CN1654342A - Sea water desalting plant processed deep in sea - Google Patents

Sea water desalting plant processed deep in sea Download PDF

Info

Publication number
CN1654342A
CN1654342A CNA2004100392396A CN200410039239A CN1654342A CN 1654342 A CN1654342 A CN 1654342A CN A2004100392396 A CNA2004100392396 A CN A2004100392396A CN 200410039239 A CN200410039239 A CN 200410039239A CN 1654342 A CN1654342 A CN 1654342A
Authority
CN
China
Prior art keywords
pressure
resistant seal
reverse osmosis
valve
seal device
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.)
Pending
Application number
CNA2004100392396A
Other languages
Chinese (zh)
Inventor
吴光夏
王维娜
钟慧
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.)
Research Center for Eco Environmental Sciences of CAS
Original Assignee
Research Center for Eco Environmental Sciences of CAS
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Research Center for Eco Environmental Sciences of CAS filed Critical Research Center for Eco Environmental Sciences of CAS
Priority to CNA2004100392396A priority Critical patent/CN1654342A/en
Publication of CN1654342A publication Critical patent/CN1654342A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • 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
    • Y02A20/131Reverse-osmosis

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The present invention is one sea water desalting apparatus to desalt sea water on the natural pressure of sea water. Inside one pressure-resisting sealed apparatus, there are reverse osmosis device, pre-treater, sea water circulating pump, desalted water conveying pump, etc. The pressure-resisting sealed apparatus is set below sea level in the depth with sea water pressure higher than osmotic pressure of sea water, so that the pressure of sea water is utilized to produce desalted water on the permeated liquid side of the reverse osmosis device, the desalted water conveying pump pumps the desalted water to sea surface and the sea water circulating pump updates the sea water inside the apparatus.

Description

Carry out the device of sea water desaltination in the seawater depths
Technical field:
The present invention relates to a kind of device that carries out sea water desaltination in the seawater depths.
Background technology:
The semi-permeable membranes that does not allow ion to see through with only allowing water molecules to see through separates salt solution and fresh water, and then fresh water can see through film and be seeped into brine side, reach balance after, the salt solution liquid level of brine side is higher than the fresh water liquid level of dilute side.The pressure reduction that this liquid level difference forms is called osmotic pressure.When the brine side pressurization surpasses osmotic pressure, water molecules can see through semi-permeable membranes from brine side, and this phenomenon is called reverse osmosis.
All reverse osmosis units all are with high-pressure pump brinepump to be arrived reverse osmosis membrane assembly at present, make water see through film with high pressure, make fresh water, will expend a lot of energy like this.
Summary of the invention:
The present invention is put into the seawater depths that pressure that seawater causes is higher than osmotic pressure to reverse osmosis membrane equipment, thereby the water naturally osmotic is crossed semi-permeable membranes.With water-circulating pump the seawater in the membrane module is brought in constant renewal in, with pump the fresh water that penetrates is pumped, this method can be saved energy, is suitable for making on a large scale fresh water.
Description of drawings:
Fig. 1 is a pressure type circulating seawer depths sea water desalinating plant
Fig. 2 is a suction formula circulating seawer depths sea water desalinating plant
Fig. 3 is two circulating seawer depths sea water desalinating plants
Embodiment:
The present invention realizes as follows:
In the seawater depths that surpasses osmotic pressure, place fixing or packaged type pressure-resistant seal device as following 400 meters, sea, as undersea boat, pressure-resistant seal storehouse or build withstand voltage buildings etc. in the seabed.In the pressure-resistant seal device reverse osmosis equipment is housed, an on high-tension side mouth of reverse osmosis equipment connects pretreating device, pretreating device comprises security personnel's strainer, and ultrafiltration apparatus, before pretreating device, connect sea water circulating pump, outlet of circulating pump connects pretreating device, inlet stretches out the pressure-resistant seal device and is tightly connected with the pressure-resistant seal device or the inlet of sea water circulating pump connects pretreating device, outlet connects an on high-tension side mouth of reverse osmosis equipment, and another interface of pretreating device stretches out the pressure-resistant seal device and is tightly connected with the pressure-resistant seal device.On high-tension side another mouthful of reverse osmosis equipment stretches out the pressure-resistant seal device and is tightly connected with the pressure-resistant seal device.Reverse osmosis equipment see through the inlet that the liquid outlet connects transferpump, carry pump outlet to stretch out the pressure-resistant seal device and be tightly connected with the pressure-resistant seal device and expose the sea.
Recycle pump also can not be contained in the interface of the reverse osmosis equipment that pretreating device is housed, and the inlet of pump is contained in another interface of reverse osmosis equipment, and pump outlet stretches out the pressure-resistant seal device and is tightly connected with the sealing pressure-resistant apparatus.
Describe below in conjunction with embodiment.
Embodiment 1
As shown in Figure 1
Pressure-resistant seal device [1] is positioned over following hundreds of rice, sea [8].Reverse osmosis equipment [2] is housed in the pressure-resistant seal device [1], an one high-tension side interface [3] connects pretreating device [6], comprise ultra-filtration equipment and security personnel's strainer in the pretreating device [6], the outlet of another termination recycle pump [9] of pretreating device, the inlet of recycle pump [10] reach outside the pressure-resistant seal device and with the pressure-resistant seal device and are tightly connected.On high-tension side another interface [4] of reverse osmosis unit [2] reaches outside the pressure-resistant seal device and with pressure-resistant seal device [1] and is tightly connected.The liquid outlet [5] that sees through of reverse osmosis unit [2] connects water tank [12], and water tank [11] connects the inlet of transferpump [7], and the sea is stretched out in the outlet of transferpump [6], and is tightly connected with the pressure-resistant seal jar.Seawater pumps into pretreatment unit [6] by recycle pump [9], is entered the high-tension side of reverse osmosis unit [2] and is discharged the pressure-resistant seal device by the outlet [4] of reverse osmosis unit [2] by the inlet [3] of reverse osmosis unit [2].In this process, because the pressure of seawater surpasses osmotic pressure, fresh water sees through reverse osmosis membrane and flows into water tank [11], sends the sea by transferpump [7].Between each parts, all can add valve.
Embodiment 2
As shown in Figure 2.
The inlet of sea water circulating pump [10] is connect the outlet [4] of reverse osmosis unit [2], and it is outer and be tightly connected with pressure-resistant seal device [1] that the outlet of sea water circulating pump reaches the pressure-resistant seal device.Between each parts, all can add valve.Open all valves, start sea water circulating pump [9].Seawater is through the inlet [3] of valve [12], pretreating device [6], reverse osmosis unit [2], the reverse osmosis membrane of flowing through, outlet [4], sea water circulating pump [9], valve [13] by reverse osmosis unit [2] flow out pressure-resistant seal device [1], the fresh water that sees through film is sent the sea through valve [14], water tank [11], valve [15] by transferpump [7].
Embodiment 3
As shown in Figure 3
Reverse osmosis equipment [18], ultrafiltration apparatus [19], sea water circulating pump [20], fresh water Send out pump [21] etc. are housed in the pressure-resistant seal device [17].The inlet of sea water circulating pump [20] connects valve [24], and the other end of valve [24] is joined two pipes together and stretched out pressure-resistant seal device [17], and is tightly connected with pressure-resistant seal device [17].The outlet of sea water circulating pump [20] connects security personnel's strainer [23], a stoste communication port [30] of another termination ultrafiltration apparatus [19] of security personnel's strainers [23], another stoste communication port [31] of ultrafiltration apparatus [19] connects valve [25], and the other end of valve [25] is joined two pipes together and stretched out pressure-resistant seal container [17] and be tightly connected with pressure-resistant seal container [17].The liquid spout [32] that sees through of ultrafiltration apparatus [19] connects valve [27], a high-tension side interface [33] of another termination reverse osmosis equipment of valve [27], another high-tension side interface of reverse osmosis equipment connects valve [26], and the other end of valve [26] is joined two pipes together and stretched out pressure-resistant seal container [17] and be tightly connected with pressure-resistant seal container [17].The liquid spout [36] that sees through of reverse osmosis equipment connects valve [28], another termination receiver [22] of valve [28], another interface of receiver [22] connects valve [29], the inlet of another termination fresh water Send out pump [21] of valve [29], the outlet of fresh water Send out pump [21] connects valve [35], the other end of valve [35] is joined two pipes together and is stretched out pressure-resistant seal container [17] and expose the sea, and is tightly connected with pressure-resistant seal container [17].
All valves are all opened.Start sea water circulating pump [20], seawater is through valve [24], pump [20], security personnel's strainer [23], enter ultrafiltration apparatus feed liquid communication port [30], through the film surface, a part sees through film, a part is flowed out by another feed liquid communication port [31] of ultrafiltration apparatus, discharges pressure-resistant seal device [17] through valve [25].The liquid that sees through of ultrafiltration apparatus sees through the high-tension side interface [33] that liquid mouth [32], valve [27] flow into reverse osmosis equipment through ultrafiltration apparatus, a part sees through reverse osmosis membrane, and another part flows out pressure-resistant seal device [17] through another high-tension side interface [34], the valve [26] of reverse osmosis equipment.Start fresh water transfer pump [21], the liquid that sees through of reverse osmosis equipment being transported to more than the sea through see through the liquid spout [36], valve [28], receiver [22], valve [29], fresh water transfer pump [21], valve [35] of reverse osmosis equipment.

Claims (5)

1, a kind of sea water desalinating plant is characterized in that reverse osmosis membrane equipment is put into the seawater depths that pressure that seawater causes is higher than osmotic pressure, with sea water circulating pump the seawater in the membrane module is brought in constant renewal in, and the fresh water that penetrates with the pump handle pumps.
2, sea water desalinating plant by claim 1 regulation, it is characterized in that in the seawater depths that surpasses osmotic pressure, place fixing or packaged type pressure-resistant seal device, as undersea boat, pressure-resistant seal storehouse or build withstand voltage buildings etc. in the seabed, in the pressure-resistant seal device reverse osmosis equipment is housed, an on high-tension side mouth of reverse osmosis equipment connects pretreating device, pretreating device comprises security personnel's strainer, and ultrafiltration apparatus, before pretreating device, connect sea water circulating pump, outlet of circulating pump connects pretreating device, inlet stretches out the pressure-resistant seal device and is tightly connected with the pressure-resistant seal device or the inlet of sea water circulating pump connects pretreating device, and outlet connects an on high-tension side mouth of reverse osmosis equipment, and another interface of pretreating device stretches out the pressure-resistant seal device and is tightly connected with the pressure-resistant seal device.On high-tension side another mouthful of reverse osmosis equipment stretches out the pressure-resistant seal device and is tightly connected with the pressure-resistant seal device, the liquid that sees through of reverse osmosis equipment exports the inlet that connects transferpump, carry pump outlet to stretch out the pressure-resistant seal device and be tightly connected with the pressure-resistant seal device and expose the sea, recycle pump also can not be contained in the interface of the reverse osmosis equipment that pretreating device is housed, and the inlet of pump is contained in another interface of reverse osmosis equipment, pump outlet stretches out the pressure-resistant seal device and is tightly connected with the sealing pressure-resistant apparatus.
3, by claim 1, the sea water desalinating plant of 2 regulations, it is characterized in that being equipped with in the pressure-resistant seal device [1] reverse osmosis equipment [2], an one high-tension side interface [3] connects pretreating device [6], comprise ultra-filtration equipment and security personnel's strainer in the pretreating device [6], the outlet of another termination recycle pump [9] of pretreating device, the inlet of recycle pump [10] reaches outside the pressure-resistant seal device and with the pressure-resistant seal device and is tightly connected, on high-tension side another interface [4] of reverse osmosis unit [2] reaches outside the pressure-resistant seal device and with pressure-resistant seal device [1] and is tightly connected, the liquid outlet [5] that sees through of reverse osmosis unit [2] connects water tank [12], water tank [11] connects the inlet of transferpump [7], the sea is stretched out in the outlet of transferpump [6], and be tightly connected with the pressure-resistant seal jar, between each parts, all can add valve.
4, by claim 1,2,3 sea water desalinating plants of stipulating, it is characterized in that the inlet [10] sea water circulating pump connects the outlet [4] of reverse osmosis unit [2], the outlet of sea water circulating pump reaches outside the pressure-resistant seal device and with pressure-resistant seal device [1] and is tightly connected, and all can add valve between each parts.
5, by claim 1, the sea water desalinating plant of 2 regulations, it is characterized in that being equipped with in the pressure-resistant seal device [17] reverse osmosis equipment [18], ultrafiltration apparatus [19], sea water circulating pump [20], fresh water Send out pump [21] etc., the inlet of sea water circulating pump [20] connects valve [24], the other end of valve [24] is joined two pipes together and is stretched out pressure-resistant seal device [17], and be tightly connected with pressure-resistant seal device [17], the outlet of sea water circulating pump [20] connects security personnel's strainer [23], a stoste communication port [30] of another termination ultrafiltration apparatus [19] of security personnel's strainers [23], another stoste communication port [31] of ultrafiltration apparatus [19] connects valve [25], the other end of valve [25] is joined two pipes together and is stretched out pressure-resistant seal container [17] and be tightly connected with pressure-resistant seal container [17], the liquid spout [32] that sees through of ultrafiltration apparatus [19] connects valve [27], a high-tension side interface [33] of another termination reverse osmosis equipment of valve [27], another high-tension side interface of reverse osmosis equipment connects valve [26], the other end of valve [26] is joined two pipes together and is stretched out pressure-resistant seal container [17] and be tightly connected with pressure-resistant seal container [17], the liquid spout [36] that sees through of reverse osmosis equipment connects valve [28], another termination receiver [22] of valve [28], another interface of receiver [22] connects valve [29], the inlet of another termination fresh water Send out pump [21] of valve [29], the outlet of fresh water Send out pump [21] connects valve [35], the other end of valve [35] is joined two pipes together and is stretched out pressure-resistant seal container [17] and expose the sea, and is tightly connected with pressure-resistant seal container [17].
CNA2004100392396A 2004-02-09 2004-02-09 Sea water desalting plant processed deep in sea Pending CN1654342A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNA2004100392396A CN1654342A (en) 2004-02-09 2004-02-09 Sea water desalting plant processed deep in sea

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNA2004100392396A CN1654342A (en) 2004-02-09 2004-02-09 Sea water desalting plant processed deep in sea

Publications (1)

Publication Number Publication Date
CN1654342A true CN1654342A (en) 2005-08-17

Family

ID=34892315

Family Applications (1)

Application Number Title Priority Date Filing Date
CNA2004100392396A Pending CN1654342A (en) 2004-02-09 2004-02-09 Sea water desalting plant processed deep in sea

Country Status (1)

Country Link
CN (1) CN1654342A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101626982B (en) * 2007-02-14 2013-05-29 Dxv水科技公司 Depth exposed membrane for water extraction
US8685252B2 (en) 2010-02-04 2014-04-01 Dxv Water Technologies, Llc Water treatment systems and methods
CN104229936A (en) * 2013-06-20 2014-12-24 张玉宝 Reverse osmosis seawater desalination device with low energy consumption and reverse osmosis seawater desalination method using same
CN105217735A (en) * 2015-11-11 2016-01-06 杜善骥 Submersible type concentrated seawater self refresh reverse osmosis desalination device
US10513446B2 (en) 2014-10-10 2019-12-24 EcoDesal, LLC Depth exposed membrane for water extraction
CN113044921A (en) * 2019-12-29 2021-06-29 广州易能克科技有限公司 Dual-purpose seawater desalination device for deep water and shallow water

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101626982B (en) * 2007-02-14 2013-05-29 Dxv水科技公司 Depth exposed membrane for water extraction
US8685252B2 (en) 2010-02-04 2014-04-01 Dxv Water Technologies, Llc Water treatment systems and methods
US8999162B2 (en) 2010-02-04 2015-04-07 Econopure Water Systems, Llc Water treatment systems and methods
CN104229936A (en) * 2013-06-20 2014-12-24 张玉宝 Reverse osmosis seawater desalination device with low energy consumption and reverse osmosis seawater desalination method using same
CN104229936B (en) * 2013-06-20 2017-04-12 张玉宝 Low-energy-consumption reverse osmosis seawater desalination and mineralization device
US10513446B2 (en) 2014-10-10 2019-12-24 EcoDesal, LLC Depth exposed membrane for water extraction
CN105217735A (en) * 2015-11-11 2016-01-06 杜善骥 Submersible type concentrated seawater self refresh reverse osmosis desalination device
CN113044921A (en) * 2019-12-29 2021-06-29 广州易能克科技有限公司 Dual-purpose seawater desalination device for deep water and shallow water

Similar Documents

Publication Publication Date Title
CA2812967C (en) Method and apparatus for dynamic, variable-pressure, customizable, membrane-based water treatment for use in improved hydrocarbon recovery operations
US9932250B2 (en) Membrane filtration system
RU2363663C2 (en) Device for continuous water demineralisation in closed circuit at alternate pressure in one tank
NO344863B1 (en) Modularized subsea seawater desalination system
KR101817685B1 (en) See water desalination system using pressure-retarded osmosis
US20180297866A1 (en) Water treatment system and water treatment method
WO2017216785A1 (en) Pressure-exchange assisted closed circuit desalination systems for continuous desalination of low energy and high recovery under fixed flow and variable pressure conditions
CN1654342A (en) Sea water desalting plant processed deep in sea
WO2012175804A1 (en) High efficiency membrane filtration
US20110290728A1 (en) SWRO Pressure Vessel and Process That Increases Production and Product Quality and Avoids Scaling Problems
CN106428504A (en) Small reverse osmosis seawater desalting device
CN2743329Y (en) Equipment for proceeding reverse osmosis using sea water natural pressure
US9010438B2 (en) Fluid treatment system
KR20160054230A (en) See water desalination system using pressure-retarded osmosis
CN103370280B (en) Compound desalination system
CN201284253Y (en) Nano filter membrane bitter brine desalting system apparatus
EP2405992B1 (en) Continuous process batch-operated reverse osmosis system with in-tank membranes and circulation of concentrate
CN107445322A (en) One kind miniaturization reverse osmosis seawater desalination system
NO345752B1 (en) Subsea desalination system for shallow water
CN2784399Y (en) Water treatment system for industrial ultra pure water
CN220788187U (en) Marine sea water desalination device based on heavy ion microporous membrane filtration
AU2011100390A4 (en) Peristaltic pressure exchanger in reverse osmosis desalination
CN2491437Y (en) Electric and manually operated counter-permeating desalter
CN209853848U (en) Reverse osmosis device
CN205222871U (en) 15 tonnes container formula seawater desalination equipment per hour

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination