CN106219848A - A kind of agitating type is double filters salt technology - Google Patents

A kind of agitating type is double filters salt technology Download PDF

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Publication number
CN106219848A
CN106219848A CN201610573141.1A CN201610573141A CN106219848A CN 106219848 A CN106219848 A CN 106219848A CN 201610573141 A CN201610573141 A CN 201610573141A CN 106219848 A CN106219848 A CN 106219848A
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CN
China
Prior art keywords
waste liquid
agitating type
double
technology according
filter
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Pending
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CN201610573141.1A
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Chinese (zh)
Inventor
令狐文生
刘伟
杨海
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University of Shaoxing
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University of Shaoxing
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Priority to CN201610573141.1A priority Critical patent/CN106219848A/en
Publication of CN106219848A publication Critical patent/CN106219848A/en
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    • 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
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • 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
    • 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
    • C02F1/442Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by nanofiltration
    • 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
    • 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

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  • 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)

Abstract

The invention discloses a kind of agitating type pair and filter salt technology, its step is as follows: step 1, by mixing high-salt wastewater in drainage screen enters into waste liquid regulating tank;Step 2, in high-salt wastewater, acid adding or alkali regulation pH value are to 79, are then joined in waste liquid tank by high-pressure pump;Step 3, joins in nanofiltration membrane component by waste liquid supercharging in waste liquid tank, and waste water is in nanofiltration membrane component enters into heated and stirred groove;Step 4, is stirred the waste water in heated and stirred groove heating, and keeps constant temperature;Step 5, joins constant temperature waste liquid in NACE membrane module, enters into sump pit after membrane filtration, i.e. obtains discharging water.The present invention takes full advantage of the advantage of membrane separation technique, has pollution-free, the advantage of low energy consumption, also solves the technological deficiency of reverse osmosis (RO) film simultaneously.

Description

A kind of agitating type is double filters salt technology
Technical field
The invention belongs to Environmental Chemistry technical field, be specifically related to a kind of agitating type pair and filter salt technology.
Background technology
Membrane filtration is a kind of screening process relevant to membrane aperture size, with the pressure differential of film both sides as driving force, with film For filter medium, under pressure, when stock solution flows through film surface, the tiny micropore of the many gathered in film surface only allows Water and small-molecule substance by and become permeate, in stock solution, volume is then trapped within film more than the material in film surface micropore footpath Liquid feeding side, become concentrated solution, thus realize the separation to stock solution and the purpose of concentration.
Reverse osmosis technology just began one's study in the fifties, made the reverse osmosis membrane with industrial value to the end of the sixties, Within 1971, begin with industrialness reverse osmosis unit to put into operation in power plant, use now hyperfiltration to carry out water and process throughout U.S. The countries such as state, Japan, France, Italy.China starts to introduce the reverse osmosis unit water in power plant the end of the seventies and processes, and 90 Developing of age reverse osmosis membrane becomes focus, and present reverse osmosis technology is mainly used in desalinization, pure water and ultra-pure water Preparation, city water process, municipal sewage treatment and application, industry plating wastewater and the process of pulp and paper industry waste water, The waste water such as chemical wastewater treatment, food industry, medical industry process.This fully demonstrates reverse osmosis technology at wastewater reusing treatment Technology maturation reliable.
But, exist a series of as industrial high-salt wastewater complicated faced by the reverse osmosis technology of current main flow desalination technology Problem, reverse osmosis membrane uses environmental requirement higher, it is impossible to adapt to complicated actual environment;Although removal efficiency is the highest, but deposit Easily change at film, it is impossible to use for a long time.
Summary of the invention
It is an object of the invention to provide a kind of agitating type pair and filter salt technology, the present invention takes full advantage of membrane separation technique Advantage, has pollution-free, the advantage of low energy consumption, also solves the technological deficiency of reverse osmosis (RO) film simultaneously.
A kind of agitating type is double filters salt technology, and its step is as follows:
Step 1, by mixing high-salt wastewater in drainage screen enters into waste liquid regulating tank;
Step 2, in high-salt wastewater, acid adding or alkali regulation pH value are to 7-9, are then joined in waste liquid tank by high-pressure pump;
Step 3, joins in nanofiltration membrane component by waste liquid supercharging in waste liquid tank, and waste water enters into heated and stirred through nanofiltration membrane component In groove;
Step 4, is stirred the waste water in heated and stirred groove heating, and keeps constant temperature;
Step 5, joins constant temperature waste liquid in NACE membrane module, enters into sump pit after membrane filtration, i.e. obtains discharging water.
Acid solution in described step 2 uses sulphuric acid, and the concentration of described sulphuric acid is 30-50%
Aqueous slkali in described step 2 uses sodium hydroxide, and described naoh concentration is 1-3mol/L.
Use drainage screen to carry out precipitation after described step 2 regulates pH value to filter.
NF membrane in described step 3 uses sulfonated polyether sulfone class composite nanometer filtering film or aromatic polyamides class composite nanometer filtering film Middle one.
Thermostat temperature in described step 4 is 50-60 DEG C, and mixing speed is 2000-3000r/min.
NACE film in described step 5 uses nanostructured polymers to make, and adds a small amount of nanoparticle the most in the plastic Son makes Organic substance matrix and inorganic matter dispersion phase compound on nano-scale.
Described plastics include the one in polyethylene, polypropylene, polrvinyl chloride.
Described nanoparticle uses the one in nano-calcium carbonate, nano barium sulfate, and the particle diameter of described nanoparticle is 100-500nm。
Being provided with chiller in described step 5 in sump pit, described chiller uses aeration chiller.
Compared with prior art, the method have the advantages that
1, the present invention carries out double membrane filtration by NF membrane and NACE film, filters mixing high-salt wastewater to discharge standard.
2, the present invention takes full advantage of the advantage of membrane separation technique, has pollution-free, the advantage of low energy consumption, also solves simultaneously The technological deficiency of reverse osmosis (RO) film.
3, the NACE film that the present invention uses has soluble solid, chlorine, low ph value or biological pollution in waste water unwise Sense;Without regeneration requirements;Scale problems without film;Service life is long;Without features such as chemical drugss.
4, the NACE membrane technology that the present invention uses has the advantages such as operating cost is low, antipollution, treatment effect are stable.
Detailed description of the invention
Below in conjunction with embodiment, the present invention is described further:
Embodiment 1
A kind of agitating type is double filters salt technology, and its step is as follows:
Step 1, by mixing high-salt wastewater in drainage screen enters into waste liquid regulating tank;
Step 2, in high-salt wastewater, acid adding or alkali regulation pH value are to 7, are then joined in waste liquid tank by high-pressure pump;
Step 3, joins in nanofiltration membrane component by waste liquid supercharging in waste liquid tank, and waste water enters into heated and stirred through nanofiltration membrane component In groove;
Step 4, is stirred the waste water in heated and stirred groove heating, and keeps constant temperature;
Step 5, joins constant temperature waste liquid in NACE membrane module, enters into sump pit after membrane filtration, i.e. obtains discharging water.
Acid solution in described step 2 uses sulphuric acid, and the concentration of described sulphuric acid is 30%
Aqueous slkali in described step 2 uses sodium hydroxide, and described naoh concentration is 1mol/L.
Use drainage screen to carry out precipitation after described step 2 regulates pH value to filter.
NF membrane in described step 3 uses sulfonated polyether sulfone class composite nanometer filtering film.
Thermostat temperature in described step 4 is 50-60 DEG C, and mixing speed is 2000r/min.
NACE film in described step 5 uses nanostructured polymers to make, and adds a small amount of nanoparticle the most in the plastic Son makes Organic substance matrix and inorganic matter dispersion phase compound on nano-scale.
Described plastics include polyethylene.
Described nanoparticle uses nano-calcium carbonate, and the particle diameter of described nanoparticle is 100nm.
Being provided with chiller in described step 5 in sump pit, described chiller uses aeration chiller.
Embodiment 2
A kind of agitating type is double filters salt technology, and its step is as follows:
Step 1, by mixing high-salt wastewater in drainage screen enters into waste liquid regulating tank;
Step 2, in high-salt wastewater, acid adding or alkali regulation pH value are to 9, are then joined in waste liquid tank by high-pressure pump;
Step 3, joins in nanofiltration membrane component by waste liquid supercharging in waste liquid tank, and waste water enters into heated and stirred through nanofiltration membrane component In groove;
Step 4, is stirred the waste water in heated and stirred groove heating, and keeps constant temperature;
Step 5, joins constant temperature waste liquid in NACE membrane module, enters into sump pit after membrane filtration, i.e. obtains discharging water.
Acid solution in described step 2 uses sulphuric acid, and the concentration of described sulphuric acid is 50%
Aqueous slkali in described step 2 uses sodium hydroxide, and described naoh concentration is 3mol/L.
Use drainage screen to carry out precipitation after described step 2 regulates pH value to filter.
NF membrane in described step 3 uses aromatic polyamides class composite nanometer filtering film.
Thermostat temperature in described step 4 is 60 DEG C, and mixing speed is 3000r/min.
NACE film in described step 5 uses nanostructured polymers to make, and adds a small amount of nanoparticle the most in the plastic Son makes Organic substance matrix and inorganic matter dispersion phase compound on nano-scale.
Described plastics include polypropylene.
Described nanoparticle uses nano barium sulfate, and the particle diameter of described nanoparticle is 00nm.
Being provided with chiller in described step 5 in sump pit, described chiller uses aeration chiller.
Embodiment 3
A kind of agitating type is double filters salt technology, and its step is as follows:
Step 1, by mixing high-salt wastewater in drainage screen enters into waste liquid regulating tank;
Step 2, in high-salt wastewater, acid adding or alkali regulation pH value are to 8, are then joined in waste liquid tank by high-pressure pump;
Step 3, joins in nanofiltration membrane component by waste liquid supercharging in waste liquid tank, and waste water enters into heated and stirred through nanofiltration membrane component In groove;
Step 4, is stirred the waste water in heated and stirred groove heating, and keeps constant temperature;
Step 5, joins constant temperature waste liquid in NACE membrane module, enters into sump pit after membrane filtration, i.e. obtains discharging water.
Acid solution in described step 2 uses sulphuric acid, and the concentration of described sulphuric acid is 40%
Aqueous slkali in described step 2 uses sodium hydroxide, and described naoh concentration is 2mol/L.
Use drainage screen to carry out precipitation after described step 2 regulates pH value to filter.
NF membrane in described step 3 uses sulfonated polyether sulfone class composite nanometer filtering film.
Thermostat temperature in described step 4 is 55 DEG C, and mixing speed is 2500r/min.
NACE film in described step 5 uses nanostructured polymers to make, and adds a small amount of nanoparticle the most in the plastic Son makes Organic substance matrix and inorganic matter dispersion phase compound on nano-scale.
Described plastics include polrvinyl chloride.
Described nanoparticle uses nano-calcium carbonate, and the particle diameter of described nanoparticle is 300nm.
Being provided with chiller in described step 5 in sump pit, described chiller uses aeration chiller.
It is the sodium sulfate of 0.5mol/ that the process of embodiment 1-3 processes total concentration, and potassium sulfate, sodium nitrate, potassium nitrate mix Closing liquid, mixed liquor after treatment meets CJ343-2010 sewage and enters the B class standard of town sewer water standard.
The foregoing is only one embodiment of the invention, be not limiting as the present invention, all employing equivalents or equivalent transformation The technical scheme that obtained of mode, all fall within protection scope of the present invention.

Claims (10)

1. an agitating type pair filters salt technology, it is characterised in that its step is as follows:
Step 1, by mixing high-salt wastewater in drainage screen enters into waste liquid regulating tank;
Step 2, in high-salt wastewater, acid adding or alkali regulation pH value are to 7-9, are then joined in waste liquid tank by high-pressure pump;
Step 3, joins in nanofiltration membrane component by waste liquid supercharging in waste liquid tank, and waste water enters into heated and stirred through nanofiltration membrane component In groove;
Step 4, is stirred the waste water in heated and stirred groove heating, and keeps constant temperature;
Step 5, joins constant temperature waste liquid in NACE membrane module, enters into sump pit after membrane filtration, i.e. obtains discharging water.
2. filter salt technology according to a kind of agitating type described in claims 1 is double, it is characterised in that the acid in described step 2 Solution uses sulphuric acid, and the concentration of described sulphuric acid is 30-50%.
3. filter salt technology according to a kind of agitating type described in claims 1 is double, it is characterised in that the alkali in described step 2 Solution uses sodium hydroxide, and described naoh concentration is 1-3mol/L.
4. filter salt technology according to a kind of agitating type described in claims 1 is double, it is characterised in that described step 2 regulates Use drainage screen to carry out precipitation after pH value to filter.
5. filter salt technology according to a kind of agitating type described in claims 1 is double, it is characterised in that receiving in described step 3 Filter membrane uses in sulfonated polyether sulfone class composite nanometer filtering film or aromatic polyamides class composite nanometer filtering film a kind of.
6. filter salt technology according to a kind of agitating type described in claims 1 is double, it is characterised in that the perseverance in described step 4 Temperature temperature is 50-60 DEG C, and mixing speed is 2000-3000r/min.
7. filter salt technology according to a kind of agitating type described in claims 1 is double, it is characterised in that in described step 5 NACE film uses nanostructured polymers to make, and adds a small amount of nanoparticle the most in the plastic and makes Organic substance matrix and inorganic matter Dispersion phase is compound on nano-scale.
8. filter salt technology according to a kind of agitating type described in claims 7 is double, it is characterised in that described plastics include poly-second One in alkene, polypropylene, polrvinyl chloride.
9. filter salt technology according to a kind of agitating type described in claims 7 is double, it is characterised in that described nanoparticle uses One in nano-calcium carbonate, nano barium sulfate, the particle diameter of described nanoparticle is 100-500nm.
10. filter salt technology according to a kind of agitating type described in claims 1 is double, it is characterised in that discharge opeing in described step 5 Being provided with chiller in groove, described chiller uses aeration chiller.
CN201610573141.1A 2016-07-21 2016-07-21 A kind of agitating type is double filters salt technology Pending CN106219848A (en)

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Application Number Priority Date Filing Date Title
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006000073A1 (en) * 2004-06-23 2006-01-05 Bioz Agri Products Inc. Method for extracting fulvic acid molecules
CN101041487A (en) * 2007-03-20 2007-09-26 山东布莱恩化工技术有限公司 Pretreatment method for sulfate radical removal from salt water by membrane process
WO2009101157A1 (en) * 2008-02-14 2009-08-20 Otv Sa Process for treating water by a nanofiltration or reverse osmosis membrane system permitting high conversion rates due to the elimination of organic matter
CN101935118A (en) * 2010-08-16 2011-01-05 刘春喜 Process for purifying and recycling hot water by membrane method
CN104591451A (en) * 2014-12-25 2015-05-06 江苏水智乐自动化设备有限公司 Tap water purification system
CN204369669U (en) * 2014-09-28 2015-06-03 星达(泰州)膜科技有限公司 A kind of nanofiltration membrane purifier

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006000073A1 (en) * 2004-06-23 2006-01-05 Bioz Agri Products Inc. Method for extracting fulvic acid molecules
CN101041487A (en) * 2007-03-20 2007-09-26 山东布莱恩化工技术有限公司 Pretreatment method for sulfate radical removal from salt water by membrane process
WO2009101157A1 (en) * 2008-02-14 2009-08-20 Otv Sa Process for treating water by a nanofiltration or reverse osmosis membrane system permitting high conversion rates due to the elimination of organic matter
CN101935118A (en) * 2010-08-16 2011-01-05 刘春喜 Process for purifying and recycling hot water by membrane method
CN204369669U (en) * 2014-09-28 2015-06-03 星达(泰州)膜科技有限公司 A kind of nanofiltration membrane purifier
CN104591451A (en) * 2014-12-25 2015-05-06 江苏水智乐自动化设备有限公司 Tap water purification system

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