CN104193039B - Glacier mineral water treatment system - Google Patents
Glacier mineral water treatment system Download PDFInfo
- Publication number
- CN104193039B CN104193039B CN201410475969.4A CN201410475969A CN104193039B CN 104193039 B CN104193039 B CN 104193039B CN 201410475969 A CN201410475969 A CN 201410475969A CN 104193039 B CN104193039 B CN 104193039B
- Authority
- CN
- China
- Prior art keywords
- water
- mineral water
- treatment system
- glacier mineral
- glacier
- 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.)
- Expired - Fee Related
Links
Abstract
The invention discloses a kind of glacier mineral water treatment system, comprise the transfer lime be communicated with glacier mineral water water source, the reliever be serially connected on transfer lime, in order to the raw water box of buffer memory glacier mineral water, and the raw water pump to be communicated with by the road with raw water box, more medium filter, four accurate filters of connecting step by step, intermediate water tank, middle water pump, oxidizing tower, titanium rod strainer, pure water tank and pure water pump, be provided with anti-siphon means between described more medium filter and accurate filter.The present invention directly adopts the pipeline be communicated with glacier mineral water water source to carry; gravity is utilized to realize unpowered conveying; utilize reliever to ensure the smooth running of subsequent processing device simultaneously; effectively reduce energy consumption; it also avoid the pollution to waterhead area simultaneously; introduce anti-siphon means, improve and occur shutting down the protection to equipment.
Description
Technical field
The present invention relates to water-treatment technology field, particularly relate to a kind of glacier mineral water treatment system.
Background technology
Glacier mineral spring, refers to the natural mineral water formed as main supply using glacier melting.Before more than 500 years, LI Shi-Zhen was just once recorded in Compendium of Material Medica: glacier mineral spring, also known as summer ice, can separate hundred poison.In Tibet, glacier mineral spring is regarded as " holy water " by local Tibetan over the past thousands of years, and they think, this water comes from the ground of bitter cold, goes through the years and practises austerities, be full of world elite, can not only cure the disease, people can also be helped to keep the pure of soul.Research finds, original glacial water is all generally natural small molecule group (3-6 water molecules composition) water, this aquaporin being easy to turnover cytolemma, small-micelle water shows following several aspect for the biological effect of human body: 1, improve water biology utilization ratio, easily utilized by each Cell uptake; 2, strengthen newly
The efficiency of old metabolism and ability, obviously improve the transmission supply of nutrition of whole body material; Improve the transportcapacity of oxygen; Promote the discharge of refuse and toxin in cell; Adjust, safeguard immune function, slow down the aging of organism; 3, normal information interchange between cell can be re-established, improve the self-rehabilitation function of human body, strengthen the information transmission between each cell and structures surrounding, promote normal gene information transmission; 4, the physiologically active strong (solvency power, diffusive force, seepage force, emulsifying power, metabolism power, clearing power) of small-micelle water can meet Human Physiology demand, also has the effect swashing in vivo various enzyme.Be conducive to the mankind and prevent cardiovascular and cerebrovascular diseases.
For high-altitude glacier water, a lot of people is had to propose treatment process, as Chinese patent 200910164313.X discloses a kind of preparation method of high-altitude glacier mineral water.Specifically comprise and gather Yuan Shui, source water aeration, filtration, micro-ozonize and sterile filling five steps.Above-mentioned patent has blocked the direct supplying step of plateau-glacier water by source water aerating step; improve processing cost; and; existing water treatment system; especially the water treatment system of accurate filter is comprised; when there is equipment downtime, the aqueous reflux of accurate filter is back to previous stage mechanism, precision Filter element moment can be caused to be taken out flat and damaged, cause production not carry out smoothly.
Summary of the invention
The object of the invention is the technological deficiency for existing in prior art, and a kind of glacier mineral water treatment system is provided.
The technical scheme adopted for realizing object of the present invention is:
A kind of glacier mineral water treatment system, comprise the transfer lime be communicated with glacier mineral water water source, be serially connected in the reliever on transfer lime, in order to the raw water box of buffer memory glacier mineral water, and the raw water pump to be communicated with by the road with raw water box, more medium filter, four accurate filters of connecting step by step, intermediate water tank, middle water pump, oxidizing tower, titanium rod strainer, pure water tank and pure water pump, anti-siphon means is provided with between described more medium filter and accurate filter, described glacier mineral water treatment system also comprises the ozone mixer structure for ozone in described oxidizing tower, described ozone mixer structure comprises ozone mixing pump, ozone source, ejector, and the aerator be arranged on bottom described oxidizing tower, the exhaust port at oxidizing tower top is set.
Described accurate filter comprises tank body, cover and filter core, and described cover is provided with gas barrier, and described upper gas barrier comprises and is communicated with described cover the bend pipe that Open Side Down, and is serially connected in the variable valve on described bend pipe.
Described more medium filter is quartz filter.
Described four accurate filter filtering accuracies of connecting step by step are respectively 50um, 20um, 10um, 5um.
The filtering accuracy 0.22um that described titanium rod strainer is done.
Described oxidizing tower top is provided with overflow port.
In described oxidizing tower, ozone content is at 0.1-0.2mg/L.
Compared with prior art, the invention has the beneficial effects as follows:
The present invention directly adopts the pipeline be communicated with glacier mineral water water source to carry, gravity is utilized to realize unpowered conveying, utilize reliever to ensure the smooth running of subsequent processing device simultaneously, effectively reduce energy consumption, it also avoid the pollution to waterhead area simultaneously, introduce anti-siphon means, improve and occur shutting down the protection to equipment, and, employing Multi-stage precise filters, the impurity that effective removal contains but does not destroy molecular structure water, ensure the mouthfeel of iceberg mineral spring and quote effect, after adopting ozone sterilization, titanium rod filters again, the bacterium corpse produced during effective removal ozone oxidation sterilization, increase water quality.
Accompanying drawing explanation
Figure 1 shows that the structural representation of glacial water treatment system of the present invention.
Embodiment
Below in conjunction with the drawings and specific embodiments, the present invention is described in further detail.Should be appreciated that specific embodiment described herein only in order to explain the present invention, be not intended to limit the present invention.
As shown in Figure 1, glacier mineral water treatment system of the present invention, comprise the transfer lime 1 be communicated with glacier mineral water water source, described transfer lime be arranged so that treatment system leaves water source, avoid the pollution to waterhead area, altitude change simultaneously by transfer lime realizes automatic transport save energy, be serially connected in the Y-filter 2 on transfer lime and reliever 3, as reducing valve etc., arranging of reliever can avoid the impact of water source change on subsequent disposal mechanism, in order to the raw water box 4 of buffer memory glacier mineral water, and the raw water pump 5 to be communicated with by the road with raw water box, more medium filter 6, as quartz filter, four accurate filters of connecting step by step 7, wherein said four accurate filter filtering accuracies of connecting step by step are respectively 50um, 20um, 10um, 5um, intermediate water tank 8, middle water pump 9, oxidizing tower 10, filtering accuracy is 0.22 μm of titanium rod strainer 11, pure water tank 12 and pure water pump 13, water is delivered to bulking system by described pure water pump, anti-siphon means 14 is provided with between described more medium filter and first accurate filter, also comprise the ozone mixer structure for ozone in described oxidizing tower, described ozone mixer structure comprises ozone mixing pump, ozone source, ejector, and the aerator be arranged on bottom described oxidizing tower, the exhaust port at oxidizing tower top is set.Wherein, described anti-siphon means is commercial anti-siphon valve, is namely provided with tonifying Qi hole in the side of valve body, is provided with water shutoff film with stiffened edge to be closed at this tonifying Qi hole place, thus form a unidirectional air supply passage opened, ensure that water is along the flowing of water inlet direction.When shutting down, accurate filter oppositely draws water to more medium filter, occur parital vacuum, and when forming negative pressure in valve body, tonifying Qi hole automatically can be opened and valve inner is communicated with air, prevents siphonage.This technology similarly to the prior art, is no longer launched to describe at this.
In ozone oxidation sterilisation step of the present invention, enter bottom oxidizing tower by ejector, through aerator, ozone is fully dissolved in water.Ensure that the sufficient time that ozone mixes with water.Generally, ozone in water content is at 0.1-0.2mg/L, and make sterilization effect more thorough, top is furnished with again exhaust emissions and overflow port, ensures that unnecessary ozone can not be trapped in indoor.After overflow port ensures that mixing column internal water is full, water can not flow backwards and get back to ozonizer, damages ozonizer.
The pipeline that direct employing is communicated with glacier mineral water water source is carried, gravity is utilized to realize unpowered conveying, utilize reliever to ensure the smooth running of subsequent processing device simultaneously, effectively reduce energy consumption, it also avoid the pollution to waterhead area simultaneously, introduce anti-siphon means, improve and occur shutting down the protection to equipment, and, employing Multi-stage precise filters, the impurity that effective removal contains but does not destroy molecular structure water, ensure the mouthfeel of iceberg mineral spring and quote effect, after adopting ozone sterilization, titanium rod filters again, the bacterium corpse produced during effective removal ozone oxidation sterilization, increase water quality.
Described aerator is communicated with ozone mixer structure, and described ozone mixer structure comprises and being provided with, and enters bottom oxidizing tower, through aerator, ozone is fully dissolved in water by ejector.Ensure that the sufficient time that ozone mixes with water.Make sterilization effect more thorough, top is furnished with again exhaust emissions and overflow port, ensures that unnecessary ozone can not be trapped in indoor.After overflow port ensures that mixing column internal water is full, water can not flow backwards and get back to ozonizer, damages ozonizer.
Further, described accurate filter comprises tank body, cover and filter core, described cover is provided with gas barrier, described upper gas barrier comprises and is communicated with described cover the bend pipe that Open Side Down, and the variable valve be serially connected on described bend pipe, gas barrier on this, automatic exhaust steam valve different from the past, but adopt variable valve to add stainless steel elbow.General automatic exhaust steam valve often damages, bad trip switch amount, and after being replaced by variable valve, regulated quantity accuracy is comparatively large, and the venting port of bending is comparatively reasonable, can not directly splash on the person.
The above is only the preferred embodiment of the present invention; it should be pointed out that for those skilled in the art, under the premise without departing from the principles of the invention; can also make some improvements and modifications, these improvements and modifications also should be considered as protection scope of the present invention.
Claims (7)
1. a glacier mineral water treatment system, it is characterized in that, comprise the transfer lime be communicated with glacier mineral water water source, be serially connected in the reliever on transfer lime, in order to the raw water box of buffer memory glacier mineral water, and the raw water pump to be communicated with by the road with raw water box, more medium filter, four accurate filters of connecting step by step, intermediate water tank, middle water pump, oxidizing tower, titanium rod strainer, pure water tank and pure water pump, anti-siphon means is provided with between described more medium filter and accurate filter, described glacier mineral water treatment system also comprises the ozone mixer structure for ozone in described oxidizing tower, described ozone mixer structure comprises ozone mixing pump, ozone source, ejector, and the aerator be arranged on bottom described oxidizing tower, the exhaust port at oxidizing tower top is set.
2. glacier mineral water treatment system as claimed in claim 1, it is characterized in that, described accurate filter comprises tank body, cover and filter core, described cover is provided with gas barrier, described upper gas barrier comprises and is communicated with described cover the bend pipe that Open Side Down, and is serially connected in the variable valve on described bend pipe.
3. glacier mineral water treatment system as claimed in claim 1, it is characterized in that, described more medium filter is quartz filter.
4. glacier mineral water treatment system as claimed in claim 1, it is characterized in that, described four accurate filter filtering accuracies of connecting step by step are respectively 50 μm, 20 μm, 10 μm, 5 μm.
5. glacier mineral water treatment system as claimed in claim 1, is characterized in that, the filtering accuracy 0.22 μm that described titanium rod strainer is done.
6. glacier mineral water treatment system as claimed in claim 1, it is characterized in that, described oxidizing tower top is provided with overflow port.
7. glacier mineral water treatment system as claimed in claim 1, it is characterized in that, in described oxidizing tower, ozone content is at 0.1-0.2mg/L.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410475969.4A CN104193039B (en) | 2014-09-18 | 2014-09-18 | Glacier mineral water treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410475969.4A CN104193039B (en) | 2014-09-18 | 2014-09-18 | Glacier mineral water treatment system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104193039A CN104193039A (en) | 2014-12-10 |
| CN104193039B true CN104193039B (en) | 2016-03-09 |
Family
ID=52078461
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410475969.4A Expired - Fee Related CN104193039B (en) | 2014-09-18 | 2014-09-18 | Glacier mineral water treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104193039B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108911303A (en) * | 2018-07-13 | 2018-11-30 | 大别山野岭饮料股份有限公司 | A kind of production technology of mineral water |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101250012A (en) * | 2007-12-22 | 2008-08-27 | 兰州奇正健康日用品有限公司 | Glacier water as well as preparation method and use thereof |
| CN101632482A (en) * | 2009-09-01 | 2010-01-27 | 西藏冰川矿泉水有限公司 | Preparation method of high-altitude glacier mineral water |
| CN203807224U (en) * | 2014-04-30 | 2014-09-03 | 山东久泰环保科技有限公司 | Pressure type ozone disinfection device for water treatment |
| CN204097241U (en) * | 2014-09-18 | 2015-01-14 | 天津邦盛净化设备有限公司 | Glacier mineral water treatment system |
-
2014
- 2014-09-18 CN CN201410475969.4A patent/CN104193039B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101250012A (en) * | 2007-12-22 | 2008-08-27 | 兰州奇正健康日用品有限公司 | Glacier water as well as preparation method and use thereof |
| CN101632482A (en) * | 2009-09-01 | 2010-01-27 | 西藏冰川矿泉水有限公司 | Preparation method of high-altitude glacier mineral water |
| CN203807224U (en) * | 2014-04-30 | 2014-09-03 | 山东久泰环保科技有限公司 | Pressure type ozone disinfection device for water treatment |
| CN204097241U (en) * | 2014-09-18 | 2015-01-14 | 天津邦盛净化设备有限公司 | Glacier mineral water treatment system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104193039A (en) | 2014-12-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102874973A (en) | High-efficiency and low-consumption integrated domestic sewage treatment device | |
| CN108217964A (en) | A kind of sewage water advanced treatment apparatus and method | |
| CN203021356U (en) | Sludge-water separator for sewage treatment | |
| CN105399277A (en) | Rural sewage treatment apparatus | |
| CN104193039B (en) | Glacier mineral water treatment system | |
| CN104710092A (en) | Plastic steel biogas septic tank | |
| CN204097241U (en) | Glacier mineral water treatment system | |
| CN209352730U (en) | A kind of artificial wetland rural sewage processing system | |
| CN208265961U (en) | A kind of Multi-functional excrement sewage treatment combination fixture | |
| CN109516639B (en) | Label improving and reforming system for urban domestic sewage treatment plant | |
| CN208038127U (en) | A kind of XS-CSFM intelligent and high-efficiencies bioreactor | |
| CN206940573U (en) | Sewage separation treatment and purification system | |
| CN206872618U (en) | Distributed, the pelletized reactor of structuring villages and small towns sewage disposal | |
| CN206538330U (en) | A kind of new three jar septic tank | |
| CN204643961U (en) | Anaerobic jar efficient liquid reflux | |
| CN219950790U (en) | Integrated sewage treatment device | |
| CN104276715B (en) | Environment Protection and Drainage of Pulled Water system for the production and processing waste water of tilapia plant area | |
| CN205740636U (en) | A kind of energy-conservation low-temperature resistance type courtyard-style sewage treatment unit | |
| CN218465644U (en) | Biochemical sewage treatment plant of improvement | |
| CN217972763U (en) | Ecological integrated sewage treatment equipment | |
| CN203998996U (en) | A kind of doser | |
| CN201864646U (en) | Underground distributed unpowered domestic sewage treatment device | |
| CN201400598Y (en) | Buried type integrated landscape water treatment system | |
| CN213738743U (en) | Medicament dosing system | |
| CN202322472U (en) | Pharmaceutical factory sewage treatment plant |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160309 Termination date: 20160918 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |