CN104418396B - A kind of desalinization or effluent treatment plant - Google Patents
A kind of desalinization or effluent treatment plant Download PDFInfo
- Publication number
- CN104418396B CN104418396B CN201310374882.3A CN201310374882A CN104418396B CN 104418396 B CN104418396 B CN 104418396B CN 201310374882 A CN201310374882 A CN 201310374882A CN 104418396 B CN104418396 B CN 104418396B
- Authority
- CN
- China
- Prior art keywords
- hot cell
- water pipe
- preheating
- preheating chamber
- condensation
- 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
Links
Classifications
-
- 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
-
- 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
- C02F1/048—Purification of waste water by evaporation
-
- 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
-
- 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
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Abstract
Disclosure one desalinization or effluent treatment plant, in the condensation preheating chamber of this device, consecutive intervals is equipped with multiple dress water pipe, the top open design of each dress water pipe, and each dress water pipe is interconnected to be formed linker in bottom, the two ends of linker are connected to preheating pond by water pipe and add hot cell；Described condensation preheating chamber is also associated with the drip pipe that a part is built in preheating pond, and adds hot cell by a jet chimney connection；Described preheating pond introduces former water by a filler pipe；Described adding, is provided with heat power supply device in hot cell.Described preheating pond and add hot cell and be provided with sewage draining exit.Desalinization of the present invention or effluent treatment plant distillation power consumption are minimum, and good purification, can reach the effect directly drunk；And equipment investment is little, it is convenient to build, it is possible to be the miniaturization equipment of family, it is also possible to factory, the maximization in city, production in enormous quantities.
Description
Technical field
The present invention relates to water treatment field, refer in particular to a kind of device utilizing distillation technique means to carry out water process, this water treatment facilities is particularly well-suited to the process of desalinization, sewage purification.
Background technology
Existing desalinization, sewage purification treatment technology can not be widely used because processing cost is high, and water base produced can not directly be drunk.As passed through the mode of simple distillation, per kilogram water is warmed up to 100 DEG C of power consumptions from 0 DEG C and is about 100 kilocalories, the water that per kilogram is 100 DEG C changes into the steam of 100 DEG C and then needs power consumption about 600 kilocalories, generally distillation per kilogram water about consumes energy 700 kilocalories, power consumption is big, the heat of vaporization of water can not be recycled again, and is difficult by solar energy.
Summary of the invention
For prior art Problems existing, the present invention provides desalinization or the effluent treatment plant of a kind of simple in construction.The distillation power consumption of this device is minimum, and good purification, can reach the effect directly drunk；And equipment investment is little, it is convenient to build, it is possible to be the miniaturization equipment of family, it is also possible to factory, the maximization in city, production in enormous quantities.
For achieving the above object, technical solution of the present invention is:
A kind of desalinization or effluent treatment plant, this device is provided with condensation preheating chamber, in this condensation preheating chamber, consecutive intervals is equipped with multiple dress water pipe, the top open design of each dress water pipe, and each dress water pipe is interconnected to be formed linker in bottom, the two ends of linker are connected to preheating pond by water pipe and add hot cell；Described condensation preheating chamber is also associated with the drip pipe that a part is built in preheating pond, and adds hot cell by a jet chimney connection；Described preheating pond introduces former water by a filler pipe；Described adding, is provided with heat power supply device in hot cell.
Further, described condensation preheating chamber can pass through multiple water pipes and connects accordingly with multiple jet chimneys and multiple add hot cell.
Further, described preheating pond and add hot cell and be provided with sewage draining exit.
Further, connect and the water pipe in condensation preheating chamber and preheating pond is equiped with water pump.
Further, connection condensation preheating chamber is equiped with air valve with adding on the jet chimney in hot cell.
Having the beneficial effect that of technique scheme
Former water in preheating pond first condensed water pipe preheats, then pumps into the dress water pipe that in condensation preheating chamber, heat conductivility is good, the heating further of steam and partly evaporation in condensed preheating chamber.The steam of condensation preheating chamber evaporation and add and be condensed into water after the steam that hot cell enters carries out heat exchange with the water in dress water pipe and discharge from drip pipe, and discharge after preheated pond heat exchange cooling and collect.Remain in preheating pond or add the concentrate in hot cell and precipitate is discharged by sewage draining exit periodic cleaning.The per kilogram water power consumption distilled by apparatus of the present invention can be low to moderate less than 50 kilocalories, and distillation power consumption is minimum, and good purification, can reach the effect directly drunk.
Accompanying drawing explanation
Accompanying drawing described herein is used for providing a further understanding of the present invention, constitutes the part of the present invention, and the schematic description and description of the present invention is used for explaining the present invention, is not intended that inappropriate limitation of the present invention.In the accompanying drawings:
Fig. 1 is the structural representation flow direction of steam or condensed water (arrow in figure be) of desalinization of the present invention or effluent treatment plant.
Detailed description of the invention
In order to make the technical problem to be solved, technical scheme and beneficial effect clearly, understand, below in conjunction with drawings and Examples, the present invention is further elaborated.Should be appreciated that specific embodiment described herein is only in order to explain the present invention, is not intended to limit the present invention.
A kind of desalinization as shown in Figure 1 or effluent treatment plant, this device is provided with a condensation preheating chamber 10, and preheats pond 30 and more than one add hot cell 20.
In described condensation preheating chamber 10, consecutive intervals is equipped with multiple dress water pipe 11, the standpipe that described dress water pipe 11 is that heat conductivility is good, is vertically arranged.The top open design of each dress water pipe 11, and each dress water pipe 11 is interconnected to form linker in bottom.
One end of described linker, by water pipe I connection preheating pond 30, this water pipe I is equiped with water pump 40；The other end of described linker adds hot cell by water pipe II connection, and is equiped with water valve 50 on this water pipe II.
Described condensation preheating chamber 10 is also associated with the drip pipe 70 that a part is built in preheating pond 30, and this drip pipe 70 extends outside preheating pond 30.Described condensation preheating chamber 10 adds hot cell 20 by jet chimney 22 connection, and is equiped with an air valve 60 on this jet chimney 22.Best, described condensation preheating chamber 10 can pass through multiple water pipes and connect accordingly with multiple jet chimneys and multiple add hot cell 20.
Described preheating pond 30 introduces former water by a filler pipe 31.
Described adding, is provided with heat power supply device 21 in hot cell 20, heat power supply device 21 must be in addition to outside clean water steam can not have other gas to enter the heat power supply device adding hot cell.Described heat power supply device can use the firing equipments such as solar energy heating, electrical heating, radiant heat transfer, steam heating, indirect heat conducting.Heat power supply device can be single device, it is also possible to be the device that mixes with other heater of solar heat collector.The jet chimney 22 communicated with condensation preheating chamber 10 is arranged on the top or sidepiece that add hot cell 20.
Described preheating pond 30 and the bottom adding hot cell 20 are provided with sewage draining exit 32,23.
During work, it is necessary to the former water of distil(l) injects in preheating pond 30 by filler pipe 31, given the former water preheating in pond by condensate pipe 70.
Preheated former water injects in the linker of condensation preheating chamber 10 by water pump 40, in the dress water pipe 11 that heat conductivility to be distributed to each connection is good, and the heating further being subject in condensation preheating chamber 10 steam and part evaporation.The steam of condensation preheating chamber 10 evaporation and add and be condensed into water after the steam that hot cell 20 enters carries out heat exchange with the water in dress water pipe 11 and discharge from drip pipe 70.
The former water that condensed preheating chamber 10 heats further intermittently enters one or more adding in hot cell 20 through one or more water pipe II and water valve 50.
Adding in hot cell 20, the heating of the heated device 31 of former water and evaporate, when adding the pressure in hot cell 20 more than or equal to the pressure condensed in preheating chamber 10, steam seriality or intermittence are entered condensation preheating chamber 10 by adjusting air valve 60, collect then through discharging from distillation floss hole 71 after the heat exchange cooling of preheating pond 30 after condensing, namely distilled.Remain in preheating pond 30 or add the concentrate in hot cell 20 and precipitate and discharged by sewage draining exit 32,23 periodic cleaning.
The condensation preheating chamber 10 of the present invention and add hot cell 20 preferably pressure vessel, when pressure is more high, heat exchange is more fast, condenses more fast, and yield is more big.
Described above illustrate and describes the preferred embodiments of the present invention, as previously mentioned, it is to be understood that the present invention is not limited to form disclosed herein, it is not to be taken as the eliminating to other embodiments, and can be used for other combinations various, amendment and environment, and in invention contemplated scope described herein, can be modified by the technology of above-mentioned instruction or association area or knowledge.And the change that those skilled in the art carry out and change are without departing from the spirit and scope of the present invention, then all should in the protection domain of claims of the present invention.
Claims (1)
1. a desalinization or effluent treatment plant, it is characterized in that: this device is provided with condensation preheating chamber, in this condensation preheating chamber, consecutive intervals is equipped with multiple dress water pipe, the top open design of each dress water pipe, and each dress water pipe is interconnected to be formed linker in bottom, the two ends of linker are connected to preheating pond by water pipe and add hot cell；Described condensation preheating chamber is also associated with the drip pipe that a part is built in preheating pond, and adds hot cell by a jet chimney connection；Described preheating pond introduces former water by a filler pipe；Described adding, is provided with heat power supply device in hot cell；Described condensation preheating chamber and to add hot cell be pressure vessel, connection condensation preheating chamber and add and be equiped with air valve on the jet chimney in hot cell；Described condensation preheating chamber is connected accordingly with multiple jet chimneys by multiple water pipes and multiple adds hot cell；Described preheating pond and add hot cell and be provided with sewage draining exit；Connect and the water pipe in condensation preheating chamber and preheating pond is equiped with water pump.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310374882.3A CN104418396B (en) | 2013-08-24 | 2013-08-24 | A kind of desalinization or effluent treatment plant |
| PCT/CN2013/082948 WO2015027530A1 (en) | 2013-08-24 | 2013-09-04 | Seawater desalination or sewage purification device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310374882.3A CN104418396B (en) | 2013-08-24 | 2013-08-24 | A kind of desalinization or effluent treatment plant |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104418396A CN104418396A (en) | 2015-03-18 |
| CN104418396B true CN104418396B (en) | 2016-07-06 |
Family
ID=52585457
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310374882.3A Expired - Fee Related CN104418396B (en) | 2013-08-24 | 2013-08-24 | A kind of desalinization or effluent treatment plant |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN104418396B (en) |
| WO (1) | WO2015027530A1 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105731567A (en) * | 2016-02-17 | 2016-07-06 | 浙江德润重工机械有限公司 | Water treatment evaporator |
| CN114380445A (en) * | 2022-01-13 | 2022-04-22 | 河南省三门峡水文水资源勘测局 | Landfill leachate treatment facility |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1539748A (en) * | 2003-10-31 | 2004-10-27 | 刘金成 | Technique for recycling waste fluid containing urea |
| CN2795191Y (en) * | 2005-03-21 | 2006-07-12 | 山东香驰豆业蛋白科技有限公司 | Soy bean separating protein whey concentrating and recovery device |
| CN1803673A (en) * | 2005-12-13 | 2006-07-19 | 梁嘉麟 | On water seawater desalination system with natural resources(cold energy and heat energy) being fully utilized |
| CN101052447A (en) * | 2004-08-23 | 2007-10-10 | 李种华 | Multiple tube rotary evaporator device possessing movable ball |
| CN101337700A (en) * | 2007-07-03 | 2009-01-07 | 天津宝成机械集团有限公司 | Desalination plant using residual heat of thermal superconductivity of heat pipe and engine high-temperature exhaust air |
| CN201592997U (en) * | 2009-12-11 | 2010-09-29 | 王心亮 | Engine exhaust residual heat heating counter-flow preheating type sea water desalinization device |
| CN201634462U (en) * | 2009-09-15 | 2010-11-17 | 江苏大学 | Seawater desalting device |
| CN202410197U (en) * | 2011-12-29 | 2012-09-05 | 河北崇阳环保科技有限公司 | Direct heat replenishing type evaporating device |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06320140A (en) * | 1993-05-06 | 1994-11-22 | Yoshiaki Kouchi | Vacuum distilling plant for water |
| JPH10263301A (en) * | 1997-03-25 | 1998-10-06 | Osaka Gas Co Ltd | Liquid thickening |
| AT507297B1 (en) * | 2008-12-03 | 2010-04-15 | Fh Ooe Forschungs & Entwicklun | SOLAR CONDENSATION SYSTEM WITH CASCADE EVAPORATION |
-
2013
- 2013-08-24 CN CN201310374882.3A patent/CN104418396B/en not_active Expired - Fee Related
- 2013-09-04 WO PCT/CN2013/082948 patent/WO2015027530A1/en active Application Filing
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1539748A (en) * | 2003-10-31 | 2004-10-27 | 刘金成 | Technique for recycling waste fluid containing urea |
| CN101052447A (en) * | 2004-08-23 | 2007-10-10 | 李种华 | Multiple tube rotary evaporator device possessing movable ball |
| CN2795191Y (en) * | 2005-03-21 | 2006-07-12 | 山东香驰豆业蛋白科技有限公司 | Soy bean separating protein whey concentrating and recovery device |
| CN1803673A (en) * | 2005-12-13 | 2006-07-19 | 梁嘉麟 | On water seawater desalination system with natural resources(cold energy and heat energy) being fully utilized |
| CN101337700A (en) * | 2007-07-03 | 2009-01-07 | 天津宝成机械集团有限公司 | Desalination plant using residual heat of thermal superconductivity of heat pipe and engine high-temperature exhaust air |
| CN201634462U (en) * | 2009-09-15 | 2010-11-17 | 江苏大学 | Seawater desalting device |
| CN201592997U (en) * | 2009-12-11 | 2010-09-29 | 王心亮 | Engine exhaust residual heat heating counter-flow preheating type sea water desalinization device |
| CN202410197U (en) * | 2011-12-29 | 2012-09-05 | 河北崇阳环保科技有限公司 | Direct heat replenishing type evaporating device |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2015027530A1 (en) | 2015-03-05 |
| CN104418396A (en) | 2015-03-18 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101481154B (en) | Method and apparatus for seawater desalination by comprehensive utilization of solar energy | |
| CN102381796B (en) | Solar photovoltaic photothermal integrated device for seawater desalination | |
| CN102557176B (en) | Sea water desalinating device of cooling tower of coastal and island thermal power plants | |
| CN104418396B (en) | A kind of desalinization or effluent treatment plant | |
| CN106186200A (en) | A kind of indirect air cooling unit recuperation of heat and water treatment facilities and method | |
| CN101985368A (en) | Condenser type seawater desalting device with steam turbine generator unit | |
| CN102329035A (en) | Fresh water collecting and supplying system | |
| WO2011157060A1 (en) | Device and method for treating water | |
| CN204404134U (en) | Pure steam generator | |
| CN204656030U (en) | A kind of liquid distillation equipment | |
| CN201882942U (en) | Power-generation turboset condenser type sea water desalinating unit | |
| CN102794030B (en) | Multipurpose spray explosion-type high-pressure temperature-adjustment vapor decomposition drying steam generator | |
| CN106365233A (en) | Solar-powered seawater desalination power generation device for ship | |
| CN206033294U (en) | Seawater desalination processing apparatus of power plant | |
| RU2303145C1 (en) | Thermal power station | |
| CN210736251U (en) | Carrier gas extraction HPE evaporation system | |
| CN104925885A (en) | Electromagnetic desalination device | |
| CN106517395A (en) | Circular light and heat concentration salt water and fresh water separator | |
| CN106219855A (en) | Direct Air-cooled Unit recuperation of heat and water treatment facilities and recuperation of heat and method for treating water | |
| CN106186132A (en) | Low cost power plant zeroth order value waste water evaporation and concentration processing system and method | |
| CN202968163U (en) | Injection water preparation device capable of on-line sterilization of raw material water tank | |
| CN207455171U (en) | A kind of air compressor machine atmospheric heat recycling is for liquid chlorine circulating vaporization system | |
| CN201353435Y (en) | Single-effect evaporation device with mechanical fan as evaporation driving force | |
| CN201144161Y (en) | Solar energy ring-effect water purifying system | |
| RO127229B1 (en) | Solar still with heat recovery device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PP01 | Preservation of patent right | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20170807 Granted publication date: 20160706 |
|
| PD01 | Discharge of preservation of patent | ||
| PD01 | Discharge of preservation of patent |
Date of cancellation: 20191011 Granted publication date: 20160706 |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160706 Termination date: 20200824 |