CN108516602A - A kind of heating power water process and the circulatory system - Google Patents
A kind of heating power water process and the circulatory system Download PDFInfo
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- CN108516602A CN108516602A CN201810668119.4A CN201810668119A CN108516602A CN 108516602 A CN108516602 A CN 108516602A CN 201810668119 A CN201810668119 A CN 201810668119A CN 108516602 A CN108516602 A CN 108516602A
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- positive displacement
- displacement pump
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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
-
- 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
- C02F1/043—Details
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K13/00—General layout or general methods of operation of complete plants
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/10—Energy recovery
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The present invention provides a kind of heating power water process and the circulatory systems,By heating power distillation unit,Carbonated drink supply unit forms,The pump of the carbonated drink supply unit is heat power positive displacement pump,The heat power positive displacement pump is by heat dump,Main pneumatic positive displacement pump,Pneumatic working medium circulation booster pump,Radiator,Cycle fluid and pipe valve composition,The heat dump of the heat power positive displacement pump is placed in main heat source or secondary heat source,Radiator is placed in low-temperature receiver,Due to being used as heat dissipation low-temperature receiver using accessing pending water solution or other low temperature environments,Heat dynamic resource using main heat source or secondary heat source as heat power positive displacement pump,The latent heat in water treatment procedure is not only utilized,The high-order energy is saved,And also improve the efficiency of water process,Reduce cost of water treatment,Water treatment system especially suitable for the driving of complete regenerative resource,Reduce the discharge of carbon dioxide,Mitigate room temperature effect.
Description
Technical field
The invention belongs to aqueous solution process fields, and in particular to heating power water process and the circulatory system.
Background technology
Existing heating power water process and the circulatory system include mainly：Vertical tube distillation, multistage flash distillation, both vapor compression distillation, negative pressure
It is evacuated the distillation separation methods such as distillation, solar distilling, air humidification dehumidification, absorption and sorption and nano material absorber of light.Heat
Power water process and circulator are mainly made of heating power distillation unit, carbonated drink supply unit.Heating power distillation unit is by main heat source, one
A above distiller（Evaporator）, condenser, pipe valve composition.Carbonated drink supply unit is made of pump, pipe valve, and accessing pending water is defeated through pumping
It is sent to main heat source heating or passes through main heat source heating into distillation in each distiller after flowing through heat exchanger preheating, distill acquisition
Carbonated drink becomes clean water output after conveying condenses, and remaining treated dope directly output or is inhaled through heat exchanger in distiller
It is exported after heat.Used circulating pump is typically all electrodynamic pump.Heat power source generally comprises the hot steam of boiler generation, the sun
It can heat collector heating（Including passive type solar energy Distallation systm and active solar energy Distallation systm）.In order to improve producing water ratio,
Investment and operating cost are reduced, scientists evaporate material therefor etc. from energy sources, apparatus structure, device and take one
Series of measures so that the economic and technical norms of water process have obtained different degrees of raising.But existing heating power water process side
Method remains：On the one hand the latent heat in the latent heat of condensation and concentrated water of treated steam is largely lost in air
, be not utilized effectively not only rate, but also influences the treatment effeciency to water.The cycle needs of another aspect aqueous solution pass through
Electric pump conveys, and consumes certain electric power, can not be used in the place without electricity.
Invention content
The technical problem to be solved by the present invention is to：Seek it is a kind of can by by treated cleaning hot vapour water in heat and by
Latent heat in concentrated solution that treated is used to drive the water solution cycle in water treatment procedure as the power of pump, is putting forward high yield water
While rate, operating cost is saved, reduces cost of water treatment, it is convenient to be run under no electric condition.
In order to achieve the above objectives with solve above-mentioned technical problem, technical solution proposed by the present invention is：
A kind of heating power water process and the circulatory system, are made of, the heating power distillation unit heating power distillation unit, carbonated drink supply unit
It is made of main heat source, more than one distiller, condenser, pipe valve, the carbonated drink supply unit is made of pump, pipe valve, pending
Water, which passes through main heat source after pump is transported to main heat source heating or flows through heat exchanger preheating and heats to enter in each distiller, to be distilled, and is steamed
It evaporates the carbonated drink of acquisition and becomes clean water output after conveying condenses, remaining in distiller treated that dope is directly exported or passed through
It is exported after heat exchanger heat absorption, it is characterised in that：The pump of the carbonated drink supply unit is heat power positive displacement pump, the heat power volume
Pump is made of heat dump, main pneumatic positive displacement pump, pneumatic working medium circulation booster pump, radiator, cycle fluid and pipe valve, and the heat is dynamic
The heat dump of power positive displacement pump is placed in main heat source or secondary heat source, and radiator is placed in low-temperature receiver, and the sender property outlet of heat dump is through pipe valve
With the working medium inlet communication of the pneumatic positive displacement pump of master, the working medium inlet communication of the sender property outlet and radiator of main pneumatic positive displacement pump dissipates
The sender property outlet of hot device is connected to the inlet of pneumatic working medium circulation booster pump, the liquid outlet of pneumatic working medium circulation booster pump and suction
The working medium inlet communication of hot device, the working medium import of pneumatic working medium circulation booster pump and sender property outlet are connected in parallel on main pneumatic positive displacement pump
In working medium import and sender property outlet, the water inlet of main pneumatic positive displacement pump is connected to pending water source, the water outlet of main pneumatic positive displacement pump
Mouthful be connected to radiator, after the water outlet of radiator and the preheated device of the inlet of main heat source or elder generation again with the inlet of main heat source
Connection, preheater are placed in time heat source, the secondary heat source refers to that treated dense hydrothermal solution or treated cleaning hot vapour water
Or assisted heating device or the heat source that is formed by above-mentioned three's connection in series-parallel, the main heat source is by a kind of main heating power source or by two
Kind or more main heating power subject string parallel running constitute.The energy of main heat source is generally higher than the energy of assisted heating device output, main
The energy source of heat source and assisted heating device includes the thermal energy converted by fossil energy and by the thermal energy of renewable energy conversion.
Above-mentioned thermal distillation unit include existing vertical tube distillation, multistage flash distillation, both vapor compression distillation, negative pressure ventilation distillation, solar distilling,
Thermal distillation unit in the distilling apparatus such as air humidification dehumidification, absorption and sorption and nano material absorber of light.Main pneumatic volume
Pump, pneumatic working medium circulation booster pump, radiator and working medium circulation pipe valve are compatible with used cycle fluid.
A kind of above-mentioned heating power water process and the circulatory system, alternative technology scheme are that treated in distiller
The one pneumatic positive displacement pump of auxiliary of concatenation, the working medium import of the pneumatic positive displacement pump of the auxiliary and sender property outlet are in parallel on vapor output pipe
In the working medium import and sender property outlet of the pneumatic positive displacement pump of master.The pneumatic positive displacement pump of the auxiliary can play the work of suction conveying vapor
With the pneumatic positive displacement pump of the auxiliary can also be a set of independently operated heat power positive displacement pump.Pneumatic positive displacement pump and working medium is assisted to follow
Endless tube valve is compatible with used cycle fluid.
A kind of above-mentioned heating power water process and the circulatory system, improved technical solution are, in parallel on the pneumatic positive displacement pump of master
The pneumatic positive displacement pump of one thermal energy balance, the working medium import of the pneumatic positive displacement pump of the thermal energy balance and sender property outlet are connected in parallel on main pneumatic volume
In the working medium import of pump and sender property outlet.The pneumatic positive displacement pump of the thermal energy balance can absorb clear hot-water or dense heat in balancing condenser
Extra thermal energy in water improves cycle efficieny.Thermal energy extra in heat source is converted into the potential energy of water simultaneously.Thermal energy balance is pneumatic
The structural principle of positive displacement pump is identical as main pneumatic positive displacement pump, the pneumatic structural principle of positive displacement pump of auxiliary.The pneumatic volume of thermal energy balance
Pump and working medium circulation pipe valve are compatible with used cycle fluid.
Above-mentioned any heating power water process and the circulatory system, alternative technology scheme are the carbonated drink conveyings
The heat dump of the heat power positive displacement pump of unit is placed in heat source, and radiator is placed in low-temperature receiver, refers to after heat dump is placed in and is handled
Dense hydrothermal solution in and an assisted heating device, radiator are placed in transported accessing pending water solution in parallel or series, institute
Stating preheater and being placed in heat source refers to that preheater is placed in by treated cleaning hot vapour water.
Above-mentioned any heating power water process and the circulatory system, alternative technology scheme are the carbonated drink conveyings
The heat dump of the heat power positive displacement pump of unit is placed in heat source, and radiator is placed in low-temperature receiver, refers to after heat dump is placed in and is handled
Cleaning hot vapour water in and an assisted heating device, radiator are placed in transported accessing pending water solution in parallel or series, institute
Stating preheater and being placed in heat source refers to that preheater is placed in by treated dense hydrothermal solution.
Above-mentioned any heating power water process and the circulatory system, alternative technology scheme are the carbonated drink conveyings
The heat dump of the heat power positive displacement pump of unit is placed in heat source, and radiator is placed in low-temperature receiver, refers to that heat dump is placed in solar energy collection
In hot device, radiator is placed in transported accessing pending water solution, the preheater be placed in heat source refer to preheater be placed in by
In treated dense hydrothermal solution or be placed in by treated clear hot-water, or by more than two preheaters be respectively placed in by
Dense hydrothermal solution after reason is neutralized by treated cleaning hot vapour water, is run in parallel or series between each preheater.
Above-mentioned any heating power water process and the circulatory system, alternative technology scheme are the carbonated drink conveyings
The heat dump of the heat power positive displacement pump of unit is placed in heat source, and radiator is placed in low-temperature receiver, refers to that heat dump is placed in boiler or pot
In the hot vapour water of stove waste heat, radiator is placed in transported accessing pending water solution, and it refers to pre- that the preheater, which is placed in heat source,
Hot device is placed in by treated dense hydrothermal solution or by treated cleaning hot vapour water, or is distinguished by more than two preheaters
It is placed in that dense hydrothermal solution neutralizes by treated cleaning hot vapour water by treated, is transported in parallel or series between each preheater
Row.
Above-mentioned any heating power water process and the circulatory system, alternative technology scheme are the carbonated drink conveyings
The heat dump of the heat power positive displacement pump of unit is placed in heat source, and radiator is placed in low-temperature receiver, refers to more than two heat dump difference
It is placed in that cleaning hot vapour water neutralizes by treated dense hydrothermal solution and one assisted heating device of serial or parallel connection by treated,
It is run in parallel or series between each heat dump, radiator is placed in transported accessing pending water solution, and the preheater is placed in heat
Refer to that more than two preheaters are respectively placed in that dense hydrothermal solution neutralizes by treated cleaning hot vapour water by treated in source,
It is run in parallel or series between each preheater.
A kind of above-mentioned heating power water process and the circulatory system, improved technical solution are, in main heat source or auxiliary heating dress
It sets and is parallel with heat-storing device.The heat-storing device can heat accumulation, the heat release when outside has compared with low energy when there is strength energy in outside
Supply system is run.
A kind of above-mentioned heating power water process and the circulatory system, improved technical solution are the heat of the carbonated drink supply unit
The heat dump of power positive displacement pump is placed in heat source, and radiator is placed in low-temperature receiver, refers to that heat dump is placed in by treated dense hot water
In solution and an assisted heating device, radiator are placed in a radiation cooling case in parallel or series, and the radiation cooling case is one
Radiation cooling device, the preheater be placed in heat source refer to preheater be placed in by treated cleaning hot vapour water in.
A kind of above-mentioned heating power water process and the circulatory system, improved technical solution are cleaning water outs after treatment
Place's one heat power positive displacement pump of concatenation.The program can be by thermal energy extra in heat source for promoting clean water.
Above-mentioned any heating power water process and the circulatory system, alternative technology scheme are, more in dense hot water
Waste heat energy can be used for heating cold water etc..
Advantageous effect：A kind of heating power water process and the circulatory system of the present invention, due to using accessing pending water solution or other
Low temperature environment as source of heat release, using in treated concentrated water hot solution or treated cleaning hot vapour water thermal energy or add one auxiliary
It helps heating device as the heat dynamic resource of heat power positive displacement pump, the latent heat in water treatment procedure is not only utilized, reduces a high position
The consumption of the energy, and the efficiency of water process is also improved, reduce cost of water treatment.It is driven especially suitable for complete regenerative resource
Application under dynamic water process environmental condition reduces the discharge of carbon dioxide, mitigates room temperature effect.
Invention is further described in detail with reference to the accompanying drawings and detailed description.
Description of the drawings：
Fig. 1 is a kind of solar-powered thermal single-stage distillation seawater desalination and circulatory system schematic diagram of the present invention.
Fig. 2 is a kind of hot water and steam multistage flash distillation sewage disposal and the circulatory system schematic diagram of the present invention.
Fig. 3 is a kind of dehumidifying sea water desalination of humidification and the circulatory system schematic diagram of the present invention.
Fig. 4 is single-effective absorption sea water desalination and the cyclic system of a kind of solar energy and biomass energy cooperation of the present invention
System schematic diagram.
Fig. 5 is that a kind of absorption type sea water desalination of the solar energy and biomass energy cooperation of the present invention and the circulatory system are shown
It is intended to.
Fig. 6 is a kind of integrated solar distillation type sea water desalination and the circulatory system schematic diagram of the present invention.
Specific implementation mode
Embodiment 1：Fig. 1 is a kind of solar-powered thermal single-stage distillation seawater desalination and circulatory system schematic diagram of the present invention.
The system is made of heating power distillation unit, carbonated drink supply unit, the heating power distillation unit by main heat source solar thermal collector A1,
The compositions such as thermal storage device A2, distiller A3, condenser A4, pipe valve, thermal storage device A2 are connected in parallel on main heat source solar thermal collector A1.Vapour
Water supply unit is a heat power positive displacement pump, and the heat power positive displacement pump is by heat dump B1, solar auxiliary heater B2, main gas
Dynamic positive displacement pump B3, pneumatic working medium circulation booster pump B4, radiator B5, the pneumatic positive displacement pump B7 of auxiliary, working medium circulation pipe valve and its interior
Cryogenic fluid R600a, carbonated drink pipe valve composition, solar auxiliary heater B2 is connected in parallel on heat dump B1.Heat power positive displacement pump
Heat dump B1 be placed in condenser A4, radiator B5 is passed through quasi- by processing seawater, and the sender property outlet b1 of heat dump B1 is through pipe valve
Be connected to the working medium import b2 of the pneumatic positive displacement pump B3 of master, the working medium of the sender property outlet b3 and radiator B5 of main pneumatic positive displacement pump B3 into
Mouth b5 connections, the sender property outlet b6 of radiator B5 are connected to the inlet b7 of pneumatic working medium circulation booster pump B4, and pneumatic working medium is followed
The working medium import b9 of the liquid outlet b8 and heat dump B1 of ring booster pump B4 are connected to, the working medium import of pneumatic working medium circulation booster pump B4
B10 and sender property outlet b11 is connected in parallel on the working medium import b2 and sender property outlet b3 of main pneumatic positive displacement pump B3, assists pneumatic positive displacement pump
The working medium import b16 and sender property outlet b17 of B7 is connected in parallel on the working medium import b2 and sender property outlet b3 of main pneumatic positive displacement pump B3, main
The water inlet b12 of pneumatic positive displacement pump B3 is connected to pending seawater water source, the water outlet b13 and radiator of main pneumatic positive displacement pump B3
The water inlet b14 connection of B5, the water outlet b15 of radiator B5 is first after preheated device A5 again with main heat source solar thermal collector A1's
Inlet a1 connections, the liquid outlet a2 of main heat source solar thermal collector A1 are connected to the spray head a3 of distiller A3 by pipe valve
On, the steam outlet a4 of distiller A3 is connected to by pipe valve with the inlet b18 of pneumatic positive displacement pump B7 is assisted, and pneumatic hold is assisted
The liquid outlet b19 of product pump B7 is connected to by pipeline with the water vapour import b20 of condenser A4.Heat dump B1 and condenser A4 can be with
It is integrated heat-exchanger.
System operation is：When having sunlight, in solar thermal collector A1 in carbonated drink and solar auxiliary heater B2
Cryogenic fluid R600a is heated simultaneously, main pneumatic positive displacement pump B3, pneumatic working medium circulation booster pump B4, the pneumatic positive displacement pump B7 of auxiliary
It is activated first, main pneumatic positive displacement pump B3 conveys seawater to be diluted into radiator B5, is sent into too after the preheated device A5 preheatings of seawater
Positive energy heat collector A1 continues to heat, and the seawater after heating enters the spray head a3 spray vaporizations in distiller A3, and the water of vaporization steams
Gas is assisted pneumatic positive displacement pump B7 to take away, and spray vaporizes the heavy bottom for staying in distiller A3 of remaining dense hot salt brine, latent heat quilt
Low temperature seawater in preheater A5 absorbs, and dense hypothermic saline is discharged by the road；The vapor for being assisted pneumatic positive displacement pump B7 to take away
It is condensed into the hot fresh water of cleaning into condenser A4, the latent heat cleaned in hot fresh water is absorbed by heat dump B1 and as heat power volume
The heat power of pump, fresh water after cooling are discharged by pipeline.Solar thermal collector A1 may be incorporated into solar auxiliary heater B2
One running body can close solar auxiliary heater B2 after system normal operation, and heat power needed for system circulation pump is come at this time
The latent heat in desalinizing seawater is absorbed derived from heat dump B1.When solar energy abundance on daytime, solar thermal collector A1 absorbs extra
Heat can be stored in thermal storage device A2, be used when night or without sunlight.
Embodiment 2：Fig. 2 is a kind of hot water and steam multistage flash distillation sewage disposal and the circulatory system schematic diagram of the present invention.It should
System is made of heating power distillation unit, carbonated drink supply unit, and the heating power distillation unit is by main heat source heat exchanger A1, distiller
The compositions such as A31, A32, A33, condenser A4, preheater A5, pipe valve, carbonated drink supply unit are a heat power positive displacement pump, the heat
Power positive displacement pump is by heat dump B1, main pneumatic positive displacement pump B3, pneumatic working medium circulation booster pump B4, radiator B5, the pneumatic appearance of auxiliary
Product pump B7, working medium circulation pipe valve and its interior cryogenic fluid R245ca, carbonated drink pipe valve composition.The heat dump B1 of heat power positive displacement pump
It is placed in condenser A4, radiator B5, which is passed through, to be intended by treated sewage, and the sender property outlet b1 of heat dump B1 is through pipe valve and main pneumatic appearance
The working medium import b2 connections of product pump B3, the working medium import b5 of the sender property outlet b3 and radiator B5 of main pneumatic positive displacement pump B3 are connected to,
The sender property outlet b6 of radiator B5 is connected to the inlet b7 of pneumatic working medium circulation booster pump B4, pneumatic working medium circulation booster pump B4
Liquid outlet b8 be connected to the working medium import b9 of heat dump B1, the working medium import b10 and working medium of pneumatic working medium circulation booster pump B4
Outlet b11 is connected in parallel on the working medium import b2 and sender property outlet b3 of main pneumatic positive displacement pump B3, assists the working medium of pneumatic positive displacement pump B7
Import b16 and sender property outlet b17 is connected in parallel on the working medium import b2 and sender property outlet b3 of main pneumatic positive displacement pump B3, distiller A31,
Steam outlet a41, a42, a43 of A32, A33 are connected to by pipe valve with the inlet b18 of pneumatic positive displacement pump B7 is assisted, and are assisted
The liquid outlet b19 of pneumatic positive displacement pump B7 is connected to by pipeline with the water vapour import b20 of condenser A4.Main pneumatic positive displacement pump B3's
Water inlet b12 is connected to pending seawater water source, the water inlet b14 of the water outlet b13 and radiator B5 of main pneumatic positive displacement pump B3
Connection, the water outlet b15 of radiator B5 are first connected to the inlet a5 of distiller A33 after preheated device A5 again, distiller A31,
The sewage preheating pipeline of A32, A33 are sequentially connected in series connection, and the inlet a7 of distiller A31 outlet a6 and main heat source heat exchanger A1 connects
Logical, the hot water inlet a9 of the liquid outlet a8 and distiller A31 of main heat source heat exchanger A1 are connected to, and distiller A31, A32, A33's waits for
The hot plumbing drain of distillation is sequentially connected in series the inlet of access preheater A5 after connection, and treated strong sewage is from preheater A5's
Liquid outlet is discharged.Steam from the import a10 input of main heat source heat exchanger A1, the condensation-water drain a11 of main heat source heat exchanger A1 with
The water inlet b20 that condenser A4 is accessed after the clean water outlet of distiller A31, A32, A33, after heat dump B1 heat absorptions
Water at low temperature is cleaned to be discharged from the water outlet of condenser A4.Heat dump B1 and condenser A4 can be integrated heat-exchanger.
System operation is：Through the heat dump B1 in condenser A4 after main heat source heat exchanger A1 access hot water or steam,
It is the main pneumatic positive displacement pump B3 of cryogenic fluid R245ca heat absorption evaporation driving, pneumatic working medium circulation booster pump B4 in heat dump B1, auxiliary
Pneumatic positive displacement pump B7 is helped to start first, main pneumatic positive displacement pump B3 conveys treatment sewage into radiator B5, the preheated device A5 of seawater
The preheater being sent into distiller A31, A32, A33 after preheating continues to preheat, and the sewage after preheating enters main heat source heat exchanger A1
Heating, the sewage after heating sequentially enter distiller A31, A32, A33 and distill step by step, and the clear hot-water after distillation is by condenser A4
It is discharged after interior heat dump heat absorption.Vapor in distiller is assisted pneumatic positive displacement pump B7 to extract out and is transported to condenser simultaneously
Condensation discharge in A4.
Embodiment 3：Fig. 3 is a kind of humidification dehumidification type sea water desalination and the circulatory system schematic diagram of the present invention.System heat
Power distillation unit is added by main heat source solar thermal collector A1, thermal storage device A2, humidification distiller A3, condenser A4, solar energy auxiliary
The compositions such as hot device B2, heat dump B1, pipe valve.Thermal storage device A2 is connected in parallel on main heat source solar thermal collector A1, and heat dump B1 is in parallel
On heater B2.Carbonated drink supply unit is pressurized by solar auxiliary heater B2, main pneumatic positive displacement pump B3, pneumatic working medium circulation
Pump B4, radiator B5, working medium circulation pipe valve and its interior cryogenic fluid R123, carbonated drink pipe valve composition.Radiator B5 is passed through quasi- quilt
Seawater is handled, the sender property outlet b1 of solar auxiliary heater B2 connects through the working medium import b2 of pipe valve and main pneumatic positive displacement pump B3
Logical, the working medium import b5 of the sender property outlet b3 and radiator B5 of main pneumatic positive displacement pump B3 are connected to, the sender property outlet b6 of radiator B5
It is connected to the inlet b7 of pneumatic working medium circulation booster pump B4, the liquid outlet b8 and solar energy of pneumatic working medium circulation booster pump B4 is auxiliary
The working medium import b9 of heater B2 is helped to be connected to through pipe valve, water inlet b12 and the pending seawater water source of main pneumatic positive displacement pump B3 connect
Logical, the water inlet b14 of the water outlet b13 and radiator B5 of main pneumatic positive displacement pump B3 are connected to, and the water outlet b15 of radiator B5 is first passed through
It is connected to again with the inlet a1 of main heat source solar thermal collector A1 after preheater A5, condenser A4, main heat source solar thermal collector
The liquid outlet a2 of A1 is connected to by pipe valve on the spray head a3 of humidification distiller A3, the steam outlet a4 of humidification distiller A3
It is flowed to condenser A4 and is condensed into fresh water and flowed out from fresh water drip tray a5, condensed cold air enters again through cold air outlet a7
In humidifier A3, the strong brine in humidifier A3 after distillation flows into heat dump heat exchange B1 through concentrated water drip tray a6, after absorbing heat
Strong brine is discharged.
System operation is：When having sunlight, in solar thermal collector A1 in carbonated drink and solar auxiliary heater B2
Cryogenic fluid R123 is heated simultaneously, and main pneumatic positive displacement pump B3, pneumatic working medium circulation booster pump B4 are activated first, main pneumatic appearance
Long-pending pump B3 conveys seawater to be diluted and enters preheater B5, is sent into solar thermal collector A1 after the condensed device A4 preheatings of seawater and continues to add
Heat, the seawater after heating enter the spray head a3 spray vaporizations in humidification distiller A3, and the vapor of vaporization is through steam outlet
A4 is flowed out from fresh water drip tray a5 to flowing at preheater A5 and be condensed into fresh water, condensed cold air through cold air outlet a7 again into
Enter in humidifier A3, the strong brine in humidifier A3 after distillation flows into heat absorbing heat exchanger B1 through concentrated water drip tray a6, after absorbing heat
Strong brine discharge.Solar thermal collector A1 and solar auxiliary heater B2 may be incorporated into a running body, when system normal operation
After can close solar auxiliary heater B2, heat power needed for system circulation pump is absorbed from heat dump B1 in concentrated seawater at this time
Latent heat.When solar energy abundance on daytime, the waste heat that solar thermal collector A1 absorbs can be stored in thermal storage device A2, wait for night
Between or when without sunlight use.
Embodiment 4：Fig. 4 is the single-effective absorption sea water desalination of a kind of solar energy and biomass energy cooperation of the present invention
And circulatory system schematic diagram.The system heating power distillation unit is by main heat source solar thermal collector A1, gas-liquid separator C, condenser
The compositions such as A4, solar auxiliary heater B2, D2, heat dump B1, absorber C1, pipe valve, solar auxiliary heater B2, D2 collection
At in main heat source solar thermal collector A1, heat dump B1 is connected in parallel on solar auxiliary heater B2.Carbonated drink supply unit by
Two sets of heat power positive displacement pumps constitute the first carbonated drink supply unit and the second carbonated drink supply unit, and the first carbonated drink supply unit is by the sun
It can auxiliary heater B2, heat dump B1, main pneumatic positive displacement pump B3, pneumatic working medium circulation booster pump B4, radiator B5, working medium circulation
Pipe valve and its interior cryogenic fluid R245cf, carbonated drink pipe valve composition.Second carbonated drink supply unit by solar auxiliary heater D2,
Main pneumatic positive displacement pump D3, pneumatic working medium circulation booster pump D4, radiator D5, working medium circulation pipe valve and its interior cryogenic fluid
R245cf, carbonated drink pipe valve composition.Absorption distillation unit is by main heat source solar thermal collector A1, gas-liquid separator C, condenser
A4, evaporator（Preheater）The compositions such as A5, absorber C1, regenerator C2, biological boiler E, pipe valve.There is metal in absorber C1
Salting liquid LiBr.Each component connection relation of system is as shown in Figure 4.
System operation is：There is when sunlight and puts biomass fired boiler E, solar thermal collector A1, solar energy auxiliary add
Carbonated drink in hot device B2, D2, biomass boiler E and the cryogenic fluid R245cf in solar auxiliary heater B2, D2 simultaneously by
Heating, the pneumatic positive displacement pump B3 of master, pneumatic working medium circulation booster pump B4 and the second carbonated drink supply unit of the first carbonated drink supply unit
The pneumatic positive displacement pump D3 of master, pneumatic working medium circulation booster pump D4 be activated simultaneously, main pneumatic positive displacement pump B3 conveys seawater to be diluted
It is admitted to again in evaporator A5 into radiator B5, the preheated device of seawater（Evaporator）A5 is added by the steam from biological boiler E
After thermal evaporation, steam is admitted to absorber C1, LiBr and absorbs vapor, and the strong brine in evaporator A5 is discharged by pipeline.
Vapor in absorber C1 and the LiBr solution from gas-liquid separator C are sent by the second carbonated drink supply unit through regenerator C2
Solar thermal collector A1 continues to heat, and the seawater after heating enters separation, vapor in vapour liquid separator C and is admitted to condenser A4
It is condensed into fresh water output.
Embodiment 5：Fig. 5 is a kind of absorption type sea water desalination of the solar energy and biomass energy cooperation of the present invention and follows
Loop system schematic diagram.The system heating power distillation unit is by main heat source solar thermal collector A1, adsorbent bed F1, adsorbent bed F2, condensation
The compositions such as device A4, evaporator A5, pipe valve.Carbonated drink supply unit by two sets of heat power positive displacement pumps constitute the first carbonated drink supply unit and
Second carbonated drink supply unit, the first carbonated drink supply unit are increased by biomass boiler E, main pneumatic positive displacement pump B3, pneumatic working medium circulation
Press pump B4, radiator B5, working medium circulation pipe valve and its interior cryogenic fluid R245cf, carbonated drink pipe valve composition.Second carbonated drink conveys
Unit is followed by solar auxiliary heater D2, main pneumatic positive displacement pump D3, pneumatic working medium circulation booster pump D4, radiator D5, working medium
Endless tube valve and its interior cryogenic fluid R245cf, carbonated drink pipe valve composition.Zeolite F is housed in adsorbent bed F1, F2.Each component of system
Connection relation is as shown in Figure 5.
System operation is：There are when sunlight while lighting biological boiler E, solar thermal collector A1, D2, biological boiler E
Cryogenic fluid R245cf in interior water and pipeline is heated simultaneously, the sea in carbonated drink heating evaporation device A5 in biological boiler E
Water, generates steam, and remaining concentrated seawater is discharged through discharge outlet.The pneumatic positive displacement pump B3 of master of first carbonated drink supply unit, pneumatic working medium
The pneumatic positive displacement pump D3 of master, the pneumatic working medium circulation booster pump D4 of circularly-supercharged pump B4 and the second carbonated drink supply unit are opened simultaneously
Dynamic, main pneumatic positive displacement pump B3 conveyings seawater respectively enters the heat exchanger tube of condenser A4, adsorbent bed F2 through radiator B5, D5 and pipe valve
It is interior.The seawater of condensed device A4 heat exchange is admitted to heating in evaporator A5, and the steam generated in evaporator A5 is through pipeline and electromagnetism
Valve 3 enters adsorbent bed F1, is adsorbed there, and solenoid valve 4, solenoid valve 7 are to close at this time.Bed F1 adsorption saturations to be adsorbed it
Afterwards, the second carbonated drink supply unit gives adsorbent bed F1 heating, at this time solenoid valve by the hot water input adsorbent bed F1 in the circulatory system
5 open, and solenoid valve 6 is closed.When saturated steam partial pressure in bed F1 to be adsorbed is more than the partial pressure in condenser A4, solenoid valve
1 opens, and solenoid valve 2 is closed, and is allowed steam to enter in condenser A4 and is condensed, and forms fresh water and is discharged by the road.The latent heat of release is by cold
But water is taken away into evaporator A5.After adsorbent bed F1 is desorbed completely, solenoid valve 5 is closed, stops heating, solenoid valve 7 is beaten
It opens, solenoid valve 8 is closed, and cooling water inputs in the heat exchanger tube of adsorbent bed F1, and adsorbent bed F1 is made to cool down.Water in adsorbent bed F1 at this time
Partial vapour pressure constantly reduces, and when being down to its partial pressure less than steam partial pressure in condenser A4, closes solenoid valve 1, opens electromagnetism
Valve 2, while opens solenoid valve 4 and closing solenoid valve 3.At this moment the vapor for carrying out flash-pot A5 enters adsorbent bed F2 again, entirely
Process repeats described above.
Embodiment 6：Fig. 6 is a kind of integrated solar distillation type sea water desalination and the circulatory system schematic diagram of the present invention.
The system heating power distillation unit is by condensation fresh water collecting device A101, A102, seawater apparatus for placing A201, A202, nanometer heat absorption
Evaporation plate A203, concentrated seawater collection device A701, cold plate 401, capillary wick materials A 501, the compositions such as light transmission device A601.
Heat power positive displacement pump is by heat dump B1, solar auxiliary heater B2, main pneumatic positive displacement pump B3, pneumatic working medium circulation booster pump
B4, radiator B5, preheater A5, working medium circulation pipe valve and its interior cryogenic fluid R600a, carbonated drink pipe valve composition, solar energy are auxiliary
Heater B2 is helped to be connected in parallel on heat dump B1.The heat dump B1 of heat power positive displacement pump is placed in heat exchanger A4.Each component of system
Connection relation is as shown in Figure 6.
System operation is：When having sunlight, the seawater in seawater apparatus for placing A202 and solar auxiliary heater B2
Interior cryogenic fluid R600a is heated simultaneously, and main pneumatic positive displacement pump B3, pneumatic working medium circulation booster pump B4 are activated, main pneumatic
Positive displacement pump B3 conveys seawater to be diluted into radiator B5, and quilt in seawater apparatus for placing A202 is sent into after the preheated device A5 preheatings of seawater
Nanometer heat absorption evaporation plate A203 continues heating evaporation, and the vapor after distillation is cold through light transmission device A601 and cold plate 401 respectively
It congeals into fresh water and flows into fresh water collecting device A101, A102, enter preheater A5 by the road, the fresh water after latent heat is absorbed is defeated
Go out.Seawater after preheating is also delivered in seawater apparatus for placing A201 simultaneously, and entering distillation through capillary wick materials A 501 fills
In setting, capillary wick material bottom is discharged into concentrated seawater into concentrated seawater collection device A701, the bottoms seawater apparatus for placing A201
Concentrated seawater after distillation is discharged into together with the concentrated seawater that concentrated seawater collection device A701 is discharged in heat exchanger A4 by the road,
Low temperature concentrated seawater after latent heat is absorbed by heat dump B1 is discharged.
Although having been combined the system that preferred embodiment describes the present invention, the present invention is not limited to as described herein
Concrete form, on the contrary, its object is to cover naturally fall into the scope of the invention of the claims limited
Various alternatives, remodeling, various characteristic elements recombinant and derivative Combination nova and equivalents.
Claims (10)
1. a kind of heating power water process and the circulatory system are made of heating power distillation unit, carbonated drink supply unit, the heating power distillation is single
Member is made of main heat source, more than one distiller, condenser, pipe valve, and the carbonated drink supply unit is made of pump, pipe valve, waits locating
Reason water, which passes through main heat source after pump flows through main heat source heating or flows through heat exchanger preheating and heats to enter in each distiller, to be distilled, and is steamed
It evaporates the carbonated drink of acquisition and becomes clean water output after conveying condenses, remaining in distiller treated that dope is directly exported or passed through
It is exported after heat exchanger heat absorption, it is characterised in that：The pump of the carbonated drink supply unit is heat power positive displacement pump, the heat power volume
Pump is made of heat dump, main pneumatic positive displacement pump, pneumatic working medium circulation booster pump, radiator, cycle fluid and pipe valve, and the heat is dynamic
The heat dump of power positive displacement pump is placed in main heat source or secondary heat source, and radiator is placed in low-temperature receiver, and the sender property outlet of heat dump is through pipe valve
With the working medium inlet communication of the pneumatic positive displacement pump of master, the working medium inlet communication of the sender property outlet and radiator of main pneumatic positive displacement pump dissipates
The sender property outlet of hot device is connected to the inlet of pneumatic working medium circulation booster pump, the liquid outlet of pneumatic working medium circulation booster pump and suction
The working medium inlet communication of hot device, the working medium import of pneumatic working medium circulation booster pump and sender property outlet are connected in parallel on main pneumatic positive displacement pump
In working medium import and sender property outlet, the water inlet of main pneumatic positive displacement pump is connected to pending water source, the water outlet of main pneumatic positive displacement pump
Mouthful be connected to radiator, after the water outlet of radiator and the preheated device of the inlet of main heat source or elder generation again with the inlet of main heat source
Connection, preheater are placed in time heat source, the secondary heat source refers to that treated dense hydrothermal solution or treated cleaning hot vapour water
Or assisted heating device or the heat source that is formed by above-mentioned three's connection in series-parallel, the main heat source is by a kind of main heating power source or by two
Kind or more main heating power subject string parallel running constitute.
2. a kind of heating power water process according to claim 1 and the circulatory system, it is characterised in that：In distiller, treated
The one pneumatic positive displacement pump of auxiliary of concatenation, the working medium import of the pneumatic positive displacement pump of the auxiliary and sender property outlet are in parallel on vapor output pipe
In the working medium import and sender property outlet of the pneumatic positive displacement pump of master.
3. a kind of heating power water process according to claim 1 and the circulatory system, it is characterised in that：On the pneumatic positive displacement pump of master
The pneumatic positive displacement pump of a thermal energy balance in parallel, the working medium import of the pneumatic positive displacement pump of the thermal energy balance and sender property outlet are connected in parallel on main pneumatic
In the working medium import of positive displacement pump and sender property outlet.
4. a kind of heating power water process according to claim 1,2,3 and the circulatory system, it is characterised in that：The carbonated drink conveying
The heat dump of the heat power positive displacement pump of unit is placed in heat source, and radiator is placed in low-temperature receiver, refers to after heat dump is placed in and is handled
Dense hydrothermal solution in and an assisted heating device, radiator are placed in transported accessing pending water solution in parallel or series, institute
Stating preheater and being placed in heat source refers to that preheater is placed in by treated cleaning hot vapour water.
5. a kind of heating power water process according to claim 1,2,3 and the circulatory system, it is characterised in that：The carbonated drink conveying
The heat dump of the heat power positive displacement pump of unit is placed in heat source, and radiator is placed in low-temperature receiver, refers to after heat dump is placed in and is handled
Cleaning hot vapour water in and an assisted heating device, radiator are placed in transported accessing pending water solution in parallel or series, institute
Stating preheater and being placed in heat source refers to that preheater is placed in by treated dense hydrothermal solution.
6. a kind of heating power water process according to claim 1,2,3 and the circulatory system, it is characterised in that：The carbonated drink conveying
The heat dump of the heat power positive displacement pump of unit is placed in heat source, and radiator is placed in low-temperature receiver, refers to that heat dump is placed in solar energy collection
In hot device, radiator is placed in transported accessing pending water solution, the preheater be placed in heat source refer to preheater be placed in by
In treated dense hydrothermal solution or it is placed in by treated clear hot-water.
7. a kind of heating power water process according to claim 1,2,3 and the circulatory system, it is characterised in that：The carbonated drink conveying
The heat dump of the heat power positive displacement pump of unit is placed in heat source, and radiator is placed in low-temperature receiver, refers to that heat dump is placed in boiler or pot
In the hot vapour water of stove waste heat, radiator is placed in transported accessing pending water solution, and it refers to pre- that the preheater, which is placed in heat source,
Hot device is placed in by treated dense hydrothermal solution or by treated cleaning hot vapour water.
8. a kind of heating power water process according to claim 1,2,3 and the circulatory system, it is characterised in that：The carbonated drink conveying
The heat dump of the heat power positive displacement pump of unit is placed in heat source, and radiator is placed in low-temperature receiver, refers to more than two heat dump difference
It is placed in that cleaning hot vapour water neutralizes by treated a dense hydrothermal solution and in parallel or series assisted heating device by treated,
It is run in parallel or series between each heat dump, radiator is placed in transported accessing pending water solution, and the preheater is placed in heat
Refer to that more than two preheaters are respectively placed in that dense hydrothermal solution neutralizes by treated cleaning hot vapour water by treated in source,
It is run in parallel or series between each preheater.
9. a kind of heating power water process according to claim 1,2,3 and the circulatory system, it is characterised in that：In main heat source or auxiliary
It helps and is parallel with heat-storing device on heating device.
10. a kind of heating power water process according to claim 1,2,3 and the circulatory system, it is characterised in that：The carbonated drink is defeated
The heat dump of the heat power positive displacement pump of unit is sent to be placed in heat source, radiator is placed in low-temperature receiver, refers to that heat dump is placed in and is handled
In dense hydrothermal solution afterwards and an assisted heating device, radiator are placed in a radiation cooling case in parallel or series, the preheating
Device be placed in heat source refer to preheater be placed in by treated cleaning hot vapour water in.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810668119.4A CN108516602A (en) | 2018-06-26 | 2018-06-26 | A kind of heating power water process and the circulatory system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810668119.4A CN108516602A (en) | 2018-06-26 | 2018-06-26 | A kind of heating power water process and the circulatory system |
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| Country | Link |
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2018
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