or multiple distilling exchanger, one or multiple gas turbine, a constant pressured and potential difference injector, a drier and a heat energy recoverer, these equipment is joint with pipeline and form a system which have a great distilling and electric energy production and little of the system can be adjusted; the system adopts the new circular theory of closed cycle, it consumes the actuating energy when it is first started, when it works, there is no pollution or noise and the system do exchange of the temperature difference and the pressure difference with low energy consumption, at the exchange course it distills the water or sewage into pure distilled water, and it can produce electricity and provide electricity to outside at the same time.
Description
Distill electricity generation system technical field
The present invention relates to one kind distill electricity generation system, more particularly to a kind of Non-energy-consumption to seawater, sewage carry out distil(l) processing while and generate electricity device.Prior art
At present, desalinization is only limited to membrane technology in the world, and the shortcoming of the technology is:First, the water after desalinating only removes the sodium magnesium ion in seawater, and the heavy metal thing in seawater can not be removed, easily human life and health is caused harm if drinking, 2nd, the sewage that one ton of seawater will discharge the magnesium ion containing sodium at high concentration of one ton of high temperature is often desalinated, coastal ecological environment is caused harm, three, the cost of desalination water it is higher than running water price several times.The content of the invention
In view of the deficiency of above-mentioned technology, " closed cycle " distillating method Non-energy-consumption, seawater and sewage the distillation desalination of low-cost and pollution-less and the system generated electricity are utilized it is an object of the invention to provide one kind.
To achieve the above object, adopt the following technical scheme that：
It is provided by the present invention distillation electricity generation system be：Whole system whole heat-barrier material is thermally insulated and is made up of corrosion-resistant metal materials, constituted by steaming leavened TRT, drying device, heat-energy recovering apparatus and pipeline and computer automatic controlled system, specifically included distillation exchanger, electric heater, etc. the equipment such as pressure head injector, gas-turbine, storage tank, drier, thermal energy recoverer；
It is described by distillation TRT, constituted by one or more distillation exchanger, pressure head injector, one storage tank of a gas-turbine such as two and by the pipeline of solenoid valve control：
The leavened exchanger of wherein described steaming, it is the housing in the hollow two ends top dome of column type being made up of corrosion-resistant metal materials, two through holes are set at the top of distillation exchanger, one of them for distillation exchanger safety valve and pressure gauge ' install and the shared pore of steam (vapor) outlet, another steam inlet being connected with the spiral heat exchange pipe coil case top through hole suitable for reading being provided with distillation exchanger；10 centimeters are provided with upper and lower two through holes, the delivery port that upper through hole is the heating steam inlet for the distillation exchanger being connected with electric heater steam (vapor) outlet, lower through-hole is the distillation exchanger being connected with electric heater cold water inlet below the lowest water level line of distillation exchanger case inside top；Three through hole is also set in distillation exchanger bottom, wherein first is the cold water inlet communicated with distillation exchanger inner bag, second is with distilling the condensation-water drain that mouth housing bottom through hole is connected under the spiral heat exchange pipe coil being provided with exchanger, storage tank is set below condensation-water drain, the 3rd is that the dense salt by solenoid valve control is communicated with distillation exchanger inner bag
Liquid is exported；In addition in distillation exchanger housing upper lateral part, a through hole being connected with water level, pressure, automatic temperature control instrument is separately set；In distillation exchanger housing side lower part, a through hole being connected with salinity auto-controller is also set；Wherein described two wait pressure head injector to be the housing in the hollow two ends top dome of column type being made up of corrosion-resistant metal materials, two pores are respectively set in housing top dome, bottom, one through hole is exhaust outlet of the case top by solenoid valve control, another through hole is vapour inlet of the case top by solenoid valve control, one through hole is the cold water inlet that with water source is connected of the housing bottom by solenoid valve control, and another through hole is delivery port of the housing