CN203582610U - Water softener for blending white spirit to remove fluorine - Google Patents
Water softener for blending white spirit to remove fluorine Download PDFInfo
- Publication number
- CN203582610U CN203582610U CN201320539166.1U CN201320539166U CN203582610U CN 203582610 U CN203582610 U CN 203582610U CN 201320539166 U CN201320539166 U CN 201320539166U CN 203582610 U CN203582610 U CN 203582610U
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- valve
- water
- water softener
- filter
- defluorination
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Abstract
The utility model discloses a water softener for blending white spirit to remove fluorine. The water softener comprises a fluorine removal processor, a resin adsorption water softener and a micro-pore filter device, which are orderly connected, wherein a fluorine-removing filter material is filled into the fluorine removal filter; cation adsorption resin is filled into the resin adsorption water softener; a plurality of polypropylene (PP) or polyethylene (PE) filter elements are arranged inside the micro-pore filter device. The grading treatment effect is achieved by adjusting opening and closing of different valves, the treatment strength is changed by adjusting a flow adjusting valve, and the backwash and regeneration targets are achieved by adjusting opening and closing of different valves.
Description
Technical field
The utility model relates to a kind of drinks production unit, especially water treating equipment during wine blending.
Background technology
Fluorine be distributed in nature very widely, be nonmetal in the most active element, oxidation capacity is very strong, can with most of hydrogeneous compounds as water, ammonia and except helium, neon argon and a small amount of fluorochemical all chemical substances no matter liquid, solid-state or gaseous state react.It is a kind of trace element of needed by human body, the fluorine that human body is taken in from the external world is too much or not enough, capital affects the healthy of people, Drinking Water in China hygienic standard regulation, fluorine content of drinking water must not surpass 1.0 mg/litre, the fluorine-containing higher water of long-term drinking, causes fluorine excessive savings in human body, will cause chronic fluorosis.
Generally have at present the coagulant sedimentation of employing or absorption method to process, but due to the very complex operation of regenerating, many people can not operate, and cause equipment to lose efficacy gradually, fluoride-removing equipment is general simultaneously only processes for defluorination, can not reach the object of demineralized water simultaneously.
Wine blending water not only requires defluorination, require demineralized water simultaneously, remove unnecessary calcium ions and magnesium ions etc., water is novel process white wine important component part, thereby its quality is had to strict demand, hook calls water must be after filtration and sorbent material absorption, or with resin to remove anhydrate middle impurity, particularly metal ion.Otherwise will affect the local flavor of wine and cause muddiness.
Summary of the invention
The purpose of this utility model is to provide a kind of water treatment device that can simultaneously solve water fluoridation for wine blending, softening, turbidity removal, solves the current equipment object of defluorination, softening, turbidity removal simultaneously.
The purpose of this utility model is achieved through the following technical solutions:
Wine blending defluorination water softening device, comprises the softening hydrophone of defluorination treater, resin absorption, the microporous filter that connect successively.Filling defluoridation filter material in described fluorine removing filter, resin absorption is softened the in-built cation-adsorption resin of filling out of hydrophone, and many PP or PE filter core are installed in microporous filter.
Described defluorination treater, resin absorption water softener, microporous filter top are communicated with and are separated by pipeline and valve F9, valve F10, valve F11, defluorination treater 2, resin absorption water softener 3 bottoms are communicated with and are separated by pipeline and valve F2, F4, defluorination treater 2 tops are communicated with and separate with resin absorption water softener 3 bottoms by valve F10, valve F3, valve F4, and resin absorption water softener 3 bottoms are communicated with and separate with microporous filter 4 tops by valve pipe and valve F6.
Wine blending defluorination water softening device, water pump 1 is connected with the bottom of fluorine removing filter 2 with flow control valve F1, valve F2, and water pump 1 outlet is connected with the top of fluorine removing filter 2 by pipeline and valve F13.
Opening degree by adjust flux valve F1 can easily be controlled defluorination and softening intensity.
This device can carry out manipulation of regeneration very easily, do not need to dismantle any element, when filtrate or plastic resin treatment amount reach capacity, only need to adjust the switching of different valves, just can be by the water pump cleaning and regeneration that directly recoils, or by different regenerated liquids respectively pump to defluorination treater or resin absorption water softener.
Described defluorination treater 2, tensimeter and emptying valve P1 are equipped with in top, and sewage draining valve F12 is equipped with in bottom.
Described resin absorption water softener 3, tensimeter and emptying valve P2 are equipped with in top, and sewage draining valve F7 is equipped with in bottom.
Described millipore filter, tensimeter and emptying valve P3 are equipped with in top, and bottom is equipped with and is produced the valve sewage draining valve F8 that holds concurrently.
The machine is also equipped with frame 5 and shifting roller 6.
This wine blending defluorination water softening device is what to realize like this processing of water: while normally producing, open and produce valve F1, produce valve F13, produce valve F3, produce valve F6, produce valve F8, close all the other valves simultaneously, start water pump 1, adjust flux variable valve F1 simultaneously, processed water by pump 1, produce valve F13, defluorination treater 2, produce valve F3, resin absorption water softener 3, produce valve F6, millipore filter 4, produce the object that valve F8 reaches defluorination, softening, turbidity removal.
In the time of only need to softening turbidity removal processing separately, open and produce valve F1, produce valve F13, produce valve F10, produce valve F6, produce valve F8, close all the other valves simultaneously, start water pump 1, while adjust flux variable valve F1, processed water reaches object softening, turbidity removal by pump 1, production valve F13, production valve F10, resin absorption water softener 3, production valve F6, millipore filter 4, production valve F8.
In the time of only need to carrying out turbidity removal processing separately, open and produce valve F1, produce valve F13, produce valve F10, produce valve F11, produce valve F8, close all the other valves simultaneously, start water pump 1, while adjust flux variable valve F1, processed water reaches the object of turbidity removal by pump 1, production valve F13, production valve F10, production valve F11, millipore filter 4, production valve F8.
The machine can easily realize back flushing and regenerative process, when back flushing or regeneration defluorination treater 2, open regeneration valve F2, regeneration valve F9, the switching degree of adjust flux variable valve F1, start water pump 1, can recoil to clean or pump into regenerated liquid and regenerate, the soak solution after regeneration is discharged by wash water valve F12.By which, also can easily realize the regeneration of the resin cation (R.C.) of resin softening water treater and recoil washing.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the utility model is further illustrated:
Fig. 1 is the utility model structural representation;
1 water pump, 2 defluorination treaters, the softening hydrophone of 3 resin absorption, 4 millipore filters in figure, 5 supports, 6 shifting rollers.
Embodiment
Below in conjunction with embodiment, the utility model is described in further detail, but embodiment of the present utility model is not limited to this.
Embodiment
As shown in Figure 1, the utility model wine blending defluorination water softening device, comprise the water pump 1, defluorination treater 2, resin softening water treater 3, the millipore filter 4 that by pipeline, connect successively, all devices is all fixed on support 5, movably roller 6 is installed on support 5, by regulating the switching of different valves can reach the effect of stage treatment, by adjust flux variable valve, can change the intensity of processing.During normal production, open and produce valve F1, produce valve F13, produce valve F3, produce valve F6, produce valve F8, close all the other valves simultaneously, start water pump 1, adjust flux variable valve F1 simultaneously, processed water by pump 1, produce valve F13, defluorination treater 2, produce valve F3, resin absorption water softener 3, produce valve F6, millipore filter 4, produce the object that valve F8 reaches defluorination, softening, turbidity removal.
The above; it is only preferred embodiment of the present utility model; not the utility model is done to any pro forma restriction, in every foundation technical spirit of the present utility model to any simple modification made for any of the above embodiments, equivalent variations, within all falling into protection domain of the present utility model.
Claims (1)
1. wine blending defluorination water softening device, comprise the water pump, defluorination treater, resin softening water treater, the millipore filter that connect successively, filling defluoridation filter material in fluorine removing filter, resin absorption is softened the in-built cation-adsorption resin of filling out of hydrophone, and many PP or PE filter core are installed in microporous filter.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320539166.1U CN203582610U (en) | 2013-08-27 | 2013-08-27 | Water softener for blending white spirit to remove fluorine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320539166.1U CN203582610U (en) | 2013-08-27 | 2013-08-27 | Water softener for blending white spirit to remove fluorine |
Publications (1)
Publication Number | Publication Date |
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CN203582610U true CN203582610U (en) | 2014-05-07 |
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CN201320539166.1U Expired - Fee Related CN203582610U (en) | 2013-08-27 | 2013-08-27 | Water softener for blending white spirit to remove fluorine |
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CN (1) | CN203582610U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106495350A (en) * | 2016-12-09 | 2017-03-15 | 宜兴市苏嘉环保设备有限公司 | Drinking water defluorination turbidity removal filter |
-
2013
- 2013-08-27 CN CN201320539166.1U patent/CN203582610U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106495350A (en) * | 2016-12-09 | 2017-03-15 | 宜兴市苏嘉环保设备有限公司 | Drinking water defluorination turbidity removal filter |
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Date | Code | Title | Description |
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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: 20140507 Termination date: 20150827 |
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EXPY | Termination of patent right or utility model |