CN105461116A - Desalting treatment device for seawater - Google Patents

Desalting treatment device for seawater Download PDF

Info

Publication number
CN105461116A
CN105461116A CN201511034495.0A CN201511034495A CN105461116A CN 105461116 A CN105461116 A CN 105461116A CN 201511034495 A CN201511034495 A CN 201511034495A CN 105461116 A CN105461116 A CN 105461116A
Authority
CN
China
Prior art keywords
filter
reverse osmosis
desalting treatment
treatment equipment
osmosis membrane
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
CN201511034495.0A
Other languages
Chinese (zh)
Inventor
韩永良
刘丽妍
赵义平
吴云
闫双春
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.)
Tianjin Han Qing Environmental Protection Technology Co Ltd
Original Assignee
Tianjin Han Qing Environmental Protection Technology Co Ltd
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 Tianjin Han Qing Environmental Protection Technology Co Ltd filed Critical Tianjin Han Qing Environmental Protection Technology Co Ltd
Priority to CN201511034495.0A priority Critical patent/CN105461116A/en
Publication of CN105461116A publication Critical patent/CN105461116A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • 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
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • 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
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/441Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • 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
    • C02F1/66Treatment of water, waste water, or sewage by neutralisation; pH adjustment
    • 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
    • C02F2301/08Multistage treatments, e.g. repetition of the same process step under different conditions
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/04Disinfection
    • 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

  • 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)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

The invention provides a desalting treatment device for seawater. The device comprises a pretreatment system, a reverse osmosis system and a disinfection system. The pretreatment system comprises a quartz sand filter, an active carbon filter, an antisludging agent adding device and a PH value adjusting filtering core. The quartz sand filter is arranged behind a water inlet, and the active carbon filter is arranged behind the quartz sand filter. The antisludging agent adding device comprises a dissolving box and a metering pump. The PH value adjusting filtering core is arranged behind the quartz sand filter. The reverse osmosis system comprises a bagged filter, a high-pressure pump and a reverse osmosis membrane stack. The bagged filter is arranged behind the active carbon filter, the high-pressure pump is arranged behind the PH value adjusting filtering core, the reverse osmosis membrane stack is arranged behind the high-pressure pump, and the disinfection system is arranged on a water outlet pipe of the reverse osmosis system. According to the device, a pretreatment and reverse osmosis combined mode is used, so that energy consumption during water desalting is low, and automatic control is facilitated.

Description

A kind of desalting treatment equipment of seawater
Technical field
The present invention relates to field of sea water desalting technology, particularly relate to a kind of desalting treatment equipment of seawater.
Background technology
Earth surface nearly more than 90% cover by seawater, along with the continuous minimizing of Freshwater resources, seawater becomes one of main path of social development and people's domestic water.But its construction investment of traditional method for desalting seawater is high, power consumption is large, and the turndown ratio of equipment is little.Therefore, an important goal of desalination technology development reduces running cost, and in the formation of running cost, the proportion shared by energy consumption is maximum, so reducing energy consumption is reduce the most effective means of sea water desaltination cost.Reverse osmosis seawater desalting is one of mainstream technology of current sea water desaltination.In reverse osmosis seawater desalting process, need to consume a large amount of electric energy and promote intake pressure to overcome the osmotic pressure of water, and the dense water overbottom pressure that reverse osmosis membrane is discharged is up to 5.5 ~ 6.5MPa, the rate of recovery according to 40% calculates, the feed water pressure energy of about 60% is also contained in the strong brine of discharge, this part energy reclaimed and become the energy consumption that significantly can reduce reverse osmosis seawater desalting into water energy, the realization of this purpose depends on the raising of Energy Recovery Technology.
Summary of the invention
Main purpose of the present invention is to solve problems of the prior art, provides that a kind of reduced investment, energy consumption are low, device volume is little, and operation of equipment is simple, the easy to maintenance and desalting treatment equipment of the seawater operated at normal temperatures.
For solving the problems of the technologies described above, the technical solution used in the present invention is: a kind of desalting treatment equipment of seawater, and the desalting treatment equipment of described seawater comprises pretreatment system, reverse osmosis system and sterilisation system, wherein,
Described pretreatment system comprises quartz filter, activated charcoal filter, Scale inhibitors chemicals dosing plant and pH value and regulates filter core, described quartz filter is arranged at after water-in, described activated charcoal filter is arranged at after described quartz filter, described Scale inhibitors chemicals dosing plant comprises a molten medicine-chest and a volume pump, Scale inhibitors in described molten medicine-chest pumps in the pipeline before reverse osmosis membrane stack by described volume pump, and described pH value regulates filter core to be arranged at after deep bed filter;
Described reverse osmosis system comprises deep bed filter, high-pressure pump and reverse osmosis membrane stack, described deep bed filter is arranged at after described activated charcoal filter, this deep bed filter is for removing impurity to protect reverse osmosis membrane stack, described high-pressure pump is arranged at described pH value and regulates after filter core, this high-pressure pump is by arranging the intake pressure of raw water quality, can obtain the different rate of recovery, described reverse osmosis membrane stack is arranged on after described high-pressure pump;
Described sterilisation system is arranged on the outlet conduit of described reverse osmosis system, prevents breed bacteria.
Further, the effluent quality of described pretreatment system is set to pollution index (SDI) <3.
Further, described quartz filter is arranged a quartz filter Full-automatic filter valve.
Further, described activated charcoal filter is arranged an activated charcoal filter Full-automatic filter valve.
Further, the reverse osmosis membrane of described reverse osmosis membrane stack is set to semi-permeable membrane, and this reverse osmosis membrane selectivity under impressed pressure effect, through some component in the aqueous solution, thus reaches the object of desalination, water purification or concentrating and separating.
Further, described reverse osmosis membrane stack is arranged a concentrated water discharge mouth, and this concentrated water discharge mouth also discharges the backwash water of quartz filter, activated charcoal filter.
Further, described sterilisation system is arranged a tap water water-in, this tap water water-in configures liquid for injecting tap water for sterilizing unit.
The advantage that the present invention has and positively effect are: the desalting treatment equipment of seawater provided by the invention, pass through pre-treatment, the mode that reverse osmosis and after-treatment system combine, the technological merit of impervious desalination system can be given full play to, ensure its good design performance and long safe operation, especially ensure that the work-ing life of reverse osmosis membrane.And the desalting treatment equipment of this seawater, can arrange the different rate of recovery according to different raw water qualities, and make system energy-conservation as much as possible by flow process and selecting of device.So the desalting treatment equipment of seawater of the present invention is applicable to the desalting engineering of the large, medium and small scale such as seawater, brackish water, and the volume of this equipment is little, simple to operate and easy to maintenance.
Accompanying drawing explanation
Fig. 1 is of the present invention is schematic diagram
In figure: 10-pretreatment system, 101-water-in, 102-quartz filter Full-automatic filter valve, 103-activated charcoal filter Full-automatic filter valve, 104-quartz filter, 105-activated charcoal filter, 106-PH value regulates filter core, 20-reverse osmosis system, 201-deep bed filter, 202-high-pressure pump, 203-reverse osmosis membrane stack, 204-concentrated water discharge mouth, 30-sterilisation system, 301-tap water water-in, 302-produces water water outlet.
Embodiment
For a better understanding of the present invention, below in conjunction with specific embodiments and the drawings, the present invention is conducted further description.
As shown in Figure 1, a kind of desalting treatment equipment of seawater, comprises pretreatment system 10, reverse osmosis system 20 and sterilisation system 30, wherein,
Pretreatment system 10 comprises quartz filter 104, activated charcoal filter 105, Scale inhibitors chemicals dosing plant and pH value and regulates filter core 106, quartz filter 104 is arranged at after water-in 101, activated charcoal filter 105 is arranged at after quartz filter 104, Scale inhibitors chemicals dosing plant comprises a molten medicine-chest and a volume pump, Scale inhibitors in molten medicine-chest pumps in the pipeline before reverse osmosis membrane stack 203 by volume pump, and pH value regulates filter core 106 to be arranged at after deep bed filter 201;
Reverse osmosis system 20 comprises deep bed filter 201, high-pressure pump 202 and reverse osmosis membrane stack 203; deep bed filter 201 is arranged at after activated charcoal filter 105; this deep bed filter 201 is for removing impurity to protect reverse osmosis membrane stack 203; high-pressure pump 202 is arranged at pH value and regulates after filter core 106; this high-pressure pump 202, by arranging the intake pressure of raw water quality, can obtain the different rate of recovery.Reverse osmosis membrane stack 203 is arranged on after high-pressure pump 202;
Sterilisation system 30 is arranged on the outlet conduit of reverse osmosis system 20, prevents breed bacteria.
The effluent quality of pretreatment system 10 is set to pollution index (SDI) <3.
Quartz filter 104 is arranged a quartz filter Full-automatic filter valve 102.
Activated charcoal filter 105 is arranged an activated charcoal filter Full-automatic filter valve 103.
The reverse osmosis membrane of reverse osmosis membrane stack 203 is set to semi-permeable membrane, and this reverse osmosis membrane selectivity under impressed pressure effect, through some component in the aqueous solution, thus reaches the object of desalination, water purification or concentrating and separating.
Reverse osmosis membrane stack 203 is arranged a concentrated water discharge mouth 204, and this concentrated water discharge mouth 204 also discharges the backwash water of quartz filter 104, activated charcoal filter 103.
Sterilisation system 30 is arranged a tap water water-in 301, this tap water water-in 301 configures liquid for injecting tap water for sterilizing unit.
Use the desalting treatment equipment of seawater provided by the invention, the different rate of recovery can be arranged according to different raw water qualities, and make system energy-conservation as much as possible by flow process and selecting of device.During work, water source enters the quartz filter Full-automatic filter valve 102 be arranged on quartz filter 104 by water-in 101, then the water outlet of quartz filter full-automatic valve 102 enters the activated charcoal filter Full-automatic filter valve 103 be arranged on activated charcoal filter 105, then the water outlet of activated charcoal filter Full-automatic filter valve 103 regulates filter core 106 through deep bed filter 201 and pH value, further removal suspended solids and other objectionable impurities, the reverse osmosis membrane stack 203 of reverse osmosis system 20 is pumped into again by high-pressure pump 202, utilize the semipermeability of reverse osmosis membrane, make under impressed pressure effect some compositional selecting in the aqueous solution through, carry out desalting treatment, the water outlet of last reverse osmosis system 20 is through the sterilization of sterilisation system 30, delivered to by product water out 302 and use water place, obtain finished product fresh water.Wherein, the backwash water of quartz filter Full-automatic filter valve 102 and activated charcoal filter Full-automatic filter valve 103, collects on a bye-pass with the dense draining of reverse osmosis system 20, is discharged by concentrated water discharge mouth 204.
Above embodiments of the invention have been described in detail, but described content being only preferred embodiment of the present invention, can not being considered to for limiting practical range of the present invention.All equalizations done according to the scope of the invention change and improve, and all should still belong within this patent covering scope.

Claims (7)

1. a desalting treatment equipment for seawater, is characterized in that: the desalting treatment equipment of described seawater comprises pretreatment system, reverse osmosis system and sterilisation system, wherein,
Described pretreatment system comprises quartz filter, activated charcoal filter, Scale inhibitors chemicals dosing plant and pH value and regulates filter core, described quartz filter is arranged at after water-in, described activated charcoal filter is arranged at after described quartz filter, described Scale inhibitors chemicals dosing plant comprises a molten medicine-chest and a volume pump, Scale inhibitors in described molten medicine-chest pumps in the pipeline before reverse osmosis membrane stack by described volume pump, and described pH value regulates filter core to be arranged at after deep bed filter;
Described reverse osmosis system comprises deep bed filter, high-pressure pump and reverse osmosis membrane stack, described deep bed filter is arranged at after described activated charcoal filter, described high-pressure pump is arranged at described pH value and regulates after filter core, and described reverse osmosis membrane stack is arranged at after described high-pressure pump;
Described sterilisation system is arranged on the outlet conduit of described reverse osmosis system.
2. the desalting treatment equipment of seawater according to claim 1, is characterized in that: the effluent quality of described pretreatment system is set to pollution index (SDI) <3.
3. the desalting treatment equipment of seawater according to claim 1, is characterized in that: also comprise, and described quartz filter is arranged a quartz filter Full-automatic filter valve.
4. the desalting treatment equipment of seawater according to claim 1, is characterized in that: also comprise, and described activated charcoal filter is arranged an activated charcoal filter Full-automatic filter valve.
5. the desalting treatment equipment of seawater according to claim 1, is characterized in that: the reverse osmosis membrane of described reverse osmosis membrane stack is set to semi-permeable membrane.
6. the desalting treatment equipment of seawater according to claim 1, is characterized in that: also comprise, and described reverse osmosis membrane stack is arranged a concentrated water discharge mouth, and this concentrated water discharge mouth also discharges the backwash water of quartz filter, activated charcoal filter.
7. the desalting treatment equipment of seawater according to claim 1, is characterized in that: also comprise, and described sterilisation system is arranged a tap water water-in.
CN201511034495.0A 2015-12-31 2015-12-31 Desalting treatment device for seawater Pending CN105461116A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201511034495.0A CN105461116A (en) 2015-12-31 2015-12-31 Desalting treatment device for seawater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201511034495.0A CN105461116A (en) 2015-12-31 2015-12-31 Desalting treatment device for seawater

