CN206015104U - Generator main frame is used in sodium hypochlorite production - Google Patents
Generator main frame is used in sodium hypochlorite production Download PDFInfo
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- CN206015104U CN206015104U CN201620968468.4U CN201620968468U CN206015104U CN 206015104 U CN206015104 U CN 206015104U CN 201620968468 U CN201620968468 U CN 201620968468U CN 206015104 U CN206015104 U CN 206015104U
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Abstract
The utility model discloses generator main frame is used in a kind of sodium hypochlorite production, including frame, frame is provided with the one-level electrolysis bath that cascade is arranged, second electrolyser, three-level electrolysis bath ... and N level electrolysis baths, the liquid outlet of one-level upper part of the electrolytic cell is connected with the inlet of second electrolyser bottom, the liquid outlet on second electrolyser top is connected with the inlet of three-level electrolysis bath bottom, ... the liquid outlet of (N 1) level upper part of the electrolytic cell is connected with the inlet of N level electrolysis baths bottom, the inlet of one-level electrolysis bath bottom is connected with the weak brine water inlet pipe positioned at bottom of the frame, flushing water water inlet pipe and acid washing water water inlet pipe, the top liquid outlet of N level electrolysis baths is connected with product drain pipe, one-level electrolysis bath, second electrolyser, the top of three-level electrolysis bath ... and N level electrolysis baths is connected with the hydrogen discharging pipe for extending to frame top.This utility model can continuously produce a large amount of liquor natrii hypochloritises, improve electrolytic efficiency, and electrolysis effectiveness is good, is easy to Automated condtrol.
Description
Technical field
This utility model is related to a kind of sodium hypochlorite production generator main frame.
Background technology
Sodium hypochlorite is mainly used in bleaching, Industrial Wastewater Treatment, papermaking, weaving, pharmacy, fine chemistry industry, disinfecting etc.
Various fields, prior art produce sodium hypochlorite with many using electrolysis, but existing equipment yields poorly, it is impossible to connection production,
Electrolysis effectiveness is not good, and automatic controlling level is low, has had a strong impact on the production of product.
Utility model content
This utility model provides one kind and can continuously produce a large amount of liquor natrii hypochloritises, substantially increases electrolytic efficiency, electricity
Solution effect is good, is easy to Automated condtrol, and generator main frame is used in the sodium hypochlorite production for reducing the labor intensity of workman.
For solving above-mentioned technical problem, the technical solution of the utility model is：Generator master is used in a kind of sodium hypochlorite production
Machine, including frame, the frame is provided with one-level electrolysis bath, second electrolyser, three-level electrolysis bath ... and the N levels that cascade is arranged
Electrolysis bath, the liquid outlet of the one-level upper part of the electrolytic cell are connected with the inlet of the second electrolyser bottom, two grades of electricity
The liquid outlet on solution groove top is connected with the inlet of the three-level electrolysis bath bottom ... ... (N-1) the level upper part of the electrolytic cell
Liquid outlet is connected with the inlet of the N levels electrolysis bath bottom, and the inlet of the one-level electrolysis bath bottom is connected with positioned at institute
Weak brine water inlet pipe, flushing water water inlet pipe and the acid washing water water inlet pipe of bottom of the frame is stated, the one-level electrolysis bath bottom is additionally provided with
Drain pipe, the drain pipe are connected with blow-off pipe and pickling return duct positioned at the bottom of the frame, the N levels electrolysis bath upper
Portion's liquid outlet is connected with the upper of product drain pipe, one-level electrolysis bath, second electrolyser, three-level electrolysis bath ... and N level electrolysis baths
Portion is connected with the hydrogen discharging pipe for extending to the frame top.
As preferred technical scheme, the one-level electrolysis bath, the second electrolyser, the three-level electrolysis bath ... and
The N levels electrolysis bath is sequentially located in the frame from the bottom to top.
Used as the improvement to above-mentioned technical proposal, the frame is additionally provided with cooler bin, and the sidepiece of the cooler bin is provided with cold
But water water inlet pipe and cooling water outlet pipe, the one-level electrolysis bath, the second electrolyser, the three-level electrolysis bath ... and institute
State and in N level electrolysis baths, be provided with electrolysis cooling tube, the two ends of the electrolysis cooling tube each extend over out electrolysis bath with the cooler bin
Connection.
As the further improvement to above-mentioned technical proposal, the one-level electrolysis bath, the second electrolyser, the three-level
Electrolysis bath ... and the transparent setting of the N levels electrolysis bath.
Used as the further improvement to above-mentioned technical proposal, the inlet of the one-level electrolysis bath bottom is also associated with being located at
The auxiliary blow-off pipe of the bottom of the frame, the auxiliary blow-off pipe are provided with auxiliary blowdown electrodynamic valve.
Used as the further improvement to above-mentioned technical proposal, it is electronic that the weak brine water inlet pipe is provided with weak brine water inlet
Valve；The flushing water water inlet pipe is provided with flushing water water inlet electrodynamic valve；The acid washing water water inlet pipe is provided with acid washing water and enters water power
Dynamic valve.
Used as the further improvement to above-mentioned technical proposal, the product drain pipe is provided with product and goes out liquid electrodynamic valve.
Used as the further improvement to above-mentioned technical proposal, the blow-off pipe is provided with blowdown electrodynamic valve, the pickling
Return duct is provided with acid solution backflow electrodynamic valve.
Used as especially further improving to above-mentioned technical proposal, the hydrogen discharging pipe is provided with row's hydrogen electrodynamic valve.
As a result of above-mentioned technical proposal, generator main frame is used in a kind of sodium hypochlorite production, including frame, is set in frame
One-level electrolysis bath, second electrolyser, three-level electrolysis bath ... and the N level electrolysis baths for having cascade to arrange, one-level upper part of the electrolytic cell
Liquid outlet is connected with the inlet of second electrolyser bottom, and the liquid outlet on second electrolyser top is entered with three-level electrolysis bath bottom
Liquid mouth connects ... ..., and (N-1) liquid outlet of level upper part of the electrolytic cell is connected with the inlet of N level electrolysis baths bottom, one-level electrolysis bath
The inlet of bottom is connected with the weak brine water inlet pipe positioned at bottom of the frame, flushing water water inlet pipe and acid washing water water inlet pipe, one-level
Electrolysis bath bottom is additionally provided with drain pipe, and drain pipe is connected with blow-off pipe and pickling return duct positioned at bottom of the frame, N level electrolysis baths
Top liquid outlet be connected with product drain pipe, one-level electrolysis bath, second electrolyser, three-level electrolysis bath ... and N level electrolysis baths
Top be connected with the hydrogen discharging pipe for extending to frame top.Weak brine enters into enter in one-level electrolysis bath through weak brine water inlet pipe
Row electrolysis, due to constantly newly entering weak brine, the saline and liquor natrii hypochloritises after one-level electrolysis is from one-level for one-level electrolysis bath
Upper part of the electrolytic cell liquid outlet is forced into second electrolyser bottom inlet, enters in second electrolyser, and in the same manner, previous stage is electrolysed
Saline and liquor natrii hypochloritises afterwards is pressed in next stage electrolysis bath.Until the saline in N level electrolysis baths is electrolysed completely, by
Product drain pipe is exported, and constantly produces liquor natrii hypochloritises.Flushing water water inlet pipe and acid washing water water inlet pipe can be put into flushing water
Or acid washing water, electrolysis bath effectively to be cleared up, it is ensured that electrolysis effectiveness, blow-off pipe and pickling return duct can release waste liquid, side
Just use, hydrogen discharging pipe can discharge the hydrogen in electrolytic process.This utility model can continuously produce a large amount of liquor natrii hypochloritises,
Electrolytic efficiency is substantially increased, electrolysis effectiveness is good, be easy to Automated condtrol, reduce the labor intensity of workman.
Description of the drawings
The following drawings is only intended to, in this utility model is done schematic illustration and explanation, not limit model of the present utility model
Enclose.Wherein：
Fig. 1 is the structural representation of this utility model embodiment；
Fig. 2 is the left view of Fig. 1；
Fig. 3 is the top view of this utility model embodiment.
In figure：1- frames；2- one-level electrolysis baths；3- second electrolysers；4- three-level electrolysis baths；5- weak brine water inlet pipes；6-
Flushing water water inlet pipe；7- acid washing water water inlet pipes；8- drain pipies；9- blow-off pipes；10- pickling return ducts；11- product drain pipes；12-
Hydrogen discharging pipe；13- cooler bins；14- cooling water inlet pipes；15- cooling water outlet pipes；16- aids in blow-off pipe；17- auxiliary blowdown electricity
Dynamic valve；18- weak brines water inlet electrodynamic valve；19- flushing waters water inlet electrodynamic valve；20- acid washing waters water inlet electrodynamic valve；21- products go out liquid
Electrodynamic valve；22- blowdown electrodynamic valves；23- acid solutions backflow electrodynamic valve；24- arranges hydrogen electrodynamic valve.
Specific embodiment
With reference to the accompanying drawings and examples, this utility model is expanded on further.In the following detailed description, only by saying
Bright mode describes some one exemplary embodiments of the present utility model.Undoubtedly, one of ordinary skill in the art can be with
Recognize, in the case of without departing from spirit and scope of the present utility model, can with a variety of modes to described
Embodiment is modified.Therefore, accompanying drawing and description are inherently illustrative, rather than for limiting the protection of claim
Scope.
As shown in Figure 1, Figure 2 and Figure 3, the present embodiment is with one-level electrolysis bath 2, second electrolyser 3, three-level electrolysis bath 4
It is illustrated.
Generator main frame is used in a kind of sodium hypochlorite production, and including frame 1, frame 1 is provided with the one-level electrolysis that cascade is arranged
The inlet of groove 2, second electrolyser 3, three-level electrolysis bath 4, the liquid outlet on 2 top of one-level electrolysis bath and 3 bottom of second electrolyser
Connection, the liquid outlet on 3 top of second electrolyser is connected with the inlet of 4 bottom of three-level electrolysis bath, and 2 bottom of one-level electrolysis bath is entered
Liquid mouth is connected with the weak brine water inlet pipe 5 positioned at 1 bottom of frame, flushing water water inlet pipe 6 and acid washing water water inlet pipe 7, and one-level is electrolysed
2 bottom of groove is additionally provided with drain pipe 8, and drain pipe 8 is connected with blow-off pipe 9 and pickling return duct 10 positioned at 1 bottom of frame, three-level electricity
The top liquid outlet of solution groove 4 is connected with product drain pipe 11, one-level electrolysis bath 2, second electrolyser 3 and three-level electrolysis bath 4 upper
Portion is connected with the hydrogen discharging pipe 12 extended at the top of frame 1.Weak brine is entered in one-level electrolysis bath 2 through weak brine water inlet pipe 5
It is electrolysed, due to constantly newly entering weak brine, the saline and liquor natrii hypochloritises after one-level electrolysis is from one for one-level electrolysis bath 2
Level 2 top liquid outlet of electrolysis bath is forced into 3 bottom inlet of second electrolyser, enters in second electrolyser 3, in the same manner, previous
Saline and liquor natrii hypochloritises after level electrolysis is pressed in next stage electrolysis bath 2.Until the saline in three-level electrolysis bath 4 is complete
Full electrolysis, is exported by product drain pipe 11, constantly produces liquor natrii hypochloritises.7 energy of flushing water water inlet pipe 6 and acid washing water water inlet pipe
Flushing water or acid washing water is enough put into, electrolysis bath is effectively cleared up, it is ensured that electrolysis effectiveness, blow-off pipe 9 and pickling return duct 10
Waste liquid can be released, convenient use, hydrogen discharging pipe 12 can discharge the hydrogen in electrolytic process.The present embodiment continuously can be produced greatly
Amount liquor natrii hypochloritises, substantially increase electrolytic efficiency, and electrolysis effectiveness is good, are easy to Automated condtrol, and the work for reducing workman is strong
Degree.
One-level electrolysis bath 2, second electrolyser 3, three-level electrolysis bath 4 ... and N levels electrolysis bath are sequentially located at machine from the bottom to top
On frame 1, said structure can make to enter into liquid from electrolysis bath bottom, and after electrolysis, saline and liquor natrii hypochloritises are pressed into by pressure
Dao next stage electrolysis bath 2 in.
Frame 1 is additionally provided with cooler bin 13, and the sidepiece of cooler bin 13 is provided with cooling water inlet pipe 14 and cooling water outlet pipe 15,
Electrolysis cooling tube is provided with one-level electrolysis bath 2, second electrolyser 3, three-level electrolysis bath 4 ... and N level electrolysis baths, is electrolysed cooling tube
Two ends each extend over out electrolysis bath and be connected with cooler bin 13, said structure ensure that the temperature of electrolysis, it is ensured that electrolysis effectiveness.
One-level electrolysis bath 2, second electrolyser 3, three-level electrolysis bath 4 ... and the transparent setting of N levels electrolysis bath, said structure
It is easy to observe electrolysis situation.
The inlet of 2 bottom of one-level electrolysis bath is also associated with the auxiliary blow-off pipe 16 positioned at 1 bottom of frame, aids in blow-off pipe
16 are provided with auxiliary blowdown electrodynamic valve 17；Weak brine water inlet pipe 5 is provided with weak brine water inlet electrodynamic valve 18；Flushing water water inlet pipe 6
It is provided with flushing water water inlet electrodynamic valve 19；Acid washing water water inlet pipe 7 is provided with acid washing water water inlet electrodynamic valve 20；On product drain pipe 11
It is provided with product and goes out liquid electrodynamic valve 21；Blow-off pipe 9 is provided with blowdown electrodynamic valve 22, and it is electronic that pickling return duct 10 is provided with acid solution backflow
Valve 23；12 row of being provided with hydrogen electrodynamic valve 24 of hydrogen discharging pipe, each electrodynamic valve is easy to Automated condtrol.
Ultimate principle of the present utility model, principal character and advantage of the present utility model has been shown and described above.One's own profession
The technical staff of industry it should be appreciated that this utility model is not restricted to the described embodiments, described in above-described embodiment and description
Principle of the present utility model is described simply, on the premise of without departing from this utility model spirit and scope, this utility model is also
Various changes and modifications are had, these changes and improvements are both fallen within the range of claimed this utility model.This utility model
Claimed scope is by appending claims and its equivalent thereof.
Claims (9)
1. generator main frame is used in a kind of sodium hypochlorite production, including frame, it is characterised in that：The frame is provided with cascade and arranges
One-level electrolysis bath, second electrolyser, three-level electrolysis bath ... and N level electrolysis baths, the liquid outlet of the one-level upper part of the electrolytic cell
It is connected with the inlet of the second electrolyser bottom, under the liquid outlet on the second electrolyser top and the three-level electrolysis bath
Inlet connection ... ... the liquid outlet of (N-1) the level upper part of the electrolytic cell in portion is connected with the inlet of the N levels electrolysis bath bottom
Connect, the inlet of the one-level electrolysis bath bottom is connected with the weak brine water inlet pipe positioned at the bottom of the frame, flushing water water inlet
Pipe and acid washing water water inlet pipe, the one-level electrolysis bath bottom are additionally provided with drain pipe, and the drain pipe is connected with positioned at the frame
The blow-off pipe of bottom and pickling return duct, the top liquid outlet of the N levels electrolysis bath are connected with product drain pipe, and one-level is electrolysed
The top of groove, second electrolyser, three-level electrolysis bath ... and N level electrolysis baths is connected with the row's hydrogen for extending to the frame top
Pipe.
2. generator main frame is used in sodium hypochlorite production as claimed in claim 1, it is characterised in that：The one-level electrolysis bath, institute
State second electrolyser, the three-level electrolysis bath ... and the N levels electrolysis bath is sequentially located in the frame from the bottom to top.
3. generator main frame is used in sodium hypochlorite production as claimed in claim 1, it is characterised in that：The frame is additionally provided with cooling
Case, the sidepiece of the cooler bin are provided with cooling water inlet pipe and cooling water outlet pipe, the one-level electrolysis bath, two grades of electrolysis
Electrolysis cooling tube, the two ends difference of the electrolysis cooling tube is provided with groove, the three-level electrolysis bath ... and the N levels electrolysis bath
Extend electrolysis bath to be connected with the cooler bin.
4. generator main frame is used in sodium hypochlorite production as claimed in claim 1, it is characterised in that：The one-level electrolysis bath, institute
State second electrolyser, the three-level electrolysis bath ... and the transparent setting of the N levels electrolysis bath.
5. generator main frame is used in sodium hypochlorite production as claimed in claim 1, it is characterised in that：The one-level electrolysis bath bottom
Inlet be also associated with the auxiliary blow-off pipe positioned at the bottom of the frame, it is electronic that the auxiliary blow-off pipe is provided with auxiliary blowdown
Valve.
6. generator main frame is used in sodium hypochlorite production as claimed in claim 1, it is characterised in that：On the weak brine water inlet pipe
It is provided with weak brine water inlet electrodynamic valve；The flushing water water inlet pipe is provided with flushing water water inlet electrodynamic valve；The acid washing water water inlet pipe
It is provided with acid washing water water inlet electrodynamic valve.
7. generator main frame is used in sodium hypochlorite production as claimed in claim 1, it is characterised in that：Set on the product drain pipe
There is product to go out liquid electrodynamic valve.
8. generator main frame is used in sodium hypochlorite production as claimed in claim 1, it is characterised in that：The blow-off pipe is provided with row
Dirty electrodynamic valve, the pickling return duct are provided with acid solution backflow electrodynamic valve.
9. the sodium hypochlorite production generator main frame as described in claim 1 to 8 is arbitrary, it is characterised in that：The hydrogen discharging pipe
The row's of being provided with hydrogen electrodynamic valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620968468.4U CN206015104U (en) | 2016-08-29 | 2016-08-29 | Generator main frame is used in sodium hypochlorite production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620968468.4U CN206015104U (en) | 2016-08-29 | 2016-08-29 | Generator main frame is used in sodium hypochlorite production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206015104U true CN206015104U (en) | 2017-03-15 |
Family
ID=58253378
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620968468.4U Active CN206015104U (en) | 2016-08-29 | 2016-08-29 | Generator main frame is used in sodium hypochlorite production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206015104U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106148994A (en) * | 2016-08-29 | 2016-11-23 | 潍坊和创环保设备有限公司 | Sodium hypochlorite produces and uses generator main frame |
| CN113697910A (en) * | 2021-09-17 | 2021-11-26 | 深圳科瑞德健康科技有限公司 | Modularization salt chlorine degassing unit |
-
2016
- 2016-08-29 CN CN201620968468.4U patent/CN206015104U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106148994A (en) * | 2016-08-29 | 2016-11-23 | 潍坊和创环保设备有限公司 | Sodium hypochlorite produces and uses generator main frame |
| CN113697910A (en) * | 2021-09-17 | 2021-11-26 | 深圳科瑞德健康科技有限公司 | Modularization salt chlorine degassing unit |
| CN113697910B (en) * | 2021-09-17 | 2022-06-21 | 深圳科瑞德健康科技有限公司 | Modularization salt chlorine degassing unit |
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|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |