CN107215926A - A kind of alkalescent drinking water manufacture method containing electronics and ionization mineral matter - Google Patents

A kind of alkalescent drinking water manufacture method containing electronics and ionization mineral matter Download PDF

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Publication number
CN107215926A
CN107215926A CN201710589208.5A CN201710589208A CN107215926A CN 107215926 A CN107215926 A CN 107215926A CN 201710589208 A CN201710589208 A CN 201710589208A CN 107215926 A CN107215926 A CN 107215926A
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CN
China
Prior art keywords
water
drinking water
mineral matter
multielement
stoste
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
CN201710589208.5A
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Chinese (zh)
Inventor
李文秀
努民
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BEIJING JIANYUAN TIANDI ENVIRONMENTAL PROTECTION TECHNOLOGY Co Ltd
Original Assignee
BEIJING JIANYUAN TIANDI ENVIRONMENTAL PROTECTION TECHNOLOGY Co Ltd
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Priority to CN201710589208.5A priority Critical patent/CN107215926A/en
Publication of CN107215926A publication Critical patent/CN107215926A/en
Pending legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104—Devices therefor; Their operating or servicing
    • C02F1/4618—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104—Devices therefor; Their operating or servicing
    • C02F1/4618—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water
    • C02F2001/4619—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water only cathodic or alkaline water, e.g. for reducing
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104—Devices therefor; Their operating or servicing
    • C02F1/4618—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water
    • C02F2001/46195—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water characterised by the oxidation reduction potential [ORP]

Abstract

The present invention discloses a kind of alkalescent drinking water manufacture method containing electronics and ionization mineral matter, comprises the following steps：1）, raw material use pH13.0（±02）Electrolytic alkali sexual performance water, particle diameter for 4~10 μm multielement Coexisting Minerals matter and below 60ppm soft water；2）, using refractory ceramics fire pot, three kinds of raw material are put into ceramic pan in proportion, moderate heat obtains stoste after boiled certain time；3）, using drinking pure water by stoste dilute 1000~1500 times, used as drinking water.

Description

A kind of alkalescent drinking water manufacture method containing electronics and ionization mineral matter
Technical field
The present invention relates to alkalescent drinking water manufacture field, more particularly to it is a kind of containing electronics and ionization mineral matter it is weak Alkali water manufacture method.
Background technology
Modern society by soil pollution, agricultural chemicals and chemical fertilizer due to being influenceed, trace element extreme in the food of people's intake Lack, trace element intake deficiency is one of the reason for causing many diseases.The various microelement-supplementings that in the market occurs are protected Strong product, can really be absorbed by the body it is micro- it is micro- its is few, additive in trace element health-care product etc. is to health in addition There is also risk.Because trace element must can be just absorbed by the body under ionization conditions, be this trace element it is quick from Sub-ization technology is the new technology of current drinking water with trace elements.
The content of the invention
The present invention relates to a kind of alkalescent drinking water manufacture method containing electronics and ionization mineral matter, specific steps are such as Under：
1st, potassium carbonate is utilized（K2CO3) as electrolyte, generate high concentration strong basicity functional water, high concentration using water electrolysis equipment Strong basicity functional water index is：PH value is 13.0（±0.2）、ORP（Oxidation-reduction potential）- 960 more than mV, K+Concentration More than 2300ppm, low surface tension.
2nd, multielement Coexisting Minerals matter selects the ore-rock containing 70 kinds of mineral matters, 8 μm~12 μm of far-infrared radiation ripple, such as The mixing ore-rock of medical stone, giant crystal stone or both.Though selected use ore-rock is through high-temperature firing and grinding, mineral matter（Such as medical stone, The mixing ore-rock of giant crystal stone or both）Porous can't be destroyed.
3rd, using double roller roll crusher by selected mineral matter coarse crushing, coarse crushing particle diameter is 0.1mm~0.5mm.Using leaving wet-milling Formula ball mill is in small, broken bits for 0.1mm~0.5mm coarse crushing particle progress by particle diameter, and the rotating speed of sand cylinder is 0.7~0.75nIt is critical, ball Grinding machine volumetric efficiency is 0.4~0.5, and wet grinding media uses water or alcohol.The multielement that particle diameter is 4~10 μm is obtained after grinding to be total to Deposit mineral matter.
4th, using pressure-resistant 50MPa, the high pressure-temperature reactor of 600 DEG C of heatproof, to particle diameter under conditions of 450~500 °C High-temperature firing is carried out for 4~10 μm of multielement Coexisting Minerals matter, the firing time is 20~30 minutes, is obtained after natural cooling many Element Coexisting Minerals matter raw material.When 4 μm~10 μm of multielement Coexisting Minerals matter is contacted with water, because specific surface area increases, easily In the ionization of mineral matter.Multielement Coexisting Minerals plasmid footpath be more than 10 μm, due to specific surface area do not influence very much mineral matter from Sonization effect, multielement Coexisting Minerals plasmid footpath is less than 4 μm, the danger that there is intrusion tissue again, and 4 μm are have selected for this ~10 μm.
5th, the ceramic pan fired using refractory ceramics（It cannot be metal pan）Drinking water processing is carried out, due to containing in water Abundant electronics, can not use canister during infusion, lose to prevent electronics.Added in refractory ceramics firing ceramics pot Below 60ppm soft water 2L, 4~10 μm of multielement 250~500g of Coexisting Minerals matter and pH value are 13.0（±0.2）It is highly concentrated Spend 0.2~0.4L of strong basicity functional water.
Moderate heat is changed to after big fire is boiled to continue to boil after 20~25 minutes, is obtained containing abundant electronics, mineral ion and low PH value under the alkalescent drinking water stoste of surface tension, stoste normal temperature is 10.5~11.0.In high concentration strong basicity functional water Containing it is abundant it is molten deposit hydrogen ion, potassium ion and electronics, molten hydrogen ion, potassium ion and the electronics deposited, can be fast under the conditions of high temperature boiling is boiled Speed ionizes multielement Coexisting Minerals matter, ionization multielement Coexisting Minerals matter is quickly dissolved in water.During batch production, press Aforementioned proportion and method.
5th, stoste is diluted 1000~1500 times using drinking water, the pH value after stoste dilution under normal temperature is 7.5~8.0, Used as drinking water.The daily amount of drinking 1.5L~2.5L.
6th, the drinking water mineral analysis analysis test result after stoste dilution is shown in Table 1.
7th, not only it is applied to promote health, diseases prevention and disease to control containing abundant electronics and mineral ion alkalescent drinking water In treatment, the multiple fields such as agricultural, livestock products, aquatic products are can also be applied to.
Embodiment
In order that the purpose of the present invention, technical scheme are clearer, the preferred embodiments of the present invention will be carried out in detail below Thin description.
The making of the direct drinking water of embodiment 1
Added in refractory ceramics firing ceramics pot below 60ppm soft water 2L, 4~10 μm of multielement Coexisting Minerals matter 0.5g and PH value is 13.0（±0.2）High concentration strong basicity functional water 0.8ml.Moderate heat is changed to after big fire is boiled to continue to boil after 20 minutes, It is 7.8 to obtain the pH value under the alkalescent drinking water containing abundant electronics, ionization mineral matter and low surface tension, normal temperature, can Directly drunk without dilution.The daily amount of drinking 1.5L~2.0L.
The making of the stoste of embodiment 2
Added in refractory ceramics firing ceramics pot below 60ppm soft water 2L, 4~10 μm of multielement Coexisting Minerals matter 20g and PH value is 13.0（±0.2）High concentration strong basicity functional water 200ml.Small fire is changed to after big fire is boiled to continue to boil 20 minutes, is obtained To the alkalescent drinking water stoste containing abundant electronics, ionization mineral matter and low surface tension, the pH value of stoste at normal temperatures For 10.5, stoste is diluted 1000~1500 times using drinking pure water, used as drinking water, the stoste after dilution is in normal temperature Under pH value be 7.6,.The daily amount of drinking 1.5L~2.0L.During a large amount of productions according to the above ratio.
Table 1, mineral analysis analysis test result
Element Content Unit Element Content Unit
7 Li lithiums 2.11 µg/L 112 Cd cadmiums <0.402 µg/L
9 Be berylliums <0.438 µg/L 115 In indiums <0.432 µg/L
11 B boron 14.2 µg/L 118 Sn tin <0.956 µg/L
23 Na sodium 15.2 mg/L 121 Sb antimony 3.28 µg/L
24 Mg magnesium 3.15 mg/L 125 Te telluriums <0.0631 µg/L
27 Al aluminium 1.90 µg/L 127 I iodine 54.4 µg/L
28 Si strontiums 23.6 mg/L 133 Cs caesiums 5.86 µg/L
31 P phosphorus 0.261 mg/L 137 Ba barium 2.94 µg/L
34 S sulphur 4.19 mg/L 139 La lanthanums 0.0236 µg/L
39 K potassium 0.516 mg/L 140 Ce ceriums <0.344 µg/L
42 Ca calcium 1.61 mg/L 141 Pr praseodymiums <0.336 µg/L
45 Sc scandiums 0.0783 µg/L 146 Nd neodymiums <0.379 µg/L
47 Ti titaniums <0.0458 µg/L 147 Sm samariums <0.0101 µg/L
51 V alum 1.18 µg/L 153 Eu europiums <0.0145 µg/L
52 Cr chromium 0.306 µg/L 157 Gd gadoliniums [g á] <0.0529 µg/L
55 Mn manganese 0.549 µg/L 159 Tb terbiums [te] <0.202 µg/L
56 Fe iron 0.461 µg/L 163 Dy dysprosiums <0.0704 µg/L
59 Co cobalts 0.0209 µg/L 165 Ho holmiums <0.106 µg/L
60 Ni nickel 0.224 µg/L 166 Er erbiums <0.319 µg/L
63 Cu copper 0.648 µg/L 169 Tm thuliums <0.573 µg/L
66 Zn zinc 2.05 ng/L 172 Yb ytterbiums <0.0179 µg/L
69 Ga galliums 0.0367 µg/L 175 Lu lutetiums <0.0123 µg/L
72 Ge germanium（zhe） <0.0248 µg/L 178 Hf He <0.689 µg/L
75 As arsenic 2.54 µg/L 181 Ta tantalums [t ǎ n] 3.01 ng/L
78 Se selenium <0.408 µg/L 182 W tungsten 2.51 µg/L
79 Br bromines 39.8 µg/L 185 Re rheniums <0.171 µg/L
85 Rb rubidiums 3.49 µg/L 189 Os osmiums <0.0446 µg/L
88 Sr strontiums 36.8 µg/L 193 Ir iridium <0.464 µg/L
89 Y yttriums <0.0764 µg/L 195 Pt platinum <0.0349 µg/L
90 Zr zirconiums <0.0356 µg/L 197 Au gold 0.0668 µg/L
93 Nb niobiums <0.978 µg/L 202 Hg mercury 0.0540 µg/L
95 Mo molybdenums <0.574 µg/L 205 Tl thalliums 0.0342 µg/L
101 Ru rutheniums（liao） 0.0658 µg/L 208 Pb lead 0.0246 µg/L
103 Rh rhodiums 0.0854 µg/L 209 Bi bismuths 0.00283 µg/L
105 Pd palladiums <0.153 µg/L 232 Th thoriums 0.00797 µg/L
107 Ag silver <0.877 µg/L 238 U uranium 2.10 µg/L

Claims (5)

1. a kind of alkalescent drinking water manufacture method containing electronics and ionization mineral matter, it is characterised in that including following step Suddenly：
1）Using water electrolysis equipment, potassium carbonate is utilized（K2CO3) as electrolyte, generate high concentration strong basicity functional water；
2）Go out the multielement Coexisting Minerals matter that particle diameter is 4~10 μm using the formula ball mill grinding of leaving；
3）Fire pot using refractory ceramics, by below 60ppm drink soft water, high concentration strong basicity functional water and particle diameter for 4~ 10 μm of multielement Coexisting Minerals matter is put into ceramic pan in proportion, and moderate heat obtains stoste after boiled certain time；
4）Stoste is diluted 1000~1500 times using below 60ppm soft water of drinking, used as drinking water.
2. a kind of alkalescent drinking water manufacture method containing electronics and ionization mineral matter in right 1, its feature exists In contained step 1）High concentration strong basicity functional water is generated using water electrolysis equipment, high concentration strong basicity functional water index is：pH It is worth for 13.0（±0.2）、ORP（Oxidation-reduction potential）- 960 more than mV, K+More than concentration 2300ppm, low surface tension.
3. a kind of alkalescent drinking water manufacture method containing electronics and ionization mineral matter in right 1, its feature exists In contained step 2）Including：
1）Multielement Coexisting Minerals matter selects the ore-rock containing 70 kinds of mineral matters, 8 μm~12 μm of far-infrared radiation ripple, such as wheat meal The mixing ore-rock of stone, giant crystal stone or both；
2）Using double roller roll crusher by selected mineral matter coarse crushing, coarse crushing particle diameter is 0.1mm~0.5mm, using leaving wet-milling formula ball Grinding machine is in small, broken bits for 0.1mm~0.5mm coarse crushing particle progress by particle diameter, and the rotating speed of sand cylinder is 0.7~0.75nIt is critical, ball mill Volumetric efficiency is 0.4~0.5, and wet grinding media uses water or alcohol, the multielement that particle diameter is 4~10 μm is obtained after grinding ore deposit coexists Material；
3）Using pressure-resistant 50MPa, the high pressure-temperature reactor of 600 DEG C of heatproof, under conditions of 450~500 °C to particle diameter be 4~ 10 μm of multielement Coexisting Minerals matter carries out high-temperature firing, and the firing time is 20~30 minutes, and multielement is obtained after natural cooling Coexisting Minerals matter raw material.
4. a kind of alkalescent drinking water manufacture method containing electronics and ionization mineral matter in right 1, its feature exists In contained step 3）Including：
1）When being manufactured containing abundant electronics and ionization mineral matter alkalescent drinking water, the ceramic pan fired using refractory ceramics, Cannot add below 60ppm soft water 2L, 4 μm~10 μm of multielement in metal pan, refractory ceramics firing ceramics pot to be total to It is 13.0 to deposit 250~500g of mineral matter and pH value（±0.2）0.2~0.4L of high concentration strong basicity functional water；
2）Moderate heat is changed to after big fire is boiled to continue to boil 20~25 minutes, obtains the weak base containing abundant electronics and ionization mineral matter Property drinking water stoste, the pH value of stoste is 10.5~11.0 under normal temperature.
5. a kind of alkalescent drinking water manufacture method containing electronics and ionization mineral matter in right 1, its feature exists In contained step 4）Stoste is diluted 1000~1500 times using drinking water, the pH value after stoste dilution under normal temperature for 7.5~ 8.0, used as health-care drinking-water.
CN201710589208.5A 2017-07-19 2017-07-19 A kind of alkalescent drinking water manufacture method containing electronics and ionization mineral matter Pending CN107215926A (en)

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6351991A (en) * 1986-08-20 1988-03-05 Tatsuo Okazaki System for producing sterilizable electrolytic ionic water
CN1220118A (en) * 1998-06-10 1999-06-23 恩施土家族苗族自治州医疗卫生用品开发公司 Method for preparing natural selenium concentrated liquid
CN101032705A (en) * 2007-04-24 2007-09-12 清华大学 Massifying method of medical stone ultra fines produced by waterproof pulverization and concentrated solution
WO2008138358A1 (en) * 2007-05-13 2008-11-20 Magued George Amin Electrolyzed alkaline water for drinking ph 9.5 +/- 1.5
CN101822403A (en) * 2010-04-20 2010-09-08 王衍洲 Ocean element electrolysis concentrated product and manufacture method thereof
CN105875498A (en) * 2016-04-18 2016-08-24 北京建元天地环保科技有限公司 Method for carrying out pig breeding by using functional water

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6351991A (en) * 1986-08-20 1988-03-05 Tatsuo Okazaki System for producing sterilizable electrolytic ionic water
CN1220118A (en) * 1998-06-10 1999-06-23 恩施土家族苗族自治州医疗卫生用品开发公司 Method for preparing natural selenium concentrated liquid
CN101032705A (en) * 2007-04-24 2007-09-12 清华大学 Massifying method of medical stone ultra fines produced by waterproof pulverization and concentrated solution
WO2008138358A1 (en) * 2007-05-13 2008-11-20 Magued George Amin Electrolyzed alkaline water for drinking ph 9.5 +/- 1.5
CN101822403A (en) * 2010-04-20 2010-09-08 王衍洲 Ocean element electrolysis concentrated product and manufacture method thereof
CN105875498A (en) * 2016-04-18 2016-08-24 北京建元天地环保科技有限公司 Method for carrying out pig breeding by using functional water

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Application publication date: 20170929