Publications (1)

Publication Number Publication Date
CN105461116A true CN105461116A (en) 2016-04-06

Family

ID=55599342

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201511034495.0A Pending CN105461116A (en) 2015-12-31 2015-12-31 Desalting treatment device for seawater

Country Status (1)

Country Link
CN (1) CN105461116A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106517596A (en) * 2016-12-22 2017-03-22 重庆市沃利克环保设备有限公司 Reverse osmosis seawater desalination system and treatment process implemented by same
CN110204080A (en) * 2019-07-11 2019-09-06 南京慧城水处理设备有限公司 Surgical instrument and operation cloth grass clean waste water treatment system

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5015789A (en) * 1973-06-14 1975-02-19
CN201010593Y (en) * 2007-03-05 2008-01-23 陶欣 Intelligent sea water desalting equipment
CN201268638Y (en) * 2008-06-17 2009-07-08 西安皓海嘉水处理科技有限责任公司 Seawater desalination system by film method
CN205442865U (en) * 2015-12-31 2016-08-10 天津汉晴环保科技有限公司 Seawater desalination's treatment facility

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5015789A (en) * 1973-06-14 1975-02-19
CN201010593Y (en) * 2007-03-05 2008-01-23 陶欣 Intelligent sea water desalting equipment
CN201268638Y (en) * 2008-06-17 2009-07-08 西安皓海嘉水处理科技有限责任公司 Seawater desalination system by film method
CN205442865U (en) * 2015-12-31 2016-08-10 天津汉晴环保科技有限公司 Seawater desalination's treatment facility

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106517596A (en) * 2016-12-22 2017-03-22 重庆市沃利克环保设备有限公司 Reverse osmosis seawater desalination system and treatment process implemented by same
CN110204080A (en) * 2019-07-11 2019-09-06 南京慧城水处理设备有限公司 Surgical instrument and operation cloth grass clean waste water treatment system

Similar Documents

Publication Publication Date Title
WO2018150980A1 (en) Reverse osmosis treatment device and reverse osmosis treatment method
CN102329018B (en) Device for desalting sea water by low-pressure membrane method
CN102249459A (en) System for desalinating sea water
JP2013126636A (en) Reverse osmosis treatment apparatus
KR101389450B1 (en) Desalination apparatus and desalinating method thereof
CN203866137U (en) Direct drinking water purification system for building pipeline
CN101186407A (en) System for desalinizing sea water by jet flow cavitation technique
CN206255935U (en) A kind of 50 tons of intermediate water reuse systems per hour
CN102963993A (en) Reusable ultrafilter using reverse osmosis thick water as flushing water and reverse osmosis system
CN105540746A (en) water purification system
WO2016066382A1 (en) A water purifier and a process of cleaning the membrane
CN203807252U (en) Seawater treatment device
CN201411394Y (en) Reverse osmosis membrane purified water machine without waste water discharge
CN203768136U (en) Scale-inhibition and corrosion-inhibition treatment system for gas drainage pump circulating water
CN105461116A (en) Desalting treatment device for seawater
CN211367282U (en) High-purity water treatment system
CN100522826C (en) Water treatment method capable of reusing concentrated water wholly
CN205442865U (en) Seawater desalination&#39;s treatment facility
CN204058142U (en) Self-cleaning water treatment system
CN207596632U (en) A kind of salted egg salting liquid recycling equipment
CN108706782A (en) A kind of sea water desalination processing unit
CN203754515U (en) Double membrane system for treating circulating water for coke dry quenching power generation
CN210495949U (en) Reverse osmosis system of water purifier capable of performing back flushing
WO2013134901A1 (en) Sea water desalination processing system
CN203498173U (en) Back washing energy saving device of reverse osmosis seawater desalination system

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20160406

RJ01 Rejection of invention patent application after publication