CN104418396A - Seawater desalination or sewage purification device - Google Patents
Seawater desalination or sewage purification device Download PDFInfo
- Publication number
- CN104418396A CN104418396A CN201310374882.3A CN201310374882A CN104418396A CN 104418396 A CN104418396 A CN 104418396A CN 201310374882 A CN201310374882 A CN 201310374882A CN 104418396 A CN104418396 A CN 104418396A
- Authority
- CN
- China
- Prior art keywords
- pipe
- preheating
- chamber
- water
- heating chamber
- 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.)
- Granted
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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
-
- 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
- C02F1/048—Purification of waste water by evaporation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
-
- 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
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The invention discloses a seawater desalination or sewage purification device, a condensation preheating chamber of the device is continuously internally vertically provided with a plurality of water containing pipes in intervals, each water containing pipe is designed with an opening at the top, the bottoms of the water containing pipes are communicated with each other to form a communicating vessel, both ends of the communicating vessel are respectively connected with a preheating water tank and a heating chamber; the condensation preheating chamber is also connected with a condensed water discharge pipe, a part of the condensed water discharge pipe is arranged in the preheating water tank, and the condensation preheating chamber is communicated with the heating chamber by a steam pipeline; raw water is introduced into the preheating water tank by a water feeding pipe, and the heating chamber is provided with a heat source device. The preheating water tank and the heating chamber are provided with a sewage outfall. The seawater desalination or sewage purification device is minimum in distillation energy consumption, good in purification effect, small in equipment investment and convenient in construction, can be used as household miniaturized equipment, also can be used in plant and urban large-scale and mass production.
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 treatment, this water treatment device is specially adapted to the process of sea water desaltination, sewage purification.
Background technology
The treatment technology of existing sea water desaltination, sewage purification can not be widely used because tooling cost is high, and water base that produces can not directly be drunk.As the mode by 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 vapour that the water that per kilogram is 100 DEG C changes into 100 DEG C then needs power consumption about 600 kilocalories, usual distillation per kilogram water about consumes energy 700 kilocalories, power consumption is large, the vaporization heat of water can not be recycled again, and is difficult to utilize sun power.
Summary of the invention
For prior art Problems existing, the invention provides the simple sea water desaltination of a kind of structure or effluent treatment plant.This device distillation power consumption is minimum, and good purification, the effect of directly drinking can be reached; And facility investment is little, it is convenient to build, and can be the miniaturization equipment of family, also can factory, the maximization in city, production in enormous quantities.
For achieving the above object, technical solution of the present invention is:
A kind of sea water desaltination 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 form communicating vessels in bottom, the two ends of communicating vessels are connected to preheating pond and heating chamber by water pipe; Described condensation preheating chamber is also connected with a part and is built in drip pipe in preheating pond, and is communicated with heating chamber by a steam-pipe; Former water is introduced by a filler pipe in described preheating pond; Heat power supply device is provided with in described heating chamber.
Further, described condensation preheating chamber is communicated with multiple heating chambers by multiple water pipe is corresponding with multiple steam-pipe.
Further, described preheating pond and heating chamber are provided with sewage draining exit.
Further, the water pipe connecting condensation preheating chamber and preheating pond is equiped with water pump.
Further, the steam-pipe being communicated with condensation preheating chamber and heating chamber is equiped with air valve.
The usefulness of technique scheme is:
Former water in preheating pond first through condensate pipe preheating, then pumps into the good dress water pipe of heat conductivility in condensation preheating chamber, the further heating of steam and partly evaporation in condensation preheating chamber.Be condensed into water after the steam that the steam of condensation preheating chamber evaporation and heating chamber enter and the water in dress water pipe carry out heat exchange to discharge from drip pipe, and discharge is collected after preheating pond heat exchange cooling.The enriched material and the throw out that remain in preheating pond or heating chamber are discharged by sewage draining exit periodic cleaning.The per kilogram water power consumption of being 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, the effect of directly drinking can be reached.
Accompanying drawing explanation
Accompanying drawing described herein is used to provide a further understanding of the present invention, forms a part of the present invention, and schematic description and description of the present invention, for explaining the present invention, does not form inappropriate limitation of the present invention.In the accompanying drawings:
Fig. 1 is the structural representation (arrow in figure is the flow direction of steam or water of condensation) of sea water desaltination of the present invention or effluent treatment plant.
Embodiment
In order to make technical problem to be solved by this invention, 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 only in order to explain the present invention, be not intended to limit the present invention.
A kind of sea water desaltination as shown in Figure 1 or effluent treatment plant, this device is provided with condensation preheating chamber 10, preheating pond 30 and a more than one heating chamber 20.
In described condensation preheating chamber 10, consecutive intervals is equipped with multiple dress water pipe 11, and described dress water pipe 11 is heat conductivility standpipe that is good, that vertically arrange.The top open design of each dress water pipe 11, and each dress water pipe 11 is interconnected to form communicating vessels in bottom.
One end of described communicating vessels is communicated with preheating pond 30 by water pipe I, and this water pipe I is equiped with water pump 40; The other end of described communicating vessels is communicated with heating chamber by water pipe II, and is equiped with water valve 50 on this water pipe II.
Described condensation preheating chamber 10 is also connected with a part and is built in drip pipe 70 in preheating pond 30, and this drip pipe 70 extends outside preheating pond 30.Described condensation preheating chamber 10 is communicated with heating chamber 20 by a steam-pipe 22, and is equiped with an air valve 60 on this steam-pipe 22.Best, described condensation preheating chamber 10 is communicated with multiple heating chambers 20 by multiple water pipes is corresponding with multiple steam-pipes.
Former water is introduced by a filler pipe 31 in described preheating pond 30.
Be provided with heat power supply device 21 in described heating chamber 20, heat power supply device 21 must be to have other gas to enter the heat power supply device of heating chamber except clean water steam.Described heat power supply device can use the heating installations such as solar heating, electrically heated, radiative transfer, steam heating, indirect heat conducting.Heat power supply device can be single device, also can be the device that solar heat collector mixes with other heating unit.The steam-pipe 22 communicated with condensation preheating chamber 10 is arranged on top or the sidepiece of heating chamber 20.
The bottom of described preheating pond 30 and heating chamber 20 is provided with sewage draining exit 32,23.
During work, need the former water of distillation purification to inject preheating pond 30 by filler pipe 31, given the former water preheat in pond by condensate pipe 70.
Former water through preheating injects in the communicating vessels of condensation preheating chamber 10 by water pump 40, to be distributed in the good dress water pipe 11 of each heat conductivility be communicated with, is subject to further heating and the part evaporation of steam in condensation preheating chamber 10.Be condensed into water after the steam that condensation preheating chamber 10 evaporates and the steam that heating chamber 20 enters carry out heat exchange with the water of dress 11 li, water pipe to discharge from drip pipe 70.
The former water heated further through condensation preheating chamber 10 intermittently enters in one or more heating chamber 20 through one or more water pipe II and water valve 50.
In heating chamber 20, former water is subject to the heating of heating unit 31 and evaporates, when pressure in heating chamber 20 is more than or equal to the pressure in condensation preheating chamber 10, steam continuity or intermittence are entered condensation preheating chamber 10 by adjusting air valve 60, discharge from distillation discharge outlet 71 after preheating pond 30 heat exchange cooling again after carrying out condensation and collect, namely distilled.The enriched material and the throw out that remain in preheating pond 30 or heating chamber 20 are discharged by sewage draining exit 32,23 periodic cleaning.
Condensation preheating chamber 10 of the present invention and heating chamber 20 preferably pressurized vessel, when pressure is higher, heat exchange is faster, and condensation is faster, and output is larger.
Above-mentioned explanation illustrate and describes the preferred embodiments of the present invention, as previously mentioned, be to be understood that the present invention is not limited to the form disclosed by this paper, should not regard the eliminating to other embodiments as, and can be used for other combinations various, amendment and environment, and can in invention contemplated scope described herein, changed 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 do not depart from the spirit and scope of the present invention, then all should in the protection domain of claims of the present invention.
Claims (9)
1. a sea water desaltination 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 form communicating vessels in bottom, the two ends of communicating vessels are connected to preheating pond and heating chamber by water pipe; Described condensation preheating chamber is also connected with a part and is built in drip pipe in preheating pond, and is communicated with heating chamber by a steam-pipe; Former water is introduced by a filler pipe in described preheating pond; Heat power supply device is provided with in described heating chamber.
2. a kind of sea water desaltination as claimed in claim 1 or effluent treatment plant, is characterized in that: described condensation preheating chamber is communicated with multiple heating chambers by multiple water pipe is corresponding with multiple steam-pipe.
3. a kind of sea water desaltination as claimed in claim 1 or 2 or effluent treatment plant, is characterized in that: described preheating pond and heating chamber are provided with sewage draining exit.
4. a kind of sea water desaltination as claimed in claim 1 or 2 or effluent treatment plant, is characterized in that: the water pipe in connection condensation preheating chamber and preheating pond is equiped with water pump.
5. a kind of sea water desaltination as claimed in claim 3 or effluent treatment plant, is characterized in that: the water pipe in connection condensation preheating chamber and preheating pond is equiped with water pump.
6. a kind of sea water desaltination as claimed in claim 1 or 2 or effluent treatment plant, is characterized in that: the steam-pipe of connection condensation preheating chamber and heating chamber is equiped with air valve.
7. a kind of sea water desaltination as claimed in claim 3 or effluent treatment plant, is characterized in that: the steam-pipe of connection condensation preheating chamber and heating chamber is equiped with air valve.
8. a kind of sea water desaltination as claimed in claim 4 or effluent treatment plant, is characterized in that: the steam-pipe of connection condensation preheating chamber and heating chamber is equiped with air valve.
9. a kind of sea water desaltination as claimed in claim 5 or effluent treatment plant, is characterized in that: the steam-pipe of connection condensation preheating chamber and heating chamber is equiped with air valve.
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 true CN104418396A (en) | 2015-03-18 |
| CN104418396B 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) |
Cited By (1)
| 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 |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 (11)
| 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 |
| 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 |
| WO2010063633A1 (en) * | 2008-12-03 | 2010-06-10 | FH OÖ FORSCHUNGS & ENTWICKLUNGS GmbH | Solar condensation system with cascade evaporation |
| 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 |
-
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 (11)
| 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 |
| 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 |
| WO2010063633A1 (en) * | 2008-12-03 | 2010-06-10 | FH OÖ FORSCHUNGS & ENTWICKLUNGS GmbH | Solar condensation system with cascade evaporation |
| 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 |
Cited By (1)
| 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 |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104418396B (en) | 2016-07-06 |
| WO2015027530A1 (en) | 2015-03-05 |
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