CN1233594A - Method for producing purified and mineralizd water - Google Patents
Method for producing purified and mineralizd water Download PDFInfo
- Publication number
- CN1233594A CN1233594A CN 99105060 CN99105060A CN1233594A CN 1233594 A CN1233594 A CN 1233594A CN 99105060 CN99105060 CN 99105060 CN 99105060 A CN99105060 A CN 99105060A CN 1233594 A CN1233594 A CN 1233594A
- Authority
- CN
- China
- Prior art keywords
- water
- mineralizer
- filtration
- mineralized
- mineralizd
- 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
Links
Landscapes
- Water Treatment By Sorption (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Treatment Of Water By Ion Exchange (AREA)
Abstract
The prepn. method of pure mineralized water is as follows: firstly, ordinary clean water is purified, then mineralize the purified water in an mineralization apparatus with condition simulated to the geological structure 200 meter deep underground and high temp. high pressure and existence of carbon dioxide, and then passes through precipitation, filtration, active carbon adsorption, blending with main elements, sterilization to obtain the product.
Description
The present invention relates to a kind of manufacture method of health-care drinking-water.
Along with the continuous development of country's industry, environmental pollution is serious day by day, and the pollution of water stands in the breach, so drinking free of contamination water is the important assurance healthy to people.Pure water be a kind of be raw material with the ortho-water, through the artificial tap water that is similar to pure water that obtains of making.Because in manufacturing processed, the harmful pollution substance in the water and nutritive substances such as human body beneficial's constant and trace element are removed together though such tap water is harmless, can not provide the nutrition of needed by human to human body.
The object of the present invention is to provide a kind of manufacturing neither to contain pollution substance, can guarantee the method for the purified and mineralizd water of nutrition contents such as the constant of needed by human and trace element again.
Technical scheme of the present invention is that the ortho-water of cleaning is made the pure water that is similar to pure water, with under the underground 200 meters dark geologic frameworks of pure water simulation in mineralizer and High Temperature High Pressure and the geologic condition that has carbonic acid gas to exist pure water being carried out mineralising, obtain finished product through precipitation, filtration, activated carbon adsorption, blending, sterilization etc. more then.
Concrete technical process of the present invention is as follows:
A, will be through precipitation, filtering common clean water purify with ordinary method, obtain pure water;
B, above-mentioned pure water is input in the mineralizer, after purifying, import carbonic acid gas and Air mixing gas in the mineralizer simultaneously, carbonic acid gas: air=1～3: 3～1, the temperature of charge of mineralizer is controlled at 45～90 ℃, with pressure-controlling at 2～20gk/cm
2, its mineralising time is controlled according to the water speed that goes out of mineralizer, and it is little to go out little speed, and the mineralising time is just long, and the salinity of water is just high, on the contrary salinity is just low;
C, with above-mentioned 6～12 hours after-filtration of mineralized water precipitation that meet salinity that obtain;
D, the mineralized water after the above-mentioned filtration is passed through charcoal filter;
E, will be through the content of its master control element of mineralized water sample examination of activated carbon adsorption, compare with the content of the master control element of product requirement again, add to be in harmonious proportion to supply differing constituent content and concoct with compound;
F, the mineralized water after will being in harmonious proportion filter with the silicon dried soil filter earlier, filter with sand filtration rod device again;
G, above-mentioned filtering mineralized water is heated to more than 85 ℃ insulation sterilization half an hour;
H, can under uviolizing.
Among the present invention, can adopt in the methods such as electroosmose process, ion exchange method, distillation method, reverse osmosis method one or both that common clean water is purified.
The present invention within the specific limits, the parameters such as content of the salinity of water carbonic acid gas during along with mineralising time, mineralising temperature, mineralising pressure, mineralising increase and increase.
Among the present invention, the compound of master control constituent content of being used to be in harmonious proportion has: sodium-chlor, sodium bicarbonate, calcium chloride, lime carbonate, magnesium chloride, magnesiumcarbonate, salt of wormwood, zinc chloride, zinc sulfate, sodium selenate etc.
Principal feature of the present invention is: removed all contaminations matter harmful in the ortho-water effectively 1.; 2. because processing condition are the mineralising conditions that simulate underground 200 meters depths, so the purified and mineralizd water that obtains can match in excellence or beauty with natural high quality mineral water; 3. the content of carbonic acid gas all can artificially be controlled during owing to the ore structure of dosing in the mineralizer, mineralising temperature, mineralising pressure, mineralising time, mineralising, thus can produce dissimilar mineralized waters, thus replace dissimilar high quality mineral water; 4. the purified and mineralizd water of producing not only contains nutritive substances such as the constant of needed by human and trace element, and is weakly alkaline, more helps the health of human body.
Below in conjunction with embodiment the present invention is described in more detail.
Embodiment 1:
A kind of manufacture method of low mineralization purified and mineralizd water.The master control element index of this purified and mineralizd water is:
PH value 7～7.8 total hardnesss (in lime carbonate) PPM 33
Calcium PPM 9 magnesium PPM 2
Potassium PPM 2 sodium PPM 9
Chlorine PPM 7 zinc PPM 1
Selenium PPM 0.5
The manufacture method of this purified and mineralizd water is as follows:
A, will through the precipitation, filtration, purification common clean water purify with electroosmose process, obtain pure water;
B, lime stone rockfills in above-mentioned pure water is input to: medical stone: in the mineralizer of long phosphate stone=2.5: 1: 15, after purifying, import carbonic acid gas and Air mixing gas in the mineralizer simultaneously, carbonic acid gas is 1: 2 with the ratio of air, the temperature of charge of mineralizer is controlled at 50 ± 2 ℃, and pressure-controlling is at 5 ± 1kg/cm
2, the mineralized water Hardness Control that flows out mineralizer is in the hardness (getting 35PPM) a little more than the master control index, low as hardness, then reduce the discharge of mineralized water, as the hardness height, then strengthen the discharge of mineralized water, till effusive mineralized water hardness meets the master control index request;
C, with 8 hours after-filtration of above-mentioned mineralized water precipitation;
D, the mineralized water after the above-mentioned filtration is adsorbed by charcoal filter;
E, will be through the content of its master control element of mineralized water sample examination of activated carbon adsorption, compare with the content of the master control element of product requirement again, add to be in harmonious proportion to supply differing constituent content and be in harmonious proportion with compound;
F, the mineralized water after will being in harmonious proportion filter with the silicon dried soil filter earlier, filter with sand filtration rod device again;
G, the filterable mineralized water of above-mentioned mistake is heated to more than 85 ℃ insulation sterilization half an hour;
H, can under uviolizing.
Embodiment 2:
The manufacture method of salinity purified and mineralizd water in a kind of.The master control element index of this purified and mineralizd water is:
PH value 7.2～7.8 total hardnesss (in lime carbonate) PPM 82
Calcium PPM 23 magnesium PPM 6
Potassium PPM 2 sodium PPM 18
Chlorine PPM 24 zinc PPM 2
Selenium PPM 1
The manufacture method of this purified and mineralizd water is as follows:
A, will through the precipitation, the common clean water ion-exchange purification of filtration, purification obtains pure water;
B, fill out vermiculite in above-mentioned pure water is input to: long phosphate stone: in the mineralizer of rhombspar=1.5: 1: 1.8, after purifying, import carbonic acid gas and Air mixing gas in the mineralizer simultaneously, carbonic acid gas is 2: 3 with the ratio of air, the temperature of charge of mineralizer is controlled at 65 ± 2 ℃, and pressure-controlling is at 12 ± 1kg/cm
2, the mineralized water Hardness Control that flows out mineralizer is at 85PPM, low as hardness, reduce the discharge of mineralized water, as the hardness height, then strengthen the discharge of mineralized water, till effusive mineralized water hardness meets the master control index request; Following operation is identical with the operation of c～h among the embodiment 1.
Embodiment 3:
A kind of manufacture method of high salinity purified and mineralizd water.The master control element index of this purified and mineralizd water is:
PH value 7.4～8.2 total hardnesss (in lime carbonate) PPM 157
Calcium PPM 50 magnesium PPM 8
Potassium PPM 3 sodium PPM 13
Chlorine PPM 50 zinc PPM 2
Selenium PPM 1
The manufacture method of this purified and mineralizd water is as follows:
A, will through the precipitation, filtration, purification common clean water purify with distillation method, obtain pure water;
B, fill out medical stone in above-mentioned pure water is input to: Black Warrior stone: in the mineralizer of vermiculite=1: 3.5: 2.5, after purifying, import carbonic acid gas and Air mixing gas in the mineralizer simultaneously, carbonic acid gas is 3: 2 with the ratio of air, and pressure-controlling is at 18 ± 1kg/cm
2, the mineralized water Hardness Control that flows out mineralizer is at 160PPM, low as hardness, reduce the discharge of mineralized water, as the hardness height, then strengthen the discharge of mineralized water, till effusive mineralized water hardness meets the master control index request; Following operation is identical with the operation of c～h among the embodiment 1.
Claims (2)
1, a kind of manufacture method of purified and mineralizd water is characterized in that:
A. will be through precipitation, the common clean water of filtration, purification purifies with ordinary method, obtains pure water;
B. above-mentioned pure water is input in the mineralizer, after purifying, import carbonic acid gas and Air mixing gas in the mineralizer simultaneously, carbonic acid gas: air=1～3: 3～1, the temperature of charge of mineralizer is controlled at 45～90 ℃, with pressure-controlling at 2～20kg/cm
2, its mineralising time is controlled according to the water speed that goes out of mineralizer;
C. with above-mentioned 6～12 hours after-filtration of mineralized water precipitation that meet salinity that obtain;
D. the mineralized water after the above-mentioned filtration is passed through charcoal filter;
E. will be through the content of its master control element of mineralized water sample examination of activated carbon adsorption, compare with the content of the master control element of product requirement again, add to be in harmonious proportion to supply differing constituent content and concoct with compound;
F, the mineralized water after will being in harmonious proportion filter with the silicon dried soil filter earlier, filter with sand filtration rod device again;
G, above-mentioned filtering mineralized water is heated to more than 85 ℃ insulation sterilization half an hour;
H, can under uviolizing.
2, the manufacture method of a kind of purified and mineralizd water according to claim 1, it is characterized in that: the compound of master control constituent content of being used to be in harmonious proportion has sodium-chlor, sodium bicarbonate, calcium chloride, lime carbonate, magnesium chloride, magnesiumcarbonate, salt of wormwood, zinc chloride, zinc sulfate, sodium selenate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 99105060 CN1091430C (en) | 1999-04-09 | 1999-04-09 | Method for producing purified and mineralizd water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 99105060 CN1091430C (en) | 1999-04-09 | 1999-04-09 | Method for producing purified and mineralizd water |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1233594A true CN1233594A (en) | 1999-11-03 |
| CN1091430C CN1091430C (en) | 2002-09-25 |
Family
ID=5271877
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 99105060 Expired - Fee Related CN1091430C (en) | 1999-04-09 | 1999-04-09 | Method for producing purified and mineralizd water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1091430C (en) |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1296289C (en) * | 2005-04-20 | 2007-01-24 | 黄玉霖 | Concentrated water of natural mineral matter and method of preparation |
| CN1850280B (en) * | 2006-05-17 | 2013-07-10 | 潘见 | Gas-synergic super-high-pressure sterilizing method for liquid material |
| CN103702947A (en) * | 2011-07-22 | 2014-04-02 | Omya国际股份公司 | Micronized CaCo3 slurry injection system for the remineralization of desalinated and fresh water |
| CN103827044A (en) * | 2011-08-31 | 2014-05-28 | Omya国际股份公司 | Remineralization of desalinated and of fresh water by dosing of a calcium carbonate solution in soft water |
| CN103876239A (en) * | 2014-04-04 | 2014-06-25 | 程正勇 | Selenium-rich water mineralization agent as well as application and preparation method thereof |
| CN104098168A (en) * | 2014-08-07 | 2014-10-15 | 李玉林 | Post-processing purified water pH value adjustment method adopting simulated deep natural mineral water environment |
| CN104692514A (en) * | 2014-12-31 | 2015-06-10 | 浙江至美环境科技有限公司 | Granular mineralizer for conditioning desalted water as well as preparation method and application of granular mineralizer |
| CN104926007A (en) * | 2015-06-03 | 2015-09-23 | 安徽野岭饮料食品有限公司 | Production process of spring water in Dabie mountain area |
| CN104921241A (en) * | 2015-06-03 | 2015-09-23 | 安徽野岭饮料食品有限公司 | Production technology of mineral water |
| CN105246838A (en) * | 2013-05-24 | 2016-01-13 | Omya国际股份公司 | Multiple batch system for the preparation of a solution of calcium hydrogen carbonate suitable for the remineralization of desalinated water and of naturally soft water |
| CN106608692A (en) * | 2015-10-23 | 2017-05-03 | 天津科技大学 | Efficient and controllable desalinated seawater mineralization process |
| CN111392935A (en) * | 2020-03-16 | 2020-07-10 | 青岛百发海水淡化有限公司 | Mineralization device in double-membrane seawater desalination process |
-
1999
- 1999-04-09 CN CN 99105060 patent/CN1091430C/en not_active Expired - Fee Related
Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1296289C (en) * | 2005-04-20 | 2007-01-24 | 黄玉霖 | Concentrated water of natural mineral matter and method of preparation |
| CN1850280B (en) * | 2006-05-17 | 2013-07-10 | 潘见 | Gas-synergic super-high-pressure sterilizing method for liquid material |
| CN103702947A (en) * | 2011-07-22 | 2014-04-02 | Omya国际股份公司 | Micronized CaCo3 slurry injection system for the remineralization of desalinated and fresh water |
| CN106006912A (en) * | 2011-07-22 | 2016-10-12 | Omya国际股份公司 | MICRONIZED CaCO3 SLURRY INJECTION SYSTEM FOR THE REMINERALIZATION OF DESALINATED AND FRESH WATER |
| CN103702947B (en) * | 2011-07-22 | 2016-06-08 | Omya国际股份公司 | Micronization CaCO for demineralized water and the remineralization of fresh water3Serosity injected system |
| CN103827044A (en) * | 2011-08-31 | 2014-05-28 | Omya国际股份公司 | Remineralization of desalinated and of fresh water by dosing of a calcium carbonate solution in soft water |
| CN103827044B (en) * | 2011-08-31 | 2017-03-22 | Omya国际股份公司 | Remineralization of desalinated and of fresh water by dosing of a calcium carbonate solution in soft water |
| CN105246838A (en) * | 2013-05-24 | 2016-01-13 | Omya国际股份公司 | Multiple batch system for the preparation of a solution of calcium hydrogen carbonate suitable for the remineralization of desalinated water and of naturally soft water |
| CN105246838B (en) * | 2013-05-24 | 2018-02-06 | Omya国际股份公司 | For preparing more batches of systems of the calcium bicarbonate solution suitable for remineralization desalted water and natural soft water |
| CN103876239A (en) * | 2014-04-04 | 2014-06-25 | 程正勇 | Selenium-rich water mineralization agent as well as application and preparation method thereof |
| CN103876239B (en) * | 2014-04-04 | 2015-09-09 | 程正勇 | Rich selenium water mineralizer and application thereof and preparation method |
| CN104098168B (en) * | 2014-08-07 | 2015-11-18 | 李玉林 | Pure water adopts the rearmounted pH value control method of the profound natural mineral water environment of simulation |
| CN104098168A (en) * | 2014-08-07 | 2014-10-15 | 李玉林 | Post-processing purified water pH value adjustment method adopting simulated deep natural mineral water environment |
| CN104692514A (en) * | 2014-12-31 | 2015-06-10 | 浙江至美环境科技有限公司 | Granular mineralizer for conditioning desalted water as well as preparation method and application of granular mineralizer |
| CN104921241A (en) * | 2015-06-03 | 2015-09-23 | 安徽野岭饮料食品有限公司 | Production technology of mineral water |
| CN104926007A (en) * | 2015-06-03 | 2015-09-23 | 安徽野岭饮料食品有限公司 | Production process of spring water in Dabie mountain area |
| CN106608692A (en) * | 2015-10-23 | 2017-05-03 | 天津科技大学 | Efficient and controllable desalinated seawater mineralization process |
| CN111392935A (en) * | 2020-03-16 | 2020-07-10 | 青岛百发海水淡化有限公司 | Mineralization device in double-membrane seawater desalination process |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1091430C (en) | 2002-09-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Kut et al. | A review of fluoride in African groundwater and local remediation methods | |
| CN1091430C (en) | Method for producing purified and mineralizd water | |
| RU2013110842A (en) | THE SYSTEM OF INTRODUCING SUSPENSION OF FINE CASCO3 FOR REMINERALIZATION OF SALTED AND FRESH WATER | |
| CA2028497A1 (en) | Composition for chemical and biological treatment of polluted water, and preparation process therefor | |
| Nemade et al. | Removal of fluorides from water using low cost adsorbents | |
| CN105366781A (en) | Water purification composite flocculating agent and preparation method and use method thereof | |
| CN112456654A (en) | Preparation method and application of biological seed crystal and method for synchronously removing calcium and fluorine in underground water | |
| CN2848838Y (en) | Nano-filtering membrane composite deep water purification device | |
| RU2483034C2 (en) | Composition for reducing water hardness | |
| CN1210212C (en) | Method for treating and activating sea water and polluted water into drinking water | |
| Ayoub et al. | Coagulation of alkalinized municipal wastewater using seawater bittern | |
| CN107021580B (en) | Method for recycling waste liquid generated after extracting tigogenin from sisal hemp | |
| CN1082033C (en) | Method for improving pH value during prodn. of purified water | |
| RU2309126C1 (en) | Method of production of the mineral medical-table drinking water "akseenya" | |
| CN1268488A (en) | High-quality drinking water prodn. with controlled mineral content | |
| CN111392934A (en) | Double-membrane seawater desalination process | |
| RU2185328C2 (en) | Method of purification and conditioning of potable water and media for method embodiment | |
| CN101049994A (en) | Ion exchanger of natural mineral for seawater desalination | |
| CH715543B1 (en) | Method and device for supplying purified, remineralized water. | |
| JPH11319411A (en) | Water cleaning agent containing shell fossil and water cleaning method using the agent | |
| CN85105155A (en) | The manufacture method of mineral water and device thereof | |
| Moloi et al. | Journal/South African Journal of Science/Vol. 120 No. 1/2 (2024)/Articles Open Access | |
| Al-Rawajfeh et al. | Enhancement effect of phosphate and silicate on water defluoridation by calcined gypsum | |
| Kaur et al. | Health impacts due to fluoride contamination in water: current scenario | |
| CN107662973A (en) | A kind of remover of chlorion |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |