CN106861474A - Hot spring natural mineral water fluorine removal terminal fluorinated volume enters mixing arrangement against jet flow - Google Patents
Hot spring natural mineral water fluorine removal terminal fluorinated volume enters mixing arrangement against jet flow Download PDFInfo
- Publication number
- CN106861474A CN106861474A CN201710230000.4A CN201710230000A CN106861474A CN 106861474 A CN106861474 A CN 106861474A CN 201710230000 A CN201710230000 A CN 201710230000A CN 106861474 A CN106861474 A CN 106861474A
- Authority
- CN
- China
- Prior art keywords
- tank body
- water
- fluorine removal
- removal terminal
- jet flow
- 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
Links
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 title claims abstract description 31
- 239000011737 fluorine Substances 0.000 title claims abstract description 31
- 229910052731 fluorine Inorganic materials 0.000 title claims abstract description 31
- 235000020682 bottled natural mineral water Nutrition 0.000 title claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 48
- 230000002045 lasting effect Effects 0.000 claims abstract 2
- 239000000047 product Substances 0.000 description 7
- 229910052500 inorganic mineral Inorganic materials 0.000 description 6
- 239000011707 mineral Substances 0.000 description 6
- 230000009286 beneficial effect Effects 0.000 description 4
- 230000006641 stabilisation Effects 0.000 description 3
- 238000011105 stabilization Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical group O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/311—Injector mixers in conduits or tubes through which the main component flows for mixing more than two components; Devices specially adapted for generating foam
- B01F25/3111—Devices specially adapted for generating foam, e.g. air foam
- B01F25/31114—Devices specially adapted for generating foam, e.g. air foam with means for introducing an additional component, e.g. in predetermined proportion or in the main component
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F2025/91—Direction of flow or arrangement of feed and discharge openings
- B01F2025/915—Reverse flow, i.e. flow changing substantially 180° in direction
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/48—Mixing water in water-taps with other ingredients, e.g. air, detergents or disinfectants
Abstract
Enter mixing arrangement against jet flow the present invention relates to a kind of hot spring natural mineral water fluorine removal terminal fluorinated volume,Including tank body,Support,Helper,It is characterized in that described tank base is provided with oral siphon and reverse jet tube and drainpipe,When the fluorine removal terminal fluorinated water for flowing into is stored into higher than reverse jet tube,The positive pressure that water layer is above come into the tank body storage water lasting higher than reverse jet tube enters the buffer brake and product water tank of water against jet flow was previously flowed into,Seamless liquidating is formed to interpenetrate,Reach the dynamic purpose that mixing is adjusted naturally,Ensure the overall fluorinated volume uniformity of fluorine removal terminal product water,Described tank body lower part is provided with symmetrical outlet pipe,The top of tank body is provided with symmetrical with gap and metering gap,Tank body top is provided with radiating tube and manhole,Tank body is placed on described support,Described helper is fixed on support across tank body.The present invention has simple structure, easy to operate, pollution-free, it is ensured that the overall fluorinated volume uniformity of fluorine removal terminal product water.
Description
Technical field
The invention belongs to hot spring natural mineral water process field, especially a kind of hot spring natural mineral water fluorine removal
Terminal fluorinated volume enters mixing arrangement against jet flow.
Background technology
Hot spring natural mineral water by after fluorine removal device, in filter process different time sections its fluorine removal terminal water
Fluorinated volume it is different, fluorine removal terminal fluorinated volume mixing arrangement be generally adverse current or two kinds of direct current hybrid mode；In direct current mixing
During mode due to every empty shock, on the one hand bringing air into and easily causing outside water pollution, another aspect hot spring mineral water is removed
Water temperature is all 35 during fluorine0More than C, after the fluorine removal terminal water that initial direct current enters enters mixing arrangement, as temperature reduction is compared
Increase again and decline, the ion motion in water weakens, and the fluorinated volume of fluorine removal terminal water water layer in mixing arrangement easily occurs not
Together, it is impossible to realize the uniform of fluorine removal terminal water mixing fluorinated volume, the erroneous judgement for causing detection to check；Enter the side of mixing using inverse jet flow
Formula, on the one hand can prevent to exclude air and bring into, effectively prevent pollution, and on the other hand, inverse jet flow enters the hot spring mineral spring of fluorine removal terminal
Water is high due to temperature, and proportion is reduced and risen, and the ion motion in water is accelerated, and constantly moves upwards and the forward direction for being introduced into water layer
The water of pressure is mixed and is interpenetrated, and reaches the purpose that dynamic mixes naturally, it is ensured that the entirety of fluorine removal terminal product water contains
Fluorine amount uniformity.
The content of the invention
It is an object of the invention to provide a kind of simple structure, pure natural property that is easy to operate, pollution-free, keeping mineral water
And the fluorine removal terminal fluorinated volume of raw water beneficial element stabilization enters nature mixing arrangement against jet flow.
The present invention is to reach above-mentioned purpose, and the technical solution taken is as follows：
A kind of hot spring natural mineral water fluorine removal terminal fluorinated volume enters mixing arrangement, including tank body, support, helper against jet flow,
Characterized in that, described tank base is provided with oral siphon and reverse jet tube and drainpipe, when the fluorine removal terminal fluorinated water storage for flowing into
Be stored to during higher than reverse jet tube, previously flowed into tank body higher than the storage water of reverse jet tube continue inverse jet flow enter water buffer brake and
The positive pressure of water layer is above come into product water tank, seamless liquidating is formed and is interpenetrated, mixing is adjusted naturally to reach dynamic
The purpose of section, it is ensured that the overall fluorinated volume uniformity of fluorine removal terminal product water, described tank body lower part is provided with symmetrical water outlet
Pipe, the top of tank body is provided with symmetrical with gap and metering gap, and tank body top is provided with radiating tube and manhole, described branch
Tank body is placed on frame, described helper is fixed on support across tank body.
The present invention has simple structure, pollution-free, easy to operate, pollution-free, it is ensured that the entirety of fluorine removal terminal product water contains
Fluorine amount uniformity, keeps pure natural property and the beneficial element stabilization of mineral water.
Brief description of the drawings：
Fig. 1 is overall structure front view of the invention,
Fig. 2 is overall structure left view of the invention,
Fig. 3 is overall structure stereogram of the invention.
In Fig. 1 ~ Fig. 3, tank body（1）, radiating tube（2）, gap（3）, metering gap（4）, outlet pipe（5）, enter water
Pipe（6）, drainpipe（7）, support（8）, helper（9）, reverse jet tube（10）, manhole（11）.
Specific embodiment：
The present invention is further described with reference to the accompanying drawings and examples：
As shown in Figure 1 to Figure 3, a kind of hot spring natural mineral water fluorine removal terminal fluorinated volume enters mixing arrangement against jet flow, including
Tank body, support, helper, wherein, the described bottom of tank body 1 is provided with oral siphon 6 and reverse jet tube 10 and drainpipe 7, when removing for flowing into
Fluorine terminal fluorinated water is stored into during higher than reverse jet tube 10, has previously been flowed into and has been continued to enter water 10 against jet flow higher than reverse jet tube in tank body 1
The positive pressure of water layer is above come into the buffer brake that storage water enters against jet flow and product water tank, seamless liquidating mutually is formed
Mutually permeate, reach the dynamic purpose that mixing is adjusted naturally, it is ensured that the overall fluorinated volume uniformity of fluorine removal terminal product water, it is described
The bottom of tank body 1 be provided with symmetrical outlet pipe 5, the top of tank body 1 is provided with symmetrical with gap 3 and metering gap 4, tank body
（1）Top is provided with radiating tube 2 and manhole 11, and tank body 1 is placed on described support 8, and described helper 9 is fixed on across tank body 1
On support 8.
The beneficial effect of this specific embodiment：It is easy to operate with simple structure, it is pollution-free, entered using inverse jet flow mixed
The mode of conjunction, on the one hand can prevent to exclude air and bring into, effectively prevent pollution, and on the other hand, inverse jet flow enters the heat of fluorine removal terminal
Spring mineral water is high due to temperature, and proportion is reduced and risen, and the ion motion in water is accelerated, and constantly moves upwards and is introduced into water layer
The water of positive pressure mixed and interpenetrated.Reach the purpose that dynamic mixes naturally, it is ensured that fluorine removal terminal product water
Overall fluorinated volume uniformity, keeps pure natural property and the beneficial element stabilization of mineral water.
Claims (1)
1. a kind of hot spring natural mineral water fluorine removal terminal fluorinated volume enters mixing arrangement, including tank body, support, people against jet flow
Ladder, it is characterised in that described tank body（1）Bottom is provided with oral siphon（6）And reverse jet tube（10）With drainpipe（7）, when what is flowed into
Fluorine removal terminal fluorinated water is stored into higher than reverse jet tube（10）When, previously flowed into tank body（1）It is interior higher than reverse jet tube（10）Storage
The positive pressure of water layer is above come into the lasting buffer brake and product water tank for entering water against jet flow of water, seamless liquidating is formed
Interpenetrate, reach the dynamic purpose that mixing is adjusted naturally, it is ensured that the overall fluorinated volume uniformity of fluorine removal terminal product water, institute
The tank body stated（1）Bottom is provided with symmetrical outlet pipe（5）, tank body（1）Top be provided with symmetrical and gap（3）Overflow with metering
The mouth of a river（4）, tank body（1）Top is provided with radiating tube（2）With manhole（11）, described support（8）Upper placement tank body（1）, it is described
Helper（9）Across tank body（1）It is fixed on support（8）On.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710230000.4A CN106861474A (en) | 2017-04-10 | 2017-04-10 | Hot spring natural mineral water fluorine removal terminal fluorinated volume enters mixing arrangement against jet flow |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710230000.4A CN106861474A (en) | 2017-04-10 | 2017-04-10 | Hot spring natural mineral water fluorine removal terminal fluorinated volume enters mixing arrangement against jet flow |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106861474A true CN106861474A (en) | 2017-06-20 |
Family
ID=59162884
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710230000.4A Pending CN106861474A (en) | 2017-04-10 | 2017-04-10 | Hot spring natural mineral water fluorine removal terminal fluorinated volume enters mixing arrangement against jet flow |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106861474A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6349237A (en) * | 1986-08-14 | 1988-03-02 | Daido Kogyo Co Ltd | Emulsion device |
| CN2608485Y (en) * | 2002-09-03 | 2004-03-31 | 上海莱拓环境科技有限公司 | Drinking water defluorine regulating and controlling device with regenerable defluorine agent for group use |
| CN200940100Y (en) * | 2006-06-26 | 2007-08-29 | 林楚芳 | Fluorine removing apparatus for water-treatment |
| CN203999030U (en) * | 2014-07-31 | 2014-12-10 | 开封金盾压力容器设备有限公司 | Novel environment friendly carbon back phosphatic rock fluoride-removing equipment |
| CN105152242A (en) * | 2015-09-29 | 2015-12-16 | 谭振光 | Natural cooling and sterile overflow injection device for thermal spring drinking natural mineral water |
| CN206613395U (en) * | 2017-04-10 | 2017-11-07 | 谭振光 | Hot spring natural mineral water fluorine removal terminal fluorinated volume enters mixing arrangement against jet flow |
-
2017
- 2017-04-10 CN CN201710230000.4A patent/CN106861474A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6349237A (en) * | 1986-08-14 | 1988-03-02 | Daido Kogyo Co Ltd | Emulsion device |
| CN2608485Y (en) * | 2002-09-03 | 2004-03-31 | 上海莱拓环境科技有限公司 | Drinking water defluorine regulating and controlling device with regenerable defluorine agent for group use |
| CN200940100Y (en) * | 2006-06-26 | 2007-08-29 | 林楚芳 | Fluorine removing apparatus for water-treatment |
| CN203999030U (en) * | 2014-07-31 | 2014-12-10 | 开封金盾压力容器设备有限公司 | Novel environment friendly carbon back phosphatic rock fluoride-removing equipment |
| CN105152242A (en) * | 2015-09-29 | 2015-12-16 | 谭振光 | Natural cooling and sterile overflow injection device for thermal spring drinking natural mineral water |
| CN206613395U (en) * | 2017-04-10 | 2017-11-07 | 谭振光 | Hot spring natural mineral water fluorine removal terminal fluorinated volume enters mixing arrangement against jet flow |
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| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170620 |
|
| WD01 | Invention patent application deemed withdrawn after publication |