CN206173454U - Diaphragm type electrolysis system of multipolar room - Google Patents
Diaphragm type electrolysis system of multipolar room Download PDFInfo
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- CN206173454U CN206173454U CN201621233508.7U CN201621233508U CN206173454U CN 206173454 U CN206173454 U CN 206173454U CN 201621233508 U CN201621233508 U CN 201621233508U CN 206173454 U CN206173454 U CN 206173454U
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Abstract
The utility model discloses a diaphragm type electrolysis system of multipolar room, diaphragm type electrolysis system of multipolar room is including the body, power, electrolysis trough and electrode. The electrolysis trough includes first electrolysis trough, second electrolysis trough and middle electrolysis trough, and components of a whole that can function independently setting between every electrolysis trough can be dismantled and piled up big electrolysis trough of cooperation formation, can select required electrolysis trough quantity according to the actual demand. In addition, a combined electrode is placed in electrolysis trough correspondence in the middle of each, and combined electrode includes combined electrode positive pole and combined electrode negative pole again, arrange anode chamber and cathode chamber respectively in, the electric current and the heat of production when combined electrode can to a great extent reduces the electrolysis are owing to electric current and thermal reduction for what the electrolysis trough was required connects the use amount of electrolytic copper strip to reduce substantially, but also does not need to increase heat rejection apparatus in addition, avoids leading to the fact extra high consumption. The utility model discloses still have advantages such as area is little, with low costs, electrolytic efficiency height.
Description
Technical field
This utility model is related to electrolysis installation field, more particularly to a kind of diaphragm type electrolysis system of many pole rooms.
Background technology
With the development and the raising of living standards of the people of social economy, the electrolysis bath of the widely used environmental protection of people comes
To obtain certain specific product, (such as electrolysis weak brine produces the sodium hypochlorite with very strong sterilizing ability to electrolyte solution
Solution).In a cell, electrolysis electrode is core component, is divided into cathode electrode and anode electrode, on main equipment, typically
There is multigroup electrolysis electrode pair, collectively constitute an electrolysis electrode group, these electrolysis electrode groups are installed in an electrolysis bath
It is interior.
Existing electrolysis bath due to the restriction of its own structure, electrolysis electrode to frequently with parallel structure, i.e., all of
Anode electrode is all docked, and the negative electrode of all electrodes is also all docked, and forms total positive pole and total negative pole access point, that is,
Monopolar electrolyzer.But monopolar electrolyzer there are problems that it is a lot, especially in the case of the multi-group electrode pair of main equipment, this
Kind of parallel connection method can produce very big electric current, and this high current in requisition for very many then to connecing electrolytic copper bar；Simultaneously because
Electric current is big, and the heat of generation is also very high, causes line loss serious, it is necessary to additionally increases heat dissipation equipment, and additionally increases radiating and set
It is standby to cause extra high power consumption.
In addition to the problems that electrode is present, existing electrolysis bath floor space is big, it is impossible to according to the appearance of institute's electrolyte
Amount is actually needed to adjust the quantity of electrolysis bath, causes the raising of electrolysis system holistic cost.
Utility model content
The technical problems to be solved in the utility model, is to provide a kind of diaphragm type electrolysis system of many pole rooms, to solve
The electrolysis electrode of the electrolysis bath of existing main equipment causes to be produced in the case of multipair electrode pair using monopolar electrolyzer
Many electric currents, use excessively connect electrolytic copper bar, produce too high heat, line loss seriously, increase extra heat dissipation equipment and cause extra Gao Gong
Consumption, and existing electrolysis bath floor space is big, assembly and disassembly not aspect, the problems such as cause electrolysis system holistic cost high.
