CN202609970U - Normal-temperature water spontaneous boiling evaporation energy-conversion device - Google Patents

Normal-temperature water spontaneous boiling evaporation energy-conversion device Download PDF

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Publication number
CN202609970U
CN202609970U CN2012202729741U CN201220272974U CN202609970U CN 202609970 U CN202609970 U CN 202609970U CN 2012202729741 U CN2012202729741 U CN 2012202729741U CN 201220272974 U CN201220272974 U CN 201220272974U CN 202609970 U CN202609970 U CN 202609970U
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CN
China
Prior art keywords
water
normal
conversion device
pipe
temperature water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN2012202729741U
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Chinese (zh)
Inventor
蔡晓虎
岳安山
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SHANDONG XINGLONG ENERGY SCIENCE AND TECHNOLOGY Co Ltd
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Individual
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Filing date
Publication date
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Priority to CN2012202729741U priority Critical patent/CN202609970U/en
Priority to PCT/CN2012/085334 priority patent/WO2013185438A1/en
Application granted granted Critical
Publication of CN202609970U publication Critical patent/CN202609970U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/10Vacuum distillation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D5/00Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0033Other features
    • B01D5/0045Vacuum condensation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D5/00Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0057Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
    • B01D5/006Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes with evaporation or distillation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/08Seawater, e.g. for desalination
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
    • C02F2301/06Pressure conditions
    • C02F2301/063Underpressure, vacuum
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/10Energy recovery
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (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)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

The utility model discloses a normal-temperature water spontaneous boiling evaporation energy-conversion device. The normal-temperature water spontaneous boiling evaporation energy-conversion device comprises a negative-pressure evaporator, wherein the bottom of the negative-pressure evaporator is provided with a drain pipe which is provided with a third stop valve, the side wall of the negative-pressure evaporator is provided with a water-conveying pipe which is provided with a first stop valve, the top of the negative-pressure evaporator is connected with a condenser through a U-shaped pipe, the condenser is connected with a hydro-generator group through a three-way pipe which is connected with a vacuum pump through a suction-pipe, and the position of an water outlet of the hydro-generator group is provided with a second stop valve. The normal-temperature water spontaneous boiling evaporation energy-conversion device is low in energy consumption and high in safety. In addition, the normal-temperature water spontaneous boiling evaporation energy-conversion device utilizes kinetic energy of desalted water for electricity-generation, energy consumption can be effectively reduced, and therefore problems exist in the prior art can be resolved.

Description

The spontaneous explosive evaporatoin energy conversion device of normal-temperature water
Technical field
The utility model relates to the spontaneous explosive evaporatoin energy conversion device of a kind of normal-temperature water.
Background technology
The desalination treatment process of existing sea water distiling plant all is that seawater is heated to boiling, makes the fresh water evaporation.But, on the one hand, needing in the heat-processed to consume great amount of heat, energy consumption is higher; On the other hand, there is potential safety hazard in the pyritous seawater, often is prone to the situation that hot water is hurted sb.'s feelings.In addition, the kinetic energy that desalting process produced also can't be recycled, and can only be whitecap expense in vain.
The utility model content
The purpose of the utility model provides the spontaneous explosive evaporatoin energy conversion device of a kind of normal-temperature water, and its energy consumption is low, safe, and the kinetic energy generating that it utilizes the water after the desalination can effectively reduce energy consumption, thereby, can solve the prior art existing problems.
The purpose of the utility model realizes through following technical scheme: the spontaneous explosive evaporatoin energy conversion device of normal-temperature water; Comprise vacuum evaporator; The bottom of vacuum evaporator is provided with water shoot; The 3rd stopping valve is installed on the water shoot, on the sidewall of vacuum evaporator hydraulic pipe is installed, first stopping valve is installed on the hydraulic pipe; The top of vacuum evaporator is connected with condensing surface through the U-shaped pipe, and condensing surface is connected with the hydraulic generator unit through threeway, and threeway is connected with vacuum pump through extraction pipe; The water outlet place of hydraulic generator unit is provided with second stopping valve.
For further realizing the purpose of the utility model; Can also adopt following technical scheme to realize: said condensing surface is a tube exchanger; The coil pipe water-in of condensing surface links to each other with the U-shaped pipe, and the water outlet of coil pipe is connected with threeway, and the sidewall of condensing surface is provided with cold water inlet and cooling water outlet.Said condensing surface is water jet condensing surface.Submersible pump is installed in the lower end of said hydraulic pipe.The advantage of the utility model is: it utilizes negative pressure to reduce the boiling point of seawater, but makes fresh water just explosive evaporatoin at normal temperatures, thereby reaches the effect of sea water desaltination.Simultaneously, the kinetic energy that produces after its fresh water capable of using condenses drives small-sized hydraulic generator unit generating, recyclable part energy.It also has compactness simple for structure, cheap for manufacturing cost and advantages of simple operation.
Description of drawings
Fig. 1 is the structural representation of the spontaneous explosive evaporatoin energy conversion device of the said normal-temperature water of the utility model.
Reference numeral: 1 submersible pump, 2 first stopping valve, 3 hydraulic pipes, 4 vacuum evaporators, 5 cold water inlet 6U shapes are managed 14 water shoots 15 the 3rd stopping valve, 16 condensation ponds, 7 condensing surfaces, 8 cooling water outlets, 9 threeways, 10 second stopping valve, 11 extraction pipes, 12 vacuum pumps, 13 seawater ponds, 17 hydraulic generator units.
Embodiment
The spontaneous explosive evaporatoin energy conversion device of the described normal-temperature water of the utility model comprises vacuum evaporator 4.The bottom of vacuum evaporator 4 is provided with water shoot 14, and the 3rd stopping valve 15 is installed on the water shoot 14.Hydraulic pipe 3 is installed on the sidewall of vacuum evaporator 4, and hydraulic pipe 3 and seawater pond UNICOM are installed first stopping valve 2 on 13 hydraulic pipes 3.The top of vacuum evaporator 4 is connected with condensing surface 7 through U-shaped pipe 6.Condensing surface 7 is connected with hydraulic generator unit 17 through threeway 9, and threeway 9 is connected with vacuum pump 12 through extraction pipe 11.The water outlet place of hydraulic generator unit 17 is provided with second stopping valve 10.
During use, earlier first stopping valve 2, the 3rd stopping valve 15 and second stopping valve 10 are closed, start vacuum pump 12, vacuum pump 12 through extraction pipe 11 with vacuumizing in condensing surface 7, U-shaped pipe 6 and the vacuum evaporator 4; When the negative pressure in the vacuum evaporator 4 reaches set(ting)value, close vacuum pump 12 again, start condensing surface 7; And open first stopping valve 2, the 3rd stopping valve 15 and second stopping valve 10, at this moment, seawater gets in the vacuum evaporator 4; On the one hand, fresh water is evaporated to water vapor, gets in the condensing surface 7 through U-shaped pipe 6; On the other hand, the seawater after cooling concentrates flows out outside the vacuum evaporator 4 through water shoot 14.After water vapors cooling in the entering condensing surface 7 is condensed into water of condensation, through the impeller of threeway 9 impact hydraulic generator units 17, drive the 17 rotation generatings of hydraulic generator unit, last water of condensation warp second stopping valve 10 gets into the 16 interior storages of condensation ponds.
Said condensing surface 7 can be a tube exchanger.The coil pipe water-in of condensing surface 7 links to each other with U-shaped pipe 6, and the water outlet of coil pipe is connected with threeway 9.The sidewall of condensing surface 7 is provided with cold water inlet 5 and cooling water outlet 8.When water vapor passed through the coil pipe of condensing surface 7, cold water was got in the condensing surfaces 7 by cold water inlet 5, behind the heat through coil pipe absorption water vapor, was discharged by cooling water outlet 8.Said condensing surface 7 also can be existing water jet condensing surface.
For guaranteeing the service discharge in vacuum evaporator 4, submersible pump 1 can be installed in the lower end of said hydraulic pipe 3.
The utility model not technology contents of detailed description is known technology.

Claims (4)

1. the spontaneous explosive evaporatoin energy conversion device of normal-temperature water; It is characterized in that: comprise vacuum evaporator (4); The bottom of vacuum evaporator (4) is provided with water shoot (14); Water shoot (14) is gone up the 3rd stopping valve (15) is installed, and hydraulic pipe (3) is installed on the sidewall of vacuum evaporator (4), and hydraulic pipe (3) is gone up first stopping valve (2) is installed; The top of vacuum evaporator (4) is connected with condensing surface (7) through U-shaped pipe (6), and condensing surface (7) is connected with hydraulic generator unit (17) through threeway (9), and threeway (9) is connected with vacuum pump (12) through extraction pipe (11); The water outlet place of hydraulic generator unit (17) is provided with second stopping valve (10).
2. the spontaneous explosive evaporatoin energy conversion device of normal-temperature water according to claim 1; It is characterized in that: said condensing surface (7) is a tube exchanger; The coil pipe water-in of condensing surface (7) links to each other with U-shaped pipe (6); The water outlet of coil pipe is connected with threeway (9), and the sidewall of condensing surface (7) is provided with cold water inlet (5) and cooling water outlet (8).
3. the spontaneous explosive evaporatoin energy conversion device of normal-temperature water according to claim 1 is characterized in that: said condensing surface (7) is water jet condensing surface.
4. the spontaneous explosive evaporatoin energy conversion device of normal-temperature water according to claim 1 is characterized in that: submersible pump (1) is installed in the lower end of said hydraulic pipe (3).
CN2012202729741U 2012-06-11 2012-06-11 Normal-temperature water spontaneous boiling evaporation energy-conversion device Expired - Fee Related CN202609970U (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN2012202729741U CN202609970U (en) 2012-06-11 2012-06-11 Normal-temperature water spontaneous boiling evaporation energy-conversion device
PCT/CN2012/085334 WO2013185438A1 (en) 2012-06-11 2012-11-27 Evaporation-energy conversion device automatically boiling water at room temperature

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2012202729741U CN202609970U (en) 2012-06-11 2012-06-11 Normal-temperature water spontaneous boiling evaporation energy-conversion device

Publications (1)

Publication Number Publication Date
CN202609970U true CN202609970U (en) 2012-12-19

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CN (1) CN202609970U (en)
WO (1) WO2013185438A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107327822A (en) * 2017-07-28 2017-11-07 成都丽雅纤维股份有限公司 One kind plasticizing water heat energy recovering method
CN112125364A (en) * 2020-09-27 2020-12-25 芜湖凯博环保科技股份有限公司 Low-cost seawater desalination device without condenser and evaporator

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110563063A (en) * 2019-09-29 2019-12-13 江苏苏境电力科技有限责任公司 steam wet type self-condensation device and method for desulfurization wastewater zero-discharge system

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1101374A (en) * 1994-01-13 1995-04-12 安徽省粮油科学研究所 Process and apparatus for utilizing negtive pressure secondary steam from oil extracting factory
JP2000325946A (en) * 1999-05-25 2000-11-28 Ebara Corp Device for desalting salt water
CN201263977Y (en) * 2008-05-29 2009-07-01 史文章 Negative-pressure evaporation granulator and negative-pressure evaporation product type self-cleaning toilet
CN101774560B (en) * 2010-03-19 2011-12-28 四川国理锂材料有限公司 Device for preparing lithium dihydrogen phosphate

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107327822A (en) * 2017-07-28 2017-11-07 成都丽雅纤维股份有限公司 One kind plasticizing water heat energy recovering method
CN112125364A (en) * 2020-09-27 2020-12-25 芜湖凯博环保科技股份有限公司 Low-cost seawater desalination device without condenser and evaporator

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Publication number Publication date
WO2013185438A1 (en) 2013-12-19

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Legal Events

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C14 Grant of patent or utility model
GR01 Patent grant
ASS Succession or assignment of patent right

Free format text: FORMER OWNER: YUE ANSHAN

Effective date: 20121212

Owner name: SHANDONG XINGLONG ENERGY TECHNOLOGY CO., LTD.

Free format text: FORMER OWNER: CAI XIAOHU

Effective date: 20121212

C41 Transfer of patent application or patent right or utility model
COR Change of bibliographic data

Free format text: CORRECT: ADDRESS; FROM: 250002 JINAN, SHANDONG PROVINCE TO: 250101 JINAN, SHANDONG PROVINCE

TR01 Transfer of patent right

Effective date of registration: 20121212

Address after: 250101 Shandong city of Ji'nan province high tech Zone Xinyu Road West Century wealth center block D room 521

Patentee after: Shandong Xinglong Energy Science and Technology Co., Ltd.

Address before: 250002 No. 1, building 3, No. 28-1, Shun tillage Road, Shizhong District, Shandong City, Ji'nan province 402

Patentee before: Cai Xiaohu

Patentee before: Yue Anshan

CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20121219

Termination date: 20150611

EXPY Termination of patent right or utility model