bottom by solenoid valve control；The wherein described gas-turbine being made up of corrosion-resistant metal materials, it is to be located at the top of distillation exchanger, be made up of metal material, sealing, insulation, pressurize drive generator acting the forward and backward gas-turbine for setting two mouths altogether, it is preceding be gas-turbine steam inlet, after be gas-turbine steam (vapor) outlet；Wherein described drying device is made up of distillery, hothouse, agitator and thermal energy recoverer and pipeline；Wherein described drying device, be the hollow two ends top dome of column type being made up of corrosion-resistant metal materials Double-layer liner housing, it is distillery between the inside and outside pair of courage in double-bladder type housing, a steam inlet is set on the outdoor courage top dome portion through hole of distillation, a steam (vapor) outlet is set by the outside middle and lower part through hole of the outdoor courage of distillation, an automatic cold air valve and the shared pore of steam trap are divided into the outdoor courage ball bottom through-hole of distillation；It is hothouse in double courages in double-bladder type housing, a dense saline solution entrance is set on the through hole set at the top of the double courages of hothouse on through hole at the top of a steam (vapor) outlet and double courages, setting the high temperature drying salt by solenoid valve control on the double courage bottom through-holes of hothouse exports；Wherein described agitator is manufactured by corrosion-resistant metal materials, is located in hothouse, the upper end with flight stirring shaft, is connected from the bottom to top through double Hymecromone holes with the decelerator being fixed at the top of double courages；Wherein described thermal energy recoverer is the housing in the hollow two ends top dome of column type being made up of corrosion-resistant metal materials, two through holes are respectively set in the top of thermal energy recoverer, bottom, hole is the steam (vapor) outlet of recover on one of them, one of lower opening is the cold water inlet by solenoid valve control, the spiral heat exchange pipe coil that upper/lower terminal is each passed through top, bottom through-hole is connected with housing is additionally provided with thermal energy recoverer, upper orifice is high temperature drying salt entrance；Lower nozzle exports for cool drying salt.
The present invention, is mainly included：Distill TRT, drying device, heat-energy recovering apparatus and pipeline and computer automatic controlled system；Described distillation electricity generation system is interior, also include distillation exchanger, electric heater, etc. pressure head injector, gas-turbine, storage tank, drier, thermal energy recoverer road constitute；
The system of the present invention is so connected：The vapour inlet of solenoid valve control and company at the top of pressure head impregnator are waited in one end to the steam (vapor) outlet of solenoid valve control with two by the road at the top of described distillation exchanger, the other end is connected with the steam inlet of gas-turbine, the steam (vapor) outlet of gas-turbine is connected with the steam inlet at the top of distillery in drying device by the road, the steam (vapor) outlet for drying the top of outdoor courage is connected with distilling the steam inlet of exchanger inside spin heat exchange coil upper end by the road, and the condensation-water drain of distillation exchanger inside spin heat exchange coil lower end is discharged to storage tank；The water inlet of solenoid valve control of exchanger bottom is distilled by the road with waiting two of pressure head injector bottom
It is connected by the water filling valve port of solenoid valve control；
One end is connected the steam (vapor) outlet of distillery side middle and lower part with the steam (vapor) outlet of solenoid valve control at the top of thermal energy recoverer by the road, and the other end and the steam inlet of distillation exchanger inside spin heat exchange coil upper end are mutually contacted；
Two are waited the housing ball bottom of pressure head impregnator to be connected by the road with pressure water source by solenoid valve control phase and two water inlets even；The high temperature drying salt outlet of the solenoid valve control of hothouse bottom in drying device is connected with high temperature drying salt entrance at the top of thermal energy recoverer by the road, and thermal energy recoverer bottom coohng dry salt outlet lower section sets dry salt storage bin；Thermal energy recoverer bottom is connected with pressure water source by the road by the cold water inlet of solenoid valve control.
The present invention is compared than prior art to be had the following advantages：Disposable to start, during operating, pollution-free, noiseless, three-waste free discharge, steaming sewage, seawater leavened for Non-energy-consumption are the leavened water of steaming cleaned, and provide free electric energy simultaneously.
Embodiments of the invention are elaborated below in conjunction with accompanying drawing, so as to become apparent from more detailed understanding to the present invention.Brief description of the drawings
Fig. 1 is the implementation schematic diagram of present invention distillation electricity generation system.Embodiment
Electricity generation system is distilled, by：Distillation TRT, drying device, heat-energy recovering apparatus and pipeline are connected with each other to be constituted by computer automatic controlled system is program control,
Described distillation TRT by distillation exchanger 14, two wait pressure head injector 1,2, the storage tank 46 of gas-turbine 24 and be made up of the pipeline of solenoid valve control：
Wherein described distillation exchanger 14, it is the housing in the hollow two ends top dome of column type being made up of corrosion-resistant metal materials, two through holes are set at the top of distillation exchanger 14, one of them is installed and the shared pore of steam (vapor) outlet 22 for the safety valve 141 and pressure gauge 142 of distillation exchanger 14, another steam inlet 21 being connected with the case top through hole suitable for reading of spiral heat exchange pipe coil 15 being provided with distillation exchanger 14;10 centimeters are provided with upper and lower two through holes, the delivery port 13 that upper through hole is the steam inlet 12 for the distillation exchanger 14 being connected with the steam (vapor) outlet 121 of electric heater 122, lower through-hole is the distillation exchanger 14 being connected with the cold water inlet 123 of electric heater 122 below the distillation case inside top lowest water level line of exchanger 14;Three through hole is also set in distillation exchanger 14 bottom, wherein first is the cold water inlet 16 communicated with the distillation inner bag of exchanger 14, second is the condensation-water drain 17 being connected with the 15 lower mouthfuls of housing bottom through holes of spiral heat exchange pipe coil being provided with distillation exchanger 14, the lower section of condensation-water drain 17 sets storage tank 46, and the 3rd is that the dense salt by solenoid valve control is communicated with the distillation inner bag of exchanger 14
Liquid outlet 18;In addition one and water level, pressure, automatic temperature control instrument 20 are separately set in the through hole of the distillation housing upper lateral part of exchanger 14;One and salinity auto-controller 19 are also set in the through hole for steaming the leavened housing side lower part of exchanger 14；
Wherein described two wait pressure head injectors 1,2, be housing in the hollow two ends top dome of column type being made up of corrosion-resistant metal materials, two pores are respectively set in housing top dome, bottom, one through hole is exhaust outlet 3,6 of the case top by solenoid valve control, another through hole is vapour inlet 4,5 of the case top by solenoid valve control, one of through hole is the cold water inlet 7,9 that with pressure water source 11 is connected of the housing bottom by solenoid valve control, and another through hole is delivery port 8,10 of the housing bottom by solenoid valve control；
The wherein described gas-turbine 24 being made up of corrosion-resistant metal materials, it is to be located at the top of distillation exchanger 14, it is made up of metal material, sealing, insulation, pressurize drive generator acting the forward and backward gas-turbine 24 for setting two mouths altogether, it is preceding be gas-turbine steam inlet 23, after be gas-turbine steam (vapor) outlet 25;
Wherein described drying device is made up of distillery 29, hothouse 30, agitator 31 and thermal energy recoverer 40 and pipeline；
Wherein described drying device is the Double-layer liner housing for the hollow two ends top dome of column type being made up of corrosion-resistant metal materials, it is distillery 29 between the inside and outside pair of courage in double-bladder type housing 32, a steam inlet 26 is set on the outer courage top dome portion through hole of distillery 29, a steam (vapor) outlet 34 is set by the outside middle and lower part through hole of the outer courage of distillery 29, the shared pore of automatic a cold wind wealthy 35 and steam trap 36 is divided into the outer courage ball bottom through-hole of distillery 29；It is hothouse 30 in inner bag in double-bladder type housing 32, a dense saline solution entrance 33 is set on the through hole set at the top of the inside and outside courage of hothouse 30 on through hole at the top of a steam (vapor) outlet 28 and inside and outside courage, the high temperature drying salt by solenoid valve control is set on the inside and outside courage bottom through-hole of hothouse 30 and exports 37; .
Wherein described agitator 31 is manufactured by corrosion-resistant metal materials, is located in hothouse 30, the upper end with the stirring shaft of flight 31, is connected from the bottom to top through double Hymecromone holes with the decelerator 27 being fixed at the top of double courages；Wherein described heat-energy recovering apparatus 40 is the thermal energy recoverer 40 for the hollow two ends top dome housing of column type being made up of corrosion-resistant metal materials, two through holes are respectively set in the top of thermal energy recoverer 40, bottom, hole is the steam (vapor) outlet 38 of thermal energy recoverer 40 on one of them, one of lower opening is the cold water inlet 44 by solenoid valve control, the spiral heat exchange pipe coil 41 that upper/lower terminal is each passed through top, bottom through-hole is connected with housing is additionally provided with thermal energy recoverer 40, upper orifice is high temperature drying salt entrance 39;Lower nozzle is cool drying salt outlet 42.
Each position of distillation electricity generation system of the present invention is so connected：
The steam (vapor) outlet 22 of the described distillation top solenoid valve control of exchanger 14 by the road one end with waiting pressure head impregnator 1, the vapour inlet 4,5 of 2 top solenoid valve controls and even, the other end is connected with the steam inlet 23 of gas-turbine 24, the steam of the steam (vapor) outlet 25 of gas-turbine 24 by the road with the top of distillery in drying device 29
Entrance 26 is connected, steam inlet 21 of the steam (vapor) outlet 28 at the top of the outer courage of hothouse 30 by the road with distillation 14 inside spin heat exchange coil of exchanger 15 upper end is connected, and the condensation-water drain 17 of the lower end of 14 inside spin heat exchange coil of distillation exchanger 15 is discharged to storage tank 46；
The water inlet 16 of the solenoid valve control of distillation exchanger 14 bottom by the road with wait pressure head injector 1, two of 2 bottoms be connected by the water filling valve port 8,10 of solenoid valve control；
One end is connected the steam (vapor) outlet 34 of the side middle and lower part of distillery 29 with the steam (vapor) outlet 38 of the top solenoid valve control of thermal energy recoverer 40 by the road, and the other end and the steam inlet 21 of distillation 14 inside spin heat exchange coil of exchanger 15 upper end are mutually contacted；
Housing ball bottom Deng pressure head impregnator 1,2 is connected with pressure water source 11 by the road by solenoid valve control phase and water inlet 7,9 even；
The high temperature drying salt outlet 37 of the solenoid valve control of the bottom of hothouse 30 in drying device is connected with the top high temperature drying salt entrance 39 of thermal energy recoverer 40 by the road, and the lower section of the bottom coohng dry salt of thermal energy recoverer 40 outlet 42 sets dry salt storage bin； ·
The bottom of thermal energy recoverer 40 is connected with pressure water source 11 by the road by the cold water inlet 44 of solenoid valve control.The distillation electricity generation system of the present invention, so works：First turn on the integrated circuit of automaton
45 make have the pressure saline source mouth of pipe 11 by solenoid valve control, Deng the bottom of pressure head injector 1 by solenoid valve control cold water inlet 7, Deng the top of pressure head injector 1 by the bottom of the grade pressure head of air bleeding valve 3 injector 1 of solenoid valve control by solenoid valve control delivery port 8 and the coupled by the road bottom of steam exchanger 14 by solenoid valve control cold water inlet 16, the top of steam exchanger 14 by solenoid valve control steam (vapor) outlet 22 and by pipeline be connected with steam (vapor) outlet 22 etc. at the top of pressure head injector 1 by the unlatching simultaneously automatically of the above all of valves such as the steam inlet 4 of solenoid valve control；
There is pressure cold water through waiting bottom of pressure head injector 1 to enter by the road in steam exchanger 14 because of water-head, the air in steam exchanger 14 is set to be forced out by the steam (vapor) outlet at top through the pressure head injector 1 such as pipe entrance top, then by the air bleeding valve doorway at top；Treat that water level reaches water level in steam exchanger 14, pressure, temperature-controlled instrument is restricted water supply position, it is first shut off automatically by the steam (vapor) outlet 22 of solenoid valve control at the top of the cold water inlet 16 and steam exchanger 14 by solenoid valve control of the bottom of steam exchanger 14, when waiting the water level in pressure head injector 1 also to reach to restrict water supply, there is the pressure saline source mouth of pipe 11 by solenoid valve control, Deng the bottom of pressure head injector 1 by solenoid valve control cold water inlet 7, also closed automatically by the delivery port 8 of solenoid valve control by the bottom of the grade pressure head of air bleeding valve 3 injector 1 of solenoid valve control Deng the top of pressure head injector 1；
The electric heater that the upside of steam exchanger 14 is provided with starts automatic heating, makes 10 centimeters above water below the top lowest water level in the housing of steam exchanger 14, is vaporized to high pressure gas, in steam exchanger 14
Needed for steam pressure reaches work during pressure；
The top of steam exchanger 14 by the steam (vapor) outlet 22 of solenoid valve control, the bottom of steam exchanger 14 by solenoid valve control cold water inlet 16, etc. the top of pressure head injector 1 by the steam inlet 4 of solenoid valve control, etc. the bottom of pressure head injector 1 by the automatic unlatching simultaneously again of delivery port 8 of solenoid valve control, enable to be vaporized reduced water in steam exchanger 14 and supplement；And by solenoid valve control have the pressure saline source mouth of pipe 11, etc. the bottom of pressure head injector 2 by solenoid valve control cold water inlet 9, etc. the top of pressure head injector 2 opened simultaneously by the air bleeding valve 6 of solenoid valve control, pressure water is pressed into etc. in pressure head injector 2, and a three above valve to be achieved of restricting water supply is closed automatically；
When waiting, the note of the hydraulic pressure in pressure head injector 1 is most, Deng the top of pressure head injector 1 by the steam inlet 4 of solenoid valve control, etc. the bottom of pressure head injector 1 by solenoid valve control delivery port 8 it is automatic again close, wait the top of pressure head injector 1 by solenoid valve control exhaust outlet 3, etc. the bottom of pressure head injector 1 have the automatic opening simultaneously of the pressure saline source mouth of pipe 11 by the cold water inlet 7 of solenoid valve control and by solenoid valve control；
And wait the top of pressure head injector 2 by the steam inlet 5 of solenoid valve control, etc. the bottom of pressure head injector 1 automatically turned on by the delivery port 10 of solenoid valve control；Hydraulic pressure note in pressure head injector 2 to be waited is to the greatest extent, Deng the water in pressure head injector 1 automatically continue again cycle alternation supplemented into steam exchanger 14 needed for the water of evaporation steam by entrance 23 of the pipeline through steam turbine 24, promotes wheel rotation to drive generator acting into gas-turbine simultaneously；
The high temperature and high pressure steam pressed out by the outlet 25 of steam turbine 24 is by the road, wherein enter and the distillery steam inlet 26 on the top shell of distillery 29 in drying device all the way, the heat release in distillery 29, cold wind and condensed water are automatically drained out from the outer bottom of distillery 29 by the shared mouth of pipe of the automatic cold air valve 35 and steam trap 36 of solenoid valve control, and condensed water is discharged into the storage tank 46 of bottom by the road;Steam is back to the steam inlet 21 of the upper end of spiral heat exchange pipe coil 15 in steam exchanger 14 from the outer middle and lower part of distillery 29 by the road by the steam (vapor) outlet 34 of solenoid valve control after the hot saturation in room 29 to be distilled, the principle of " closed cycle " is pressed in into the spiral heat exchange pipe coil 15 in steam exchanger 14, from top to bottom carry out the temperature difference with the cold water in steam exchanger 14 to exchange, the steam in spiral heat exchange pipe coil 15 is condensed into condensed water and is discharged into storage tank 46 by the condensation-water drain 17 of solenoid valve control through the lower end of spiral heat exchange pipe coil 15;
The cold water of the inner top of steam exchanger 14 is vaporizated into high steam in temperature difference exchange, circulates again and steam turbine is done work.
The concentration of the salt solution distillation in steam exchanger 14 is treated, the concentration that auto-controller is limited is reached, the bottom of steam exchanger 14 exports 18 valves by the dense saline solution of solenoid valve control and automatically turned on, is pressed into by the road in dry device
The dense saline solution entrance 33 of the interior upper lateral part of hothouse 30, into in hothouse 30, the rotation acting automatically of agitator 31, dense saline solution heat absorption is vaporizated into steam, and the steam (vapor) outlet 28 through the top of hothouse 30 is managed with the outer middle and lower part of distillery 29 by the steam (vapor) outlet 34 of solenoid valve control with the steam inlet 21 of the upper end of spiral heat exchange pipe coil 15 in steam exchanger 14 to be connected；Dense saline solution in hothouse 30 is dried to high temperature salt fines, the inner bottom part of hothouse 30 is automatically turned on by the high temperature drying salt outlet 37 of solenoid valve control, enter from the high temperature drying salt entrance 39 at the top of thermal energy recoverer 40 in the spiral heat exchange pipe coil 41 in thermal energy recoverer 40, the principle of " closed cycle " is pressed with the cold water in thermal energy recoverer 40, from top to bottom exchanged heat, normal temperature salt fines are condensed into the exit of the lower end of spiral heat exchange pipe coil 41, cool drying salt outlet 42 through the lower bottom part of thermal energy recoverer 40, fall into lower section dry salt storage bin 43；Cold water in high temperature drying salt with thermal energy recoverer 40 is from top to bottom exchanged heat, steam (vapor) outlet 38 of the raw steam at the top of thermal energy recoverer 40, into with steaming in the steam pipework that the leavened steam (vapor) outlet 34 of room 29 is connected, heat exchange carries out temperature difference exchange in into steam exchanger 14, system is reached that Non-energy-consumption does work in operation.
The operation principle of the present invention is as follows：The present invention is, according to " the Nature closed cycle " rule, using " heat is difficult downward conduction phenomenon ", " low-temperature heat source " to be carried out to the temperature difference, pressure difference Non-energy-consumption from the bottom to top, in exchanger and exchanged by " high temperature heat source " from top to bottom.It only need to disposably be started, and 3/1000ths thermal energy losses caused by itself are supplemented in the running.
The multigroup gas-turbine of multigroup distillation exchanger life can also be chained together and constitute one or more large and small different distillation electricity generation systems by the present invention.Industrial applicability
Present system disposably starts, pollution-free during operating, noiseless, three-waste free discharge, operates low energy consumption, not only can be by the distilled water of sewage, seawater cleaning for cleaning, and provides electric energy simultaneously, industrially applicable.
Claims (1)
- Claim1st, electricity generation system is distilled, by：Steam leavened TRT, drying device, heat-energy recovering apparatus and pipeline and computer automatic controlled system composition, it is characterised in that：Described distillation TRT is by distillation exchanger（14), two are waited pressure head impregnator（1 )、 （2), gas-turbine（24), storage tank（46) and by the pipeline of solenoid valve control constitute：Wherein described distillation exchanger（14), it is the housing for the hollow two ends top dome of column type being made up of corrosion-resistant metal materials, it is interior to be provided with spiral heat exchange pipe coil（15);Distill exchanger（14) top sets two through holes, and one of them is distillation exchanger（14) safety valve（And pressure gauge 141)（142) install and steam (vapor) outlet（22) shared pore, another is to be located at distillation exchanger（14) spiral heat exchange pipe coil in（15) steam inlet suitable for reading（21) pore；Steaming leavened exchanger（14) 10 centimeters below case inside top lowest water level line are provided with upper and lower two through holes, and upper through hole is steam inlet（12), with electric heater（122) steam (vapor) outlet（121) it is connected, lower through-hole is delivery port（13), with electric heater（122) cold water inlet（123) it is connected；Steaming leavened exchanger（14) bottom also sets three through hole, wherein first is and distillation exchanger（14) cold water inlet that inner bag is communicated（16) pore, second is to be located at distillation exchanger（14) spiral heat exchange pipe coil in（15) spiral heat exchange pipe coil（15) condensation-water drain of bottom（17) pore, condensation-water drain（17) lower section sets storage tank（46), the 3rd is and distillation exchanger（14) inner bag is communicated exports (18) pore by the dense saline solution of solenoid valve control；In addition in distillation exchanger（14) housing upper lateral part sets water level, pressure, an automatic temperature control instrument（20);In distillation exchanger（14) housing side lower part sets a salinity auto-controller（19);Wherein described two wait pressure head impregnator（1 )、 （2), it is the housing for the hollow two ends top dome of column type being made up of corrosion-resistant metal materials, two through holes is respectively set in housing top dome, bottom, top one through hole is the exhaust outlet by solenoid valve control（3)、 （6), another through hole is the vapour inlet by solenoid valve control（4)、 ( 5)；Bottom one through hole is by solenoid valve control and pressure water source（11) connected cold water inlet（7)、 （9), another through hole is the delivery port by solenoid valve control（8)、 ( 10)；Wherein described gas-turbine（24) it is made up of corrosion-resistant metal materials, is located at the leavened exchanger of steaming（14) top, it seals, is incubated, pressurize, drives generator acting, gas-turbine（24) forward and backward sets two mouths, and preceding is gas-turbine steam inlet（23), it is afterwards gas-turbine steam (vapor) outlet（25);The drying device is by distillery（29), hothouse（30), agitator（31) constituted with thermal energy recoverer (40) and pipeline；Wherein described drying device is the Double-layer liner housing for the hollow two ends top dome of column type being made up of corrosion-resistant metal materials, in double-bladder type housing（32) it is distillery between inside and outside pair of courage in（29), the distillery（29) δ Outer courage top dome portion sets a steam inlet（26), distillation room（29) the outside middle and lower part of outer courage sets a steam (vapor) outlet（34), in distillery（29) outer courage ball bottom sets an automatic cold air valve（And steam trap 35)（36) shared pore；In double-bladder type housing（32) it is hothouse in the inner bag in（30), in the hothouse（30) a steam (vapor) outlet is set at the top of inside and outside courage（28) and a dense saline solution entrance is set（33), in hothouse（30) inside and outside courage bottom sets the high temperature drying salt by solenoid valve control and exported（37);Wherein described agitator (31) is manufactured by corrosion-resistant metal materials, stirring shaft band flight（31), stirring shaft is with being fixed on double-bladder type housing（32) decelerator at the top of（27) it is connected and through double-bladder type housing（32) stretch into hothouse (30)；Wherein described thermal energy recoverer（40) it is the housing for the hollow two ends top dome of column type being made up of corrosion-resistant metal materials, it is pushed up, bottom respectively sets two through holes, hole is thermal energy recoverer on one of them（40) steam (vapor) outlet (38), one of lower opening is the cold water inlet by solenoid valve control（44), in thermal energy recoverer（40) spiral heat exchange pipe coil that upper/lower terminal is each passed through top, bottom through-hole is connected with housing is additionally provided with（41), upper orifice is high temperature drying salt entrance（39);Lower nozzle exports for cool drying salt（42).2nd, electricity generation system is distilled according to claim 1, it is characterised in that：Described distillation exchanger（14) steam (vapor) outlet of top solenoid valve control（22) by the road one end with wait pressure head impregnator（1), the vapour inlet of (2) top solenoid valve control（4), (5) and company, the other end is connected with the steam inlet (23) of gas-turbine (24), the steam (vapor) outlet (25) of gas-turbine (24) by the road with distillery in drying device（29) steam inlet at the top of（26) it is connected, hothouse（30) steam (vapor) outlet at the top of outer courage（28) by the road with steaming leavened exchanger（14) inside spin heat exchange coil（15) steam inlet of upper end（21) it is connected, distills exchanger（14) inside spin heat exchange coil（15) condensation-water drain of lower end（17) to storage tank（46) discharge； .Distillery（29) steam (vapor) outlet of side middle and lower part（34) one end and thermal energy recoverer by the road（40) steam (vapor) outlet of top solenoid valve control（38) it is connected, the other end and distillation exchanger（14) inside spin heat exchange coil（15) steam inlet of upper end（21) mutually contact；Deng pressure head impregnator（1), the housing ball bottom of (2) is by solenoid valve control phase and delivery port even（8)、(10) by the road with distilling exchanger（14) bottom water inlet（16) it is connected；Deng pressure head impregnator（1), the housing ball bottom of (2) is by solenoid valve control phase and water inlet even（ 7 )、（9) by the road with pressure water source（11) it is connected；Hothouse in drying device（30) the high temperature drying salt outlet of the solenoid valve control of bottom（37) by the road with thermal energy recoverer（40) top high temperature drying salt entrance（39) it is connected, thermal energy recoverer（40) bottom coohng dry salt is exported（42) lower section sets dry salt storage bin（43); Thermal energy recoverer（40) bottom by solenoid valve control cold water inlet（44) by the road with pressure water source α ι) be connected.3rd, distillation electricity generation system according to claim 1 or claim 2, it is characterised in that：Whole system whole magnetic valve and water level, pressure, automatic temperature control instrument（20), electric heater is all by computer system（45) automatic control carries out alternately open and close.4th, distillation electricity generation system according to claim 1 or claim 2, it is characterised in that：The various devices and pipeline of whole system all must be by the heat-insulated processing of heat-barrier material.5th, electricity generation system is distilled according to Claims 1-4, it is characterised in that：Gen Expansion design requirements are by multiple distillation exchangers（And gas-turbine 14)（24) the distillation electricity generation system of series combination Cheng Geng great energy.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN02116203.4 | 2002-03-19 | ||
| CN02116203A CN1445011A (en) | 2002-03-19 | 2002-03-19 | Distilling apparatus without energy consumption |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1656021A true CN1656021A (en) | 2005-08-17 |
Family
ID=27811309
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN02116203A Pending CN1445011A (en) | 2002-03-19 | 2002-03-19 | Distilling apparatus without energy consumption |
| CNA038114364A Pending CN1656021A (en) | 2002-03-19 | 2003-03-19 | Distillation generating system |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN02116203A Pending CN1445011A (en) | 2002-03-19 | 2002-03-19 | Distilling apparatus without energy consumption |
Country Status (3)
| Country | Link |
|---|---|
| CN (2) | CN1445011A (en) |
| AU (1) | AU2003227164A1 (en) |
| WO (1) | WO2003078329A1 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102606792A (en) * | 2012-04-06 | 2012-07-25 | 重庆大学 | Vent valve system preventing city water transmission and distribution pipe network system from secondary pollution |
| CN103574583B (en) * | 2013-11-14 | 2015-04-08 | 哈尔滨工程大学 | Load-variable moisture separator suitable for steam system |
| WO2016166768A1 (en) * | 2015-04-17 | 2016-10-20 | Amit Katyal | System and method for simultaneous evaporation and condensation in connected vessels |
| US10876772B2 (en) | 2015-04-17 | 2020-12-29 | Amit Katyal | System and method for simultaneous evaporation and condensation in connected vessels |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3002957A1 (en) * | 1980-01-29 | 1981-07-30 | Heinz-Jürgen 3300 Braunschweig Schymura | Sewage and industrial wastes utilisation - by precleaning, distillation producing steam for power generation, and heat pumps |
| CN1010853B (en) * | 1984-07-20 | 1990-12-19 | 西门子股份有限公司 | Steam power equipment generating steam from natural water contg. salt |
| CN1012690B (en) * | 1985-08-15 | 1991-05-29 | 刘幸生 | Generating equipment for desalination of seawater and purification of waste water |
| US4882012A (en) * | 1987-12-10 | 1989-11-21 | Kurt Wasserman | Water distiller |
| US4938868A (en) * | 1988-05-02 | 1990-07-03 | Nelson Thomas R | Method of distilling under partial vacuum |
| CN1105000A (en) * | 1993-12-09 | 1995-07-12 | 邝赤科 | Compler utilization system |
-
2002
- 2002-03-19 CN CN02116203A patent/CN1445011A/en active Pending
-
2003
- 2003-03-19 CN CNA038114364A patent/CN1656021A/en active Pending
- 2003-03-19 AU AU2003227164A patent/AU2003227164A1/en not_active Abandoned
- 2003-03-19 WO PCT/CN2003/000200 patent/WO2003078329A1/en not_active Application Discontinuation
Also Published As
| Publication number | Publication date |
|---|---|
| WO2003078329A1 (en) | 2003-09-25 |
| CN1445011A (en) | 2003-10-01 |
| AU2003227164A1 (en) | 2003-09-29 |
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