What the technical solution of the utility model was realized in：A kind of diaphragm type electrolysis system of many pole rooms, the multipole
The diaphragm type electrolysis system of room includes body, power supply, electrolysis bath and electrode；The first inlet and second are provided with the body
Inlet；The electrolysis bath middle setting has cavity volume, and the electrolysis bath includes the first electrolysis bath, the second electrolysis bath and at least
Individual middle electrolysis bath, the middle electrolysis bath stacking is arranged between the first electrolysis bath and the second electrolysis bath；First electrolysis
Between groove and middle electrolysis bath, between middle electrolysis bath and middle electrolysis bath, between middle electrolysis bath and the second electrolysis bath respectively
It is provided with cation exchange membrane；The electrode includes anode electrode, cathode electrode and combination electrode, and the combination electrode includes multiple
Composite electrode anode and combination electrode negative electrode；
The anode electrode is placed in the first electrolysis bath, and the cathode electrode is placed in the second electrolysis bath, anode electrode with
Positive source is electrically connected, and cathode electrode is electrically connected with power cathode；
The middle electrolysis bath includes anode chamber and cathode chamber, and the anode chamber is isolated with cathode chamber by dividing plate；Institute
State combination electrode anode to be placed in anode room, and be oppositely arranged with the cathode electrode in the second electrolysis bath or middle electric with adjacent
Combination electrode negative electrode in the negative electrode room of solution groove is oppositely arranged；The combination electrode negative electrode is placed in negative electrode room, and electric with first
Anode electrode in solution groove is oppositely arranged or is oppositely arranged with the combination electrode anode in the anode room of adjacent middle electrolysis bath；
First inlet is communicated respectively with the anode chamber of the first electrolysis bath and middle electrolysis bath, and described second enters
Liquid mouth is communicated respectively with the cathode chamber of the second electrolysis bath and middle electrolysis bath.
Further, between first electrolysis bath and middle electrolysis bath in, between middle electrolysis bath and middle electrolysis bath,
Between be also respectively provided with sealing ring between electrolysis bath and the second electrolysis bath, the shape of the sealing ring and the first electrolysis bath, centre
Electrolysis bath, the shape of the second electrolysis bath are adapted.
Further, fixing device is additionally provided with the middle electrolysis bath, the fixing device is used for combination electrode
It is fixed in middle electrolysis bath.
Further, the fixing device detachably locks with combination electrode.
Further, the combination electrode anode and the cathode electrode in the second electrolysis bath be oppositely arranged or with it is adjacent in
Between electrolysis bath negative electrode room in combination electrode negative electrode be oppositely arranged including：Negative electrode in combination electrode anode and the second electrolysis bath
Electrode is vertically arranged and is parallel to each other, or the combination electrode in the negative electrode room of combination electrode anode and adjacent middle electrolysis bath is cloudy
It is extremely vertically arranged and be parallel to each other；Anode electrode in the combination electrode negative electrode and the first electrolysis bath be oppositely arranged or with phase
Combination electrode anode in the middle of adjacent in the anode room of electrolysis bath be oppositely arranged including：In combination electrode negative electrode and the first electrolysis bath
Anode electrode is vertically arranged and is parallel to each other, or the anode electrode in combination electrode negative electrode and the first electrolysis bath it is vertically arranged and
It is parallel to each other.
Further, the cathode electrode, anode electrode, combination electrode, the material of dividing plate are titanium alloy.
Further, the surface of the anode electrode and cathode electrode is provided with scale prevention coating.
The diaphragm type electrolysis system of many pole rooms of the present utility model has the advantage that：First split sets between each electrolysis bath
Put, detachable stacking cooperatively forms a big electrolysis bath, can according to the actual requirements select required electrolysis bath quantity；Its
Secondary, each middle electrolysis bath correspondence places a combination electrode, and combination electrode includes combination electrode anode and combination electrode negative electrode again,
It is respectively placed in anode chamber and negative electrode room, combination electrode can largely reduce electric current and the heat produced when being electrolysed, by
In the reduction of electric current and heat so that the usage amount for connecing electrolytic copper bar required for electrolysis bath is greatly reduced, but also need not
Increase heat dissipation equipment in addition, it is to avoid cause extra high power consumption.This utility model also has little floor space, low cost, electrolysis
The advantages of efficiency high.
Description of the drawings
Fig. 1 is the overall knot of the diaphragm type electrolysis system of a kind of many pole rooms described in the specific embodiment of this utility model one
Structure sectional view；
Fig. 2 is the compound electric of the diaphragm type electrolysis system of a kind of many pole rooms described in the specific embodiment of this utility model one
The sectional view of pole；
Fig. 3 is the compound electric of the diaphragm type electrolysis system of a kind of many pole rooms described in the specific embodiment of this utility model one
The top view of pole；
Description of reference numerals：
11st, positive source；12nd, power cathode；
2nd, the first electrolysis bath；21st, anode electrode；
3rd, the second electrolysis bath；31st, cathode electrode；
4th, middle electrolysis bath；
5th, combination electrode；51st, combination electrode anode；52nd, combination electrode negative electrode；
6th, body；
7th, cation exchange membrane；
8th, dividing plate；
9th, fixing device；
101st, the first inlet；102nd, the second inlet；
111st, the first liquid outlet；112nd, the second liquid outlet.
Specific embodiment
To describe the technology contents of technical scheme, structural features in detail, purpose and effect being realized, below in conjunction with concrete reality
Apply example and coordinate accompanying drawing to be explained in detail.
Fig. 1 is referred to, is the diaphragm type electrolysis system of a kind of many pole rooms described in the specific embodiment of this utility model one
Overall structure sectional view, the device can solve the electrolysis electrode of the electrolysis bath of existing main equipment and adopt monopolar electrolyzer
And cause to be produced in the case of multipair electrode pair excessive electric current, using excessively connecing electrolytic copper bar, to produce too high heat, line loss serious,
Increase extra heat dissipation equipment and cause extra high power consumption, and the problem such as big, the electrolysis cost height of existing electrolysis bath floor space.
Fig. 1 provides a kind of diaphragm type electrolysis system of many pole rooms, and the diaphragm type electrolysis system of many pole rooms includes this
Body 6, power supply, electrolysis bath and electrode；The first inlet 101 and the second inlet 102 are provided with the body 6；The electrolysis
Groove middle setting has cavity volume, and the electrolysis bath includes the first electrolysis bath 2, the second electrolysis bath 3 and at least one middle electrolysis bath
4, the stacking of middle electrolysis bath 4 is arranged between the first electrolysis bath 2 and the second electrolysis bath 3；First electrolysis bath 2 and centre
It is respectively arranged between electrolysis bath 4, between middle electrolysis bath and middle electrolysis bath, between the middle electrolysis bath 3 of electrolysis bath 4 and second
Cation exchange membrane 7；The electrode includes anode electrode 21, cathode electrode 31 and combination electrode.The anode electrode 21 is placed in
In first electrolysis bath 2, the cathode electrode 31 is placed in the second electrolysis bath 3, and anode electrode 21 is electrically connected with positive source 11, cloudy
Pole electrode 31 is electrically connected with power cathode 12.
As Figure 2-3, the combination electrode 5 includes combination electrode anode 51 and combination electrode negative electrode 52.Combination electrode
Anode 51 and the middle setting of combination electrode negative electrode 52 have dividing plate 8, and combination electrode 5 is placed in middle electrolysis bath, by dividing plate 8 by
Between electrolysis bath be divided into two pole rooms of negative and positive.State combination electrode anode 51 to be placed in anode room, and with the second electrolysis bath in the moon
Pole electrode is oppositely arranged or is oppositely arranged with the combination electrode negative electrode in the negative electrode room of adjacent middle electrolysis bath；The compound electric
Pole negative electrode 52 is placed in negative electrode room, and be oppositely arranged with the anode electrode in the first electrolysis bath or with adjacent middle electrolysis bath
Combination electrode anode in anode room is oppositely arranged.
The middle electrolysis bath 4 includes anode chamber and cathode chamber, and the anode chamber is isolated with cathode chamber by dividing plate 8；
First inlet 101 communicate with the anode chamber of the first electrolysis bath and middle electrolysis bath respectively, second inlet
102 communicate respectively with the cathode chamber of the second electrolysis bath and middle electrolysis bath.First inlet is used for needed for Liu Jin anode chambers
Electrolyte, the electrolyte that the second inlet enters needed for cathode chamber for stream.Accordingly, the first liquid outlet is additionally provided with body
With the second liquid outlet, it is respectively used to flow out anode chamber's product and cathode chamber product.As a example by be electrolysed saturated brine, the first inlet
It is respectively used to flow into saturated brine and NaOH solution with the second inlet, the first liquid outlet and the second liquid outlet are respectively used to flow out
Chlorine and NaCl solution and hydrogen and NaOH solution.
The combination electrode anode be oppositely arranged with the cathode electrode in the second electrolysis bath or with adjacent middle electrolysis bath
Negative electrode room in combination electrode negative electrode be oppositely arranged including：Combination electrode anode is vertical with the cathode electrode in the second electrolysis bath
Arrange and be parallel to each other, or the combination electrode negative electrode in the negative electrode room of combination electrode anode and adjacent middle electrolysis bath vertically sets
Put and be parallel to each other；The combination electrode negative electrode is oppositely arranged or middle electric with adjacent with the anode electrode in the first electrolysis bath
Solution groove anode room in combination electrode anode be oppositely arranged including：Anode electrode in combination electrode negative electrode and the first electrolysis bath
It is vertically arranged and be parallel to each other, or the anode electrode in combination electrode negative electrode and the first electrolysis bath is vertically arranged and mutually flat
OK.
By taking Fig. 1 as an example, the electrolysis bath of the diaphragm type electrolysis system of many pole rooms includes the first electrolysis bath, second electric in Fig. 1
Solution groove and two middle electrolysis baths.Certainly, in other embodiments, the quantity of middle electrolysis bath can be any amount.
In the present embodiment, the first electrolysis bath, the second electrolysis bath, the shape of middle electrolysis bath are adapted, and middle part is provided with cavity volume, in
Between electrolysis bath can stack arrange with increase middle part cavity volume volume, and then increase the anode chamber and the cathode chamber electrolyte volume.In order to just
In explanation, the middle electrolyser that will be close to the first electrolysis bath is called the first middle electrolysis bath, including first anode room and first
Cathode chamber, is provided with the first combination electrode anode in first anode room, the first combination electrode negative electrode is provided with the first negative electrode room.
In the same manner, the middle electrolysis bath that will be close to the second electrolysis bath is called the second middle electrolysis bath, including second plate room and the second negative electrode
Room, is provided with the second combination electrode anode in second plate room, the second combination electrode negative electrode is provided with the second negative electrode room.First
Between electrolysis bath and the first middle electrolysis bath, between the first middle electrolysis bath and the second middle electrolysis bath, the second middle electrolysis bath
Cation exchange membrane is provided between the second electrolysis bath.As a example by be electrolysed saturated brine, the setting of cation exchange membrane can
So that the cation generated in cell reaction is by exchange membrane, and then the NaOH for solving to be generated in cell reaction and CL2 reacts
The reaction for generating NaCLO occurs, and goes out so as to reach the problem for preventing the product for being electrolysed saturated common salt water generating from hybrid reaction occurring
It is existing.
Below the application principle to the combination electrode in middle electrolysis bath in electrolytic process is illustrated.First electrolysis
Anode electrode 21 in groove 2 has taken positive charge due to being connected with positive source 11, and the cathode electrode in the second electrolysis bath 3
31 due to the negative charge for being connected and taking with power cathode 12.First combination electrode, the second combination electrode directly do not connect with power supply
Touch, also be connected with anode electrode or cathode electrode directly contact that (middle setting has cation to interact to touch, combination electrode and anode
The gap of electrode or cathode electrode coordinates and is not connected to).It is former according to charge inducing because anode electrode 21 has taken positive charge
Reason, negative charge on the first combination electrode Ka band in the negative electrode room in the first electrolysis bath, in the same manner, due to the band of cathode electrode 31
Negative charge is gone up, positive charge on the second combination electrode anode strap in the anode room in the second electrolysis bath.Electrolysis in the middle of first
Groove was both adjacent with the first electrolysis bath 2, at the same it is also adjacent with the second middle electrolysis bath, due to the first combination electrode negative electrode positively charged
Lotus, then for the first combination electrode, its combination electrode anode positively charged in the anode room of the first middle electrolysis bath
Lotus.That is, the first combination electrode has positive and negative charge and situation about depositing in anode chamber and cathode chamber.Second compound electric
The electrically charged situation of pole male or female can be obtained in the same manner.
Electric current from positive pole to negative pole, sequentially pass through anode electrode, the first combination electrode negative electrode, the first combination electrode anode,
Second combination electrode negative electrode, the second combination electrode anode, cathode electrode form loop.That is electrolyte is by above-mentioned several electricity
Pole conducting is adjacent, and according to series circuit voltage divider principle, electric current can at double decline according to the electrodeplate connected such that it is able to very
Electric current and the heat produced when electrolysis electrode is electrolysed is reduced in big degree, due to the reduction of electric current and heat so that electrolysis bath institute
The usage amount for connecing electrolytic copper bar for needing is greatly reduced, but also need not in addition increase heat dissipation equipment, it is to avoid cause extra
High power consumption.Meanwhile, total decomposition voltage is by the electricity of (series connection here refers to that electrolyte is in series) of connecting in combination electrode group
Significantly improving for number of poles, drastically increases the electrolytic efficiency of electrolysis bath.
In certain embodiments, fixing device is additionally provided with the middle electrolysis bath, the fixing device is used for will be multiple
Composite electrode is fixed in middle electrolysis bath.Target contact due to one side with power positive cathode, on the other hand and not with
Anode electrode or cathode electrode directly contact, so that being fixed by fixing device.In certain embodiments, it is described solid
Determine device detachably to lock with target.So that fixing device can be changed at any time, maintenance cost is reduced.The fixation
Device can adopt bolt arrangement, and the bolt arrangement is corrosion resistant insulated bolt, on the one hand adapts to the electricity of different electrolytes
Solution environment, on the other hand insulation can ensure that fixing device does not produce impact to the electrolysis of electrode.Certainly, fixing device can also
Target is fixed using other structures, is such as screwed, be fixed structure.
In certain embodiments, the surface of the anode electrode and cathode electrode is provided with scale prevention coating.By arranging
Scale prevention coating, can effectively prevent the accumulation of the surface smut of anode electrode and cathode electrode, affect anode electrode and negative electrode electricity
The electrolytic efficiency of pole, while being also beneficial to extend the service life of anode electrode or cathode electrode.
In certain embodiments, between first electrolysis bath and middle electrolysis bath, middle electrolysis bath and middle electrolysis bath
Between, sealing ring, the shape of the sealing ring and the first electrolysis are also respectively provided between middle electrolysis bath and the second electrolysis bath
Groove, middle electrolysis bath, the shape of the second electrolysis bath are adapted.The effect of sealing ring is that the leakage pair for preventing electrolyte sets
It is standby to cause corrosion, the work of equipment is affected, also function to prevent from being electrolysed the gases did escape that saturated aqueous common salt is produced, H2 meets fiery pole
Burning easily occurs may be caused to damage to equipment, and CL2 has toxicity, personal safety can be threatened, so sealing ring
Arrange extremely important；It is higher that the shape of sealing ring is adapted its sealing with the shape of electrolysis bath.
In certain embodiments, the material of the sealing ring is four fluorubber.Four fluorubber recoverabilities are very good, use four
The only good airproof performance of sealing ring 8 that fluorubber is made, and can be reused based on its good restorative sealing ring.
Of coursing sealing ring can also be made with other materials, can carry out good sealing to electrolysis bath.
In certain embodiments, the cathode electrode, anode electrode, combination electrode, the material of dividing plate are titanium alloy.Titanium is closed
Gold utensil has good electric conductivity and anticorrosive property, is well suited as the material of electrode.
The diaphragm type electrolysis system of many pole rooms of the present utility model has the advantage that：First split sets between each electrolysis bath
Put, detachable stacking cooperatively forms a big electrolysis bath, can according to the actual requirements select required electrolysis bath quantity；Its
Secondary, each middle electrolysis bath correspondence places a combination electrode, and combination electrode includes combination electrode anode and combination electrode negative electrode again,
It is respectively placed in anode chamber and negative electrode room, combination electrode can largely reduce electric current and the heat produced when being electrolysed, by
In the reduction of electric current and heat so that the usage amount for connecing electrolytic copper bar required for electrolysis bath is greatly reduced, but also need not
Increase heat dissipation equipment in addition, it is to avoid cause extra high power consumption.This utility model also has little floor space, low cost, electrolysis
The advantages of efficiency high.
Although being described to the various embodiments described above, those skilled in the art once know basic wound
The property made concept, then can make other change and modification, so the foregoing is only reality of the present utility model to these embodiments
Example is applied, scope of patent protection of the present utility model, every utilization this utility model description and accompanying drawing content is not thereby limited
The equivalent structure made or equivalent flow conversion, or other related technical fields are directly or indirectly used in, include in the same manner
Within scope of patent protection of the present utility model.
Claims (7)
1. a kind of diaphragm type electrolysis system of many pole rooms, it is characterised in that the diaphragm type electrolysis system of many pole rooms includes this
Body, power supply, electrolysis bath and electrode；The first inlet and the second inlet are provided with the body；Set in the middle of the electrolysis bath
Cavity volume is equipped with, the electrolysis bath includes the first electrolysis bath, the second electrolysis bath and at least one middle electrolysis bath, the middle electricity
Solution groove stacking is arranged between the first electrolysis bath and the second electrolysis bath；Between first electrolysis bath and middle electrolysis bath, it is middle
Cation exchange membrane is respectively arranged between electrolysis bath and middle electrolysis bath, between middle electrolysis bath and the second electrolysis bath；It is described
Electrode includes anode electrode, cathode electrode and combination electrode, and the combination electrode includes that combination electrode anode and combination electrode are cloudy
Pole；
The anode electrode is placed in the first electrolysis bath, and the cathode electrode is placed in the second electrolysis bath, anode electrode and power supply
Positive pole is electrically connected, and cathode electrode is electrically connected with power cathode；
The middle electrolysis bath includes anode chamber and cathode chamber, and the anode chamber is isolated with cathode chamber by dividing plate；It is described multiple
Composite electrode anode is placed in anode room, and be oppositely arranged with the cathode electrode in the second electrolysis bath or with adjacent middle electrolysis bath
Negative electrode room in combination electrode negative electrode be oppositely arranged；The combination electrode negative electrode is placed in negative electrode room, and with the first electrolysis bath
Interior anode electrode is oppositely arranged or is oppositely arranged with the combination electrode anode in the anode room of adjacent middle electrolysis bath；
First inlet is communicated respectively with the anode chamber of the first electrolysis bath and middle electrolysis bath, second inlet
Communicate with the cathode chamber of the second electrolysis bath and middle electrolysis bath respectively.
2. the diaphragm type electrolysis system of many pole rooms as claimed in claim 1, it is characterised in that first electrolysis bath with it is middle
It is also respectively provided between electrolysis bath, between middle electrolysis bath and middle electrolysis bath, between middle electrolysis bath and the second electrolysis bath
Sealing ring, the shape of the sealing ring is adapted with the shape of the first electrolysis bath, middle electrolysis bath, the second electrolysis bath.
3. the diaphragm type electrolysis system of many pole rooms as claimed in claim 1, it is characterised in that also sets in the middle electrolysis bath
Fixing device is equipped with, the fixing device is used to that combination electrode to be fixed in middle electrolysis bath.
4. the diaphragm type electrolysis system of many pole rooms as claimed in claim 3, it is characterised in that the fixing device and compound electric
Extremely detachably lock.
5. the diaphragm type electrolysis system of many pole rooms as claimed in claim 1, it is characterised in that the combination electrode anode and the
Cathode electrode in two electrolysis baths is oppositely arranged or relative with the combination electrode negative electrode in the negative electrode room of adjacent middle electrolysis bath
Setting includes：Cathode electrode in combination electrode anode and the second electrolysis bath is vertically arranged and is parallel to each other, or combination electrode
Combination electrode negative electrode in the negative electrode room of anode and adjacent middle electrolysis bath is vertically arranged and is parallel to each other；The combination electrode is cloudy
Pole is oppositely arranged or positive with the combination electrode in the anode room of adjacent middle electrolysis bath with the anode electrode in the first electrolysis bath
Pole be oppositