CN108975574A - A kind of alkalinity pure water and its production technology - Google Patents

A kind of alkalinity pure water and its production technology Download PDF

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Publication number
CN108975574A
CN108975574A CN201810907950.0A CN201810907950A CN108975574A CN 108975574 A CN108975574 A CN 108975574A CN 201810907950 A CN201810907950 A CN 201810907950A CN 108975574 A CN108975574 A CN 108975574A
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China
Prior art keywords
pure water
water
alkaline
layer
production technology
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CN201810907950.0A
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Chinese (zh)
Inventor
孙宗君
孙宗培
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Anhui Biyun Lake Food Science And Technology Development Co Ltd
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Anhui Biyun Lake Food Science And Technology Development Co Ltd
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Priority to CN201810907950.0A priority Critical patent/CN108975574A/en
Publication of CN108975574A publication Critical patent/CN108975574A/en
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    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00—Multistage treatment of water, waste water or sewage
    • 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
    • C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
    • 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
    • C02F1/42—Treatment of water, waste water, or sewage by ion-exchange
    • 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
    • C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
    • 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
    • C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
    • 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
    • C02F1/72—Treatment of water, waste water, or sewage by oxidation
    • C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/02—Non-contaminated water, e.g. for industrial water supply
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/06—Controlling or monitoring parameters in water treatment pH
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/22—O2
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00—General aspects of water treatment
    • C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions

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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)
  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Non-Alcoholic Beverages (AREA)

Abstract

It include following component: 10-15 milligrams of sodium bicarbonate, 5-10 milligrams of saleratus in every liter of alkaline pure water the invention discloses a kind of alkaline pure water and its production technology.The present invention is raw material by tap water, simple production process, by being handled in advance using multi-medium filtering layer tap water, most of insoluble fine grained impurity and disinfectant ingredient can be removed, after through treatment on ion exchange columns, the salt ion in tap water can be removed, obtain pure water, it is carried out disinfection processing by pure water of the ozone to acquisition, and ozone ingredient is discharged using heating kettle, harm will not be generated to human body, by the way that oxygen is added, improve the oxygen content of pure water, improve the application mouthfeel of pure water, the pH value of pure water is adjusted to alkalescent by addition sodium bicarbonate and saleratus and supplements the necessary sodium and kalium element of human body, be conducive to improve human internal environment, improve health.

Description

A kind of alkalinity pure water and its production technology
Technical field
The invention belongs to pure water technical fields, and in particular to a kind of alkalinity pure water and its production technology.
Background technique
Drinking water refers to can be without handling, directly feed the water that human body drinks.Water is the chief component of body fluid, is Constitute the important substance of cell, tissue fluid, blood plasma etc..Water as in vivo all chemical reaction media, be various nutrients and The platform of matter transportation.
Existing pure water generallys use municipal tap water and is prepared, and can be obtained after taste removal and ultrafiltration membrance filter Pure water is simultaneously sold.But lack sodium and kalium element needed by human in above-mentioned pure water, and the water in tap water pipe network contains Oxygen amount is low, is unfavorable for people and directly drinks.
Summary of the invention
The purpose of the present invention is to provide a kind of alkaline pure water and its production technologies, to solve to mention in above-mentioned background technique Out the problem of.
To achieve the above object, the invention provides the following technical scheme: a kind of alkalinity pure water, includes in every liter of pure water Following component: 10-15 milligrams of sodium bicarbonate, 5-10 milligrams of saleratus.
A kind of production technology of alkalinity pure water, including following operating procedure:
S1: selection municipal tap water is raw material, and tap water is passed through multi-medium filtering layer and is filtered, and collects level-one filtrate, standby With；
S2: being passed through ion exchange column for the filtrate in S1 and be filtered, and collects second level filtrate, spare；
S3: the second level filtrate in S2 being passed through in accurate filter and is filtered, and obtains three-level filtrate, spare；
S4: the three-level filtrate in S2 being added into process tank, is continually fed into ozone 5-10 minutes, and using blender with 100- 200r/min revolving speed persistently stirs 3-5 hours, obtains pure water；
S5: pure water in S4 being added into blend tank, and pure water is heated to 60-80 DEG C, with 200-260r/min revolving speed It is stirred, slowly sodium bicarbonate and saleratus is added into blend tank, and the pH value of solution is examined using Ph meter It surveys, and the pH value for controlling solution persistently stirs 10-20 minutes later between 7.4-7.6, obtains alkaline water；
S6: S5 neutral and alkali water is added into heating kettle, is heated by heating kettle to alkaline water, is discharged smelly in alkaline water Oxygen, cooled to room temperature after heating, and water is transferred in oxygenation tank, constantly it is filled in the alkaline water into oxygenation tank Oxygen improves alkaline content of oxygen dissolved in water, continues 20-30 minutes；
S7: being filtered processing by RO filter membrane for the oxygenated water in S6, obtains alkaline pure water, and by automatic filling machine into Row is filling.
Preferably, multi-medium filtering layer successively includes the wood of the diatomite layer of 3-5cm thickness, 1-2cm thickness from top to bottom Matter cellulose layer, the sintering oxidation aluminium layer of 0.5-1cm thickness, the active carbon layer of 5-10cm thickness, 2-4cm thickness PP fiber Layer, and tap water enters from diatomite layer and flows out from PP fibrous layer, it is 1.2-1.4MPa that water flow, which enters pressure,.
Preferably, the rate that is passed through of ozone is 10-20L/min in step S4.
Preferably, the heating temperature of heating kettle is 90-100 DEG C in step S5.
Preferably, the rate that is passed through of oxygen is 5-10L/min in step S6.
Technical effect and advantage of the invention:
The present invention is raw material, simple production process, by using multi-medium filtering layer to carry out tap water in advance by tap water Processing, can remove most of insoluble fine grained impurity and disinfectant ingredient can remove after through treatment on ion exchange columns Salt ion in tap water obtains pure water, is carried out disinfection processing by pure water of the ozone to acquisition, and uses heating kettle general The discharge of ozone ingredient will not generate harm to human body, by the way that oxygen is added, improves the oxygen content of pure water, improve pure water Application mouthfeel, the pH value of pure water is adjusted to alkalescent by the way that sodium bicarbonate and saleratus is added and supplements human body necessity Sodium and kalium element, be conducive to improve human internal environment, improve health.
Specific embodiment
Below in conjunction with the embodiment of the present invention, technical scheme in the embodiment of the invention is clearly and completely described, Obviously, described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.Based in the present invention Embodiment, every other embodiment obtained by those of ordinary skill in the art without making creative efforts, all Belong to the scope of protection of the invention.
Embodiment 1
A kind of alkalinity pure water, includes following component: 10 milligrams of sodium bicarbonate, 5 milligrams of saleratus in every liter of pure water.
A kind of production technology of alkalinity pure water, including following operating procedure:
S1: selection municipal tap water is raw material, and tap water is passed through multi-medium filtering layer and is filtered, and multi-medium filtering layer is from upper Under successively include the diatomite layer of 3cm thickness, the lignocellulosic layer of 1cm thickness, 0.5cm thickness sintering oxidation aluminium layer, The PP fibrous layer of the active carbon layer of 5cm thickness, 2cm thickness, and tap water enters from diatomite layer and flows out from PP fibrous layer, water It is 1.2MPa that stream, which enters pressure, collects level-one filtrate, spare；
S2: being passed through ion exchange column for the filtrate in S1 and be filtered, and collects second level filtrate, spare；
S3: the second level filtrate in S2 being passed through in accurate filter and is filtered, and obtains three-level filtrate, spare；
S4: the three-level filtrate in S2 being added into process tank, is continually fed into ozone 5 minutes, and the rate that is passed through of ozone is 10L/ Min, and using blender with 100r/min revolving speed, it persistently stirs 3 hours, obtains pure water；
S5: pure water in S4 is added into blend tank, and pure water is heated to 60 DEG C, is stirred with 200r/min revolving speed It mixes, slowly sodium bicarbonate and saleratus is added into blend tank, and the pH value of solution is detected using Ph meter, and controls The pH value of solution processed is 7.4, persistently stirs 10 minutes later, obtains alkaline water；
S6: S5 neutral and alkali water is added into heating kettle, is heated by heating kettle to alkaline water, the heating temperature of heating kettle It is 90 DEG C, the ozone in alkaline water, cooled to room temperature after heating is discharged, and water is transferred in oxygenation tank, constantly Oxygen is filled in alkaline water into oxygenation tank, the rate that is passed through of oxygen is 5L/min, improves alkaline content of oxygen dissolved in water, holds It is 20 minutes continuous；
S7: being filtered processing by RO filter membrane for the oxygenated water in S6, obtains alkaline pure water, and by automatic filling machine into Row is filling.
Embodiment 2
A kind of alkalinity pure water, includes following component: 13 milligrams of sodium bicarbonate, 7 milligrams of saleratus in every liter of pure water.
A kind of production technology of alkalinity pure water, including following operating procedure:
S1: selection municipal tap water is raw material, and tap water is passed through multi-medium filtering layer and is filtered, and multi-medium filtering layer is from upper Under successively include the diatomite layer of 4cm thickness, the lignocellulosic layer of 1.5cm thickness, 0.8cm thickness sintered alumina The PP fibrous layer of layer, the active carbon layer of 8cm thickness, 3cm thickness, and tap water enters from diatomite layer and from PP fiber laminar flow Out, it is 1.3MPa that water flow, which enters pressure, collects level-one filtrate, spare；
S2: being passed through ion exchange column for the filtrate in S1 and be filtered, and collects second level filtrate, spare；
S3: the second level filtrate in S2 being passed through in accurate filter and is filtered, and obtains three-level filtrate, spare；
S4: the three-level filtrate in S2 being added into process tank, is continually fed into ozone 8 minutes, and the rate that is passed through of ozone is 15L/ Min, and using blender with 150r/min revolving speed, it persistently stirs 4 hours, obtains pure water；
S5: pure water in S4 is added into blend tank, and pure water is heated to 70 DEG C, is stirred with 230r/min revolving speed It mixes, slowly sodium bicarbonate and saleratus is added into blend tank, and the pH value of solution is detected using Ph meter, and controls The pH value of solution processed is 7.5, persistently stirs 15 minutes later, obtains alkaline water；
S6: S5 neutral and alkali water is added into heating kettle, is heated by heating kettle to alkaline water, the heating temperature of heating kettle It is 95 DEG C, the ozone in alkaline water, cooled to room temperature after heating is discharged, and water is transferred in oxygenation tank, constantly Oxygen is filled in alkaline water into oxygenation tank, the rate that is passed through of oxygen is 8L/min, improves alkaline content of oxygen dissolved in water, holds It is 25 minutes continuous；
S7: being filtered processing by RO filter membrane for the oxygenated water in S6, obtains alkaline pure water, and by automatic filling machine into Row is filling.
Embodiment 3
A kind of alkalinity pure water, includes following component: 15 milligrams of sodium bicarbonate, 10 milligrams of saleratus in every liter of pure water.
A kind of production technology of alkalinity pure water, including following operating procedure:
S1: selection municipal tap water is raw material, and tap water is passed through multi-medium filtering layer and is filtered, and multi-medium filtering layer is from upper Under successively include the diatomite layer of 5cm thickness, the lignocellulosic layer of 2cm thickness, 1cm thickness sintering oxidation aluminium layer, The PP fibrous layer of the active carbon layer of 10cm thickness, 4cm thickness, and tap water enters from diatomite layer and flows out from PP fibrous layer, It is 1.4MPa that water flow, which enters pressure, collects level-one filtrate, spare；
S2: being passed through ion exchange column for the filtrate in S1 and be filtered, and collects second level filtrate, spare；
S3: the second level filtrate in S2 being passed through in accurate filter and is filtered, and obtains three-level filtrate, spare；
S4: the three-level filtrate in S2 being added into process tank, is continually fed into ozone 10 minutes, and the rate that is passed through of ozone is 20L/ Min, and using blender with 200r/min revolving speed, it persistently stirs 5 hours, obtains pure water；
S5: pure water in S4 is added into blend tank, and pure water is heated to 80 DEG C, is stirred with 260r/min revolving speed It mixes, slowly sodium bicarbonate and saleratus is added into blend tank, and the pH value of solution is detected using Ph meter, and controls The pH value of solution processed is 7.6, persistently stirs 20 minutes later, obtains alkaline water；
S6: S5 neutral and alkali water is added into heating kettle, is heated by heating kettle to alkaline water, the heating temperature of heating kettle It is 100 DEG C, the ozone in alkaline water, cooled to room temperature after heating is discharged, and water is transferred in oxygenation tank, constantly Oxygen is filled in alkaline water into oxygenation tank, the rate that is passed through of oxygen is 10L/min, alkaline content of oxygen dissolved in water is improved, Continue 30 minutes；
S7: being filtered processing by RO filter membrane for the oxygenated water in S6, obtains alkaline pure water, and by automatic filling machine into Row is filling.
Specifically, in use, it is raw material, simple production process, by using multimedium in advance that the present invention, which passes through tap water, Filter layer handles tap water, can remove most of insoluble fine grained impurity and disinfectant ingredient, pass through ion After exchange column processing, the salt ion in tap water can be removed, pure water is obtained, is carried out disinfection by pure water of the ozone to acquisition Processing, and ozone ingredient is discharged using heating kettle, harm will not be generated to human body, by the way that oxygen is added, improve pure water Oxygen content, improve the application mouthfeel of pure water, by be added sodium bicarbonate and saleratus by the pH value of pure water adjust to Alkalescent simultaneously supplements the necessary sodium and kalium element of human body, is conducive to improve human internal environment, improves health.
Finally, it should be noted that the foregoing is only a preferred embodiment of the present invention, it is not intended to restrict the invention, Although the present invention is described in detail referring to the foregoing embodiments, for those skilled in the art, still may be used To modify the technical solutions described in the foregoing embodiments or equivalent replacement of some of the technical features, All within the spirits and principles of the present invention, any modification, equivalent replacement, improvement and so on should be included in of the invention Within protection scope.

Claims (6)

1. a kind of alkalinity pure water, it is characterised in that: include following component: 10-15 milligrams of sodium bicarbonate, carbon in every liter of pure water 5-10 milligrams of potassium hydrogen phthalate.
2. a kind of production technology of alkaline pure water according to claim 1, it is characterised in that: walked including following operation It is rapid:
S1: selection municipal tap water is raw material, and tap water is passed through multi-medium filtering layer and is filtered, and collects level-one filtrate, standby With；
S2: being passed through ion exchange column for the filtrate in S1 and be filtered, and collects second level filtrate, spare；
S3: the second level filtrate in S2 being passed through in accurate filter and is filtered, and obtains three-level filtrate, spare；
S4: the three-level filtrate in S2 being added into process tank, is continually fed into ozone 5-10 minutes, and using blender with 100- 200r/min revolving speed persistently stirs 3-5 hours, obtains pure water；
S5: pure water in S4 being added into blend tank, and pure water is heated to 60-80 DEG C, with 200-260r/min revolving speed It is stirred, slowly sodium bicarbonate and saleratus is added into blend tank, and the pH value of solution is examined using Ph meter It surveys, and the pH value for controlling solution persistently stirs 10-20 minutes later between 7.4-7.6, obtains alkaline water；
S6: S5 neutral and alkali water is added into heating kettle, is heated by heating kettle to alkaline water, is discharged smelly in alkaline water Oxygen, cooled to room temperature after heating, and water is transferred in oxygenation tank, constantly it is filled in the alkaline water into oxygenation tank Oxygen improves alkaline content of oxygen dissolved in water, continues 20-30 minutes；
S7: being filtered processing by RO filter membrane for the oxygenated water in S6, obtains alkaline pure water, and by automatic filling machine into Row is filling.
3. a kind of production technology of alkaline pure water according to claim 2, it is characterised in that: multi-medium filtering layer is from upper Under successively include the diatomite layer of 3-5cm thickness, the lignocellulosic layer of 1-2cm thickness, 0.5-1cm thickness sintering oxidation Aluminium layer, the active carbon layer of 5-10cm thickness, 2-4cm thickness PP fibrous layer, and tap water from diatomite layer enter and from PP fibre Dimension laminar flow goes out, and it is 1.2-1.4MPa that water flow, which enters pressure,.
4. a kind of production technology of alkaline pure water according to claim 2, it is characterised in that: ozone is logical in step S4 Entering rate is 10-20L/min.
5. a kind of production technology of alkaline pure water according to claim 2, it is characterised in that: heating kettle in step S5 Heating temperature is 90-100 DEG C.
6. a kind of production technology of alkaline pure water according to claim 2, it is characterised in that: oxygen is logical in step S6 Entering rate is 5-10L/min.
CN201810907950.0A 2018-08-10 2018-08-10 A kind of alkalinity pure water and its production technology Pending CN108975574A (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1178197A (en) * 1996-09-27 1998-04-08 李传声 Alkali mineral drinking water and preparation thereof
US7507388B2 (en) * 2004-11-11 2009-03-24 Eti Soda Uretim Pazarlama Nakliyat Ve Elektrik Uretim Sanayi Ve Ticaret A.S. Process for production of dense soda, light soda, sodium bicarbonate and sodium silicate from solutions containing bicarbonate
CN201722229U (en) * 2010-07-06 2011-01-26 熊景安 Natural alkalescent water production device
CN104080740A (en) * 2012-02-03 2014-10-01 Omya国际股份公司 Process for the preparation of an aqueous solution comprising at least one earth alkali hydrogen carbonate and its use
CN105167091A (en) * 2015-09-22 2015-12-23 漯河市日康食品饮料有限公司 Soda water beverage and preparation method thereof

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1178197A (en) * 1996-09-27 1998-04-08 李传声 Alkali mineral drinking water and preparation thereof
US7507388B2 (en) * 2004-11-11 2009-03-24 Eti Soda Uretim Pazarlama Nakliyat Ve Elektrik Uretim Sanayi Ve Ticaret A.S. Process for production of dense soda, light soda, sodium bicarbonate and sodium silicate from solutions containing bicarbonate
CN201722229U (en) * 2010-07-06 2011-01-26 熊景安 Natural alkalescent water production device
CN104080740A (en) * 2012-02-03 2014-10-01 Omya国际股份公司 Process for the preparation of an aqueous solution comprising at least one earth alkali hydrogen carbonate and its use
CN105167091A (en) * 2015-09-22 2015-12-23 漯河市日康食品饮料有限公司 Soda water beverage and preparation method thereof

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
杨晓光等: "《会喝才健康》", 31 August 2012, 中国中医药出版社 *
阮美娟等: "《饮料工艺学》", 31 January 2013, 中国轻工业出版社 *

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Application publication date: 20181211