CN1091430C - Method for producing purified and mineralizd water - Google Patents
Method for producing purified and mineralizd water Download PDFInfo
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- CN1091430C CN1091430C CN 99105060 CN99105060A CN1091430C CN 1091430 C CN1091430 C CN 1091430C CN 99105060 CN99105060 CN 99105060 CN 99105060 A CN99105060 A CN 99105060A CN 1091430 C CN1091430 C CN 1091430C
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Abstract
The present invention relates to a method for producing health drinking water. A method for producing purified and mineralized water comprises: firstly, ordinary clean water is purified into purified water; then, the purified water is mineralized in a mineralizing device by simulating an underground geological structure as deep as 200 meters at high temperature and high pressure under the geological condition that carbon dioxide exists; the purified water is treated by precipitation, filtration, activated carbon adsorption, preparation by main control elements, sterilization, etc. for obtaining a finished product. The purified and mineralized water does not pollute substances, and ensures human necessary the content of nutrient substances, such as constant elements, trace elements, etc.; the purified and mineralized water is health drinking water superior to natural mineral water with good quality.
Description
Technical field
The present invention relates to a kind of manufacture method of health-care drinking-water.
Background technology
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.
Summary of the invention
The object of the present invention is to provide a kind of manufacturing both not conform to 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, then pure water is carried out mineralising to pure water under 200 meters dark geologic frameworks of simulate formation and High Temperature High Pressure and the geologic condition that has carbonic acid gas to exist in mineralizer, obtain finished product through precipitation, filtration, activated carbon adsorption, blending, sterilization etc. again.
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 (mol ratio)=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, and it is little to go out water 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 with compound and to differ constituent content and concoct, wherein the master control element is controlled in the following scope (unit is a mg/litre):
Potassium 0.1-20mg/L chlorine 0.01-3mg/L selenium 0.01-1mg/L lithium 0.5-5mg/L sodium 0.1-8mg/L zinc 0.2-5mg/L magnesium 0.1-5mg/L strontium 0.2-10mg/L iodine 0.2-5mg/L calcium 1-5mg/L;
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.
What the master control constituent content was high is medical mineralized water, and what the master control constituent content was low is to drink mineralized water.
Principal feature of the present invention is: 1, removed all contaminations matter harmful in the ortho-water effectively; 2, because processing condition are mineralising conditions of 200 meters depths of simulate formation, so the purified and mineralizd water that obtains can match in excellence or beauty with natural high quality mineral water; The content of carbonic acid gas all can artificially be controlled during 3, 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.
Embodiment
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: 1.5, after purifying, import carbonic acid gas and Air mixing gas in the mineralizer simultaneously, carbonic acid gas is 1: 2 with the ratio (mol 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
PPM 1
The manufacture method of this purified and mineralizd water is as follows:
A, will through the precipitation, filtration, purification common clean water ion-exchange purification, obtain 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, after purifying, import carbonic acid gas and Air mixing gas in the mineralizer simultaneously, carbonic acid gas is 2: 3 with the ratio (mol 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,, then strengthen the discharge of mineralized water as the hardness height, till effusive mineralized water hardness met the master control index request, above operation was 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, the ratio of carbonic acid gas and air (mol ratio) is 3: 2, 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,, then strengthen the discharge of mineralized water as the hardness height, till effusive mineralized water hardness met the master control index request, above operation was identical with the operation of c～h among the embodiment 1.
Claims (1)
1, a kind of manufacture method of purified and mineralizd water is characterized in that:
A, process 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, the mol ratio of carbonic acid gas and 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 with compound and to differ constituent content and concoct, wherein the master control element is controlled in the scope that following unit is a mg/litre:
Potassium 0.1-20mg/L chlorine 0.01-3mg/L selenium 0.01-1mg/L lithium 0.5-5mg/L sodium 0.1-8mg/L zinc 0.2-5mg/L magnesium 0.1-5mg/L strontium 0.2-10mg/L iodine 0.2-5mg/L calcium 1-5mg/L;
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;
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.
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 CN1233594A (en) | 1999-11-03 |
| CN1091430C true CN1091430C (en) | 2002-09-25 |
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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 |
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| CN (1) | CN1091430C (en) |
Families Citing this family (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 |
| RS53994B1 (en) * | 2011-07-22 | 2015-10-30 | Omya International Ag | Micronized caco3 slurry injection system for the remineralization of desalinated and fresh water |
| SI2565165T1 (en) * | 2011-08-31 | 2016-11-30 | Omya International Ag | Remineralization of desalinated and of fresh water by dosing of a calcium carbonate solution in soft water |
| EP2805924B1 (en) * | 2013-05-24 | 2018-02-21 | Omya International AG | 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 |
| 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 |
| CN104692514B (en) * | 2014-12-31 | 2017-05-10 | 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 |
| 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
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| Publication number | Publication date |
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| CN1233594A (en) | 1999-11-03 |
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