CN102259995A - Integrated treatment process for processing rural standard exceeding drinking-water - Google Patents
Integrated treatment process for processing rural standard exceeding drinking-water Download PDFInfo
- Publication number
- CN102259995A CN102259995A CN 201110192437 CN201110192437A CN102259995A CN 102259995 A CN102259995 A CN 102259995A CN 201110192437 CN201110192437 CN 201110192437 CN 201110192437 A CN201110192437 A CN 201110192437A CN 102259995 A CN102259995 A CN 102259995A
- Authority
- CN
- China
- Prior art keywords
- water
- turbidity
- drinking
- treatment process
- standard
- 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
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention relates to an integrated treatment process for processing rural standard exceeding drinking-water, comprising the following steps of: (1) carrying out a conventional deposition treatment on the standard-exceeding raw water in a water-storage buffer pool to obtain water with the turbidity being less than or equal to 100 NTU; (2) allowing the water with the turbidity being less than or equal to 100 NTU to pass through a water-feeding pump and enter into a multiple-media filter so as to obtain water with the turbidity being less than or equal to 1 NTU and with SDI being less than 3; (3) adding a scale inhibitor into the water with the turbidity being less than or equal to 1 NTU and with SDI being less than 3 by a dosing system, fully mixing, adding hydrochloric acid to make the pH value of the mixed liquid to be 6.8-7.2 so as to obtain water which undergoes acid adjustment; (4) allowing the water which undergo acid adjustment to successively pass through a precision filter and a pressure pump and enter into a membrane module filtration system for filtering so as to obtain fresh water; (5) sterilizing the fresh water by adopting a UV sterilizer to obtain the standard drinking water. According to the invention, by the comprehensive utilization of advanced and applicative water treatment technologies of filtering, adsorption and sterilization as well as devices thereof with the combination of membrane technologies of microfiltration, ultrafiltration, nanofiltration and the like, the rural safe drinking-water which accords with the ''Sanitary Standards for Drinking Water Quality'' is processed.
Description
Technical field
The present invention relates to the tap water water treatment field, relate in particular to a kind of integrated treatment process that the rural area exceeds standard and drinks water of handling.
Background technology
In the human body 70%~80%, moisture, the water quality that long-term drinking is bad, can cause that physique is not good, resistibility weakens naturally, then all kinds of diseases and ailments are inevitable, moreover the pollutent of long-term accumulated is when arriving health and can't bear, brilliant again doctor, more effectively medicine probably also difficulty prove effective, so the saying of " king that water is hundred medicines " is arranged.Estimate according to " rural potable water safety and sanitation assessment indicator system ", the aggregate level of China's Rural water supply is not high, and there still have people more than 300,000,000 to drink water to be dangerous, having a strong impact on the masses' healthy and orthobiosis.Because water body is contaminated to be on the rise, particularly organic pollution adopts conventional precipitation, filtration, sterilization only can remove 20% organic pollutant, and therefore, the deep purifying treatment industry of Drinking Water in China obtains flourish under this background.
The deep purifying of water mainly adopts following several mode: charcoal absorption---and the charcoal absorption water purification technology is the high efficiency of additive capability that utilizes gac, removes stink, organism, phenol, alkylbenzene sulfonate, disinfection byproduct (DBP), heavy metal ion and other micro-objectionable impuritiess in the water.Secondary filter---secondary filter is to use accurate filter that water is filtered, and it can be removed the impurity particle scope and look the kind of accurate filter and difference, and accurate filter is commonly used in water treatment candle filter and a pre-filming filter.What the filter core element of candle filter was commonly used is porous ceramics and polypropylene fibre, can remove the particle more than 2~5 microns; Pre-filming filter is commonly used diatomite filtration, before filtering to filter element precoating diatomite form 2~-filter membrane that 3mm is thick, can remove colloidal solid, bacterium, part virus and larger molecular organics.Membrane sepn treatment technology---membrane sepn is a kind of under certain impellent effect, utilizes the through performance of certain films to divide the technology of ion, molecule and impurity in dried up.It has separation efficiency height, no phase transformation, no chemical transformation, simplicity of design, characteristics such as easy to operate and energy-conservation.Membrane technique is a new technology of the research and development fifties.China is applied to sea water desaltination with this technology at first, is used for the preparation (semi-conductor, biology, medicine, beverage, microelectronics) of industrial pure water then.Be used for the preparation of tap water the beginning of the nineties in last century.
China's membrane separation technique is started late, and also is in the infancy at present.The membrane separation technique that with pressure is motivating force has reverse osmosis, nanofiltration, ultrafiltration and micro-filtration.
Wherein: micro-filtration (MF)---micro-filtration accounts for 40%~50% at present on market, and the filter membrane aperture is 0.05~5.00 μ m, and the operation transmembrane pressure is 0.1~0.3Mpa, is suitable for that falling of liquid medium is turbid most, degerming handles, and can remove 10
-6Impurity, greatly reduce the turbidity of water, especially to good iron removal effect.Bacterium detention rate is generally used for producing the end processing of high purity water up to 99.9%.
Ultrafiltration (UF)---ultrafiltration can remove in the water 10
-9(nano level) particulate matter can directly prepare drink water, also can do reverse osmosis, nanofiltration pre-treatment, and the transmembrane pressure of operation is 0.3~1.0Mpa; Ultrafiltration is mainly used in molecular weight removing greater than 6000 larger molecular organics.More than the water handled of two kinds of methods all keep mineral substance and trace element in the water.
Reverse osmosis (RO)---reverse osmosis technology is that industrial sectors such as electronics, medicine, chemical industry prepare one of major technique of pure water.The advanced treatment that is used for tap water in recent years in a large number.The aperture of reverse osmosis membrane about 10
-11~10, can remove in the water almost all materials, comprise various suspended substances, micelle, organism, bacterium, virus, mineral substance, pyrogen etc.
Other treatment processs---as distillation method, electroosmose process, ion exchange method etc.The general treatment process of these methods is relatively complicated, and the cost for the treatment of water is higher.
Therefore, along with the continuous development of membrane science technology, adopting efficient, economic membrane integrating technique purifying treatment brackish water will be an important directions of rural potable water treatment technology Future Development.
Summary of the invention
It is simple that technical problem to be solved by this invention provides a kind of technology, the processing rural area that can be applicable to different areas, the dissimilar water that the exceeds standard integrated treatment process of drinking-water that exceeds standard.
For addressing the above problem, a kind of integrated treatment process that the rural area exceeds standard and drinks water of handling of the present invention may further comprise the steps:
(1) the former water that will exceed standard carries out conventional precipitation process in the water storage Buffer Pool, obtains the water of turbidity≤100NTU;
(2) water with described turbidity≤100NTU enters more medium filter through service pump, obtains the water of turbidity≤1NTU and SDI<3;
(3) add Scale inhibitors by medicine system in the water of described turbidity≤1NTU and SDI<3, behind thorough mixing, add mass concentration and be 36% hydrochloric acid, making the pH value of mixed solution is 6.8~7.2, obtains the water after the acid adjustment;
(4) water after the described acid adjustment is entered the membrane module filtering system successively behind accurate filter, force (forcing) pump and filter, obtain fresh water;
(5) adopt the ultraviolet Sterilizers to carry out disinfection described fresh water after, promptly get the standard tap water.
More medium filter in the described step (2) is meant by one deck quartz sand one deck hard coal, from big to small, the multilayer level strainer that rearranges from down to up.
Accurate filter in the described step (4) is meant that the filter core material is that polypropylene, filtering accuracy are the strainer of 5 μ m~10 μ m.
Membrane module filtering system in the described step (4) is to be that the microfiltration membrane of 0.05~5.00 μ m, ultra-filtration membrane, molecular weight cut-off that the aperture is 0.001~0.02 μ m are the filtering system that 200~800 nanofiltration membrane composes in parallel by the aperture.
It is the fluorescent tube of 11w or 16w that ultraviolet Sterilizers in the described step (5) adopts power.
The present invention compared with prior art has the following advantages:
Membrane technique technology assembled configuration such as water technologies such as 1, the advanced and applicable filtration of integrated use of the present invention, absorption, sterilization and device and micro-filtration, ultrafiltration, nanofiltration, at the water quality that sense organ, toxicology, bacteriology, chemical index exceed standard, handle out the rural safe drinking water that meets " drinking water sanitary standard ".
2, because the present invention has also carried out acid adjustment after adding Scale inhibitors, therefore, help the use of subsequent film assembly filtering system, also prevent fouling simultaneously.
3, technology of the present invention is simple, can be applicable to different areas, the dissimilar water that exceeds standard.
Embodiment
A kind of handle the rural area exceed standard drinking-water integrated treatment process, may further comprise the steps:
(1) the former water that will exceed standard carries out conventional precipitation process in the water storage Buffer Pool, to remove large granular impurity and coagulation, reduces the turbidity that exceeds standard, and obtains the water of turbidity≤100NTU.
(2) water with turbidity≤100NTU enters more medium filter through service pump, to remove colloidalmaterial, suspended substance solid particulate, silt, part larger molecular organics matter and microorganism, obtains the water of turbidity≤1 NTU and SDI<3.
Wherein: more medium filter is meant by one deck quartz sand one deck hard coal, from big to small, the multilayer level strainer that rearranges from down to up.
(3) add Scale inhibitors by medicine system in the water of turbidity≤1 NTU and SDI<3, behind thorough mixing, add mass concentration and be 36% hydrochloric acid, making the pH value of mixed solution is 6.8~7.2, obtains the water after the acid adjustment.
(4) water after the acid adjustment is entered the membrane module filtering system successively behind accurate filter, force (forcing) pump and filter, obtain fresh water.
Wherein: accurate filter is meant that the filter core material is that polypropylene, filtering accuracy are the strainer of 5 μ m~10 μ m.
The membrane module filtering system is to be that the microfiltration membrane of 0.05~5.00 μ m, ultra-filtration membrane, molecular weight cut-off that the aperture is 0.001~0.02 μ m are the filtering system that 200~800 nanofiltration membrane composes in parallel by the aperture.
(5) fresh water is adopted the ultraviolet Sterilizers carry out disinfection after, promptly get the standard tap water.It is the fluorescent tube of 11w or 16w that its medium ultraviolet Sterilizers adopts power.
Claims (5)
1. handle the integrated treatment process that the rural area exceeds standard and drinks water for one kind, may further comprise the steps:
(1) the former water that will exceed standard carries out conventional precipitation process in the water storage Buffer Pool, obtains the water of turbidity≤100NTU;
(2) water with described turbidity≤100NTU enters more medium filter through service pump, obtains the water of turbidity≤1NTU and SDI<3;
(3) add Scale inhibitors by medicine system in the water of described turbidity≤1NTU and SDI<3, behind thorough mixing, add mass concentration and be 36% hydrochloric acid, making the pH value of mixed solution is 6.8~7.2, obtains the water after the acid adjustment;
(4) water after the described acid adjustment is entered the membrane module filtering system successively behind accurate filter, force (forcing) pump and filter, obtain fresh water;
(5) adopt the ultraviolet Sterilizers to carry out disinfection described fresh water after, promptly get the standard tap water.
2. a kind of exceed standard integrated treatment process of drinking-water of rural area of handling as claimed in claim 1 is characterized in that: the more medium filter in the described step (2) is meant by one deck quartz sand one deck hard coal, from big to small, the multilayer level strainer that rearranges from down to up.
3. a kind of integrated treatment process that the rural area exceeds standard and drinks water of handling as claimed in claim 1, it is characterized in that: the accurate filter in the described step (4) is meant that the filter core material is that polypropylene, filtering accuracy are the strainer of 5 μ m~10 μ m.
4. a kind of exceed standard integrated treatment process of drinking-water of rural area of handling as claimed in claim 1 is characterized in that: the membrane module filtering system in the described step (4) is to be that the microfiltration membrane of 0.05~5.00 μ m, ultra-filtration membrane, molecular weight cut-off that the aperture is 0.001~0.02 μ m are the filtering system that 200~800 nanofiltration membrane composes in parallel by the aperture.
5. a kind of integrated treatment process that the rural area exceeds standard and drinks water of handling as claimed in claim 1, it is characterized in that: it is the fluorescent tube of 11w or 16w that the ultraviolet Sterilizers in the described step (5) adopts power.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201110192437 CN102259995A (en) | 2011-07-05 | 2011-07-05 | Integrated treatment process for processing rural standard exceeding drinking-water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201110192437 CN102259995A (en) | 2011-07-05 | 2011-07-05 | Integrated treatment process for processing rural standard exceeding drinking-water |
Publications (1)
Publication Number | Publication Date |
---|---|
CN102259995A true CN102259995A (en) | 2011-11-30 |
Family
ID=45006869
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 201110192437 Pending CN102259995A (en) | 2011-07-05 | 2011-07-05 | Integrated treatment process for processing rural standard exceeding drinking-water |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN102259995A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106186432A (en) * | 2016-08-18 | 2016-12-07 | 成都振中电气有限公司 | A kind of drinking water immediate processing method |
CN106542674A (en) * | 2016-12-08 | 2017-03-29 | 苏州陈恒织造有限公司 | A kind of distributing rural domestic sewage treatment circulating device |
CN106542675A (en) * | 2016-12-08 | 2017-03-29 | 苏州陈恒织造有限公司 | A kind of distributing treatment method for rural sewage |
CN111675376A (en) * | 2020-06-09 | 2020-09-18 | 安徽名膜环境技术有限公司 | Integrated intensive distribution type drinking water purification and supply process and device |
CN114538693A (en) * | 2022-03-14 | 2022-05-27 | 大连博斯特科技有限公司 | Cleaning agent regeneration method for antirust surface cleaning process |
-
2011
- 2011-07-05 CN CN 201110192437 patent/CN102259995A/en active Pending
Non-Patent Citations (1)
Title |
---|
《甘肃科技》 20080229 赵虎群等 "西北民族大学苦咸水淡化工程设计概述" 第60-62,88页 1-5 第24卷, 第4期 * |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106186432A (en) * | 2016-08-18 | 2016-12-07 | 成都振中电气有限公司 | A kind of drinking water immediate processing method |
CN106542674A (en) * | 2016-12-08 | 2017-03-29 | 苏州陈恒织造有限公司 | A kind of distributing rural domestic sewage treatment circulating device |
CN106542675A (en) * | 2016-12-08 | 2017-03-29 | 苏州陈恒织造有限公司 | A kind of distributing treatment method for rural sewage |
CN111675376A (en) * | 2020-06-09 | 2020-09-18 | 安徽名膜环境技术有限公司 | Integrated intensive distribution type drinking water purification and supply process and device |
CN114538693A (en) * | 2022-03-14 | 2022-05-27 | 大连博斯特科技有限公司 | Cleaning agent regeneration method for antirust surface cleaning process |
CN114538693B (en) * | 2022-03-14 | 2023-11-07 | 大连博斯特科技有限公司 | Cleaning agent regeneration method for rust-proof surface cleaning process |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Tang et al. | Role of dissolved organic matters (DOM) in membrane fouling of membrane bioreactors for municipal wastewater treatment | |
Yu et al. | Investigation of pre-coagulation and powder activate carbon adsorption on ultrafiltration membrane fouling | |
Yu et al. | Application of pulsed UV-irradiation and pre-coagulation to control ultrafiltration membrane fouling in the treatment of micro-polluted surface water | |
Konieczny et al. | A coagulation–MF system for water treatment using ceramic membranes | |
Cornelissen et al. | Effect of anionic fluidized ion exchange (FIX) pre-treatment on nanofiltration (NF) membrane fouling | |
CN102259995A (en) | Integrated treatment process for processing rural standard exceeding drinking-water | |
Liang et al. | Performance evaluation of water treatment ultrafiltration pilot plants treating algae-rich reservoir water | |
WO2003106348A1 (en) | Methods for reducing boron concentration in high salinity liquid | |
CN100490953C (en) | Ceramic-diaphragm seawater pretreating method | |
Qin et al. | Reservoir water treatment using hybrid coagulation–ultrafiltration | |
CN201686578U (en) | Medical water purifying machine | |
CN111072193A (en) | Ultrafiltration mineral water production system | |
Bujakowski et al. | Geothermal water treatment–preliminary experiences from Poland with a global overview of membrane and hybrid desalination technologies | |
Jeong et al. | Submerged membrane coagulation hybrid system as pretreatment to organic matter removal from seawater | |
László et al. | Purification of thermal wastewater by membrane separation and ozonation | |
CN201452883U (en) | Direct drinking machine in public | |
Chen et al. | Combination of microalgae cultivation with membrane processes for the treatment of municipal wastewater | |
CN103274547B (en) | Deep purification method for removing soluble pollutant from drinking water | |
Abdallah et al. | Design of low energy integrated membranes units for production of highly purified water | |
Malhas et al. | Application of ultrafiltration membrane-embedded activated carbon-filter in Kuwait wastewater treatment in comparison with a conventional method | |
Aly et al. | Application of ultra-filtration technique as a water purification technology in Egypt-case study | |
Johir et al. | Hybrid filtration method for pre-treatment of stormwater | |
WO2013061057A1 (en) | Water treatment methods and systems | |
Jianping et al. | Pilot study of ultrafiltration-nanofiltration process for the treatment of raw water from Huangpu river in China | |
Helmer et al. | Feedbacks on performance tests with filtralite media® compared to conventional media filters at pilot scale |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20111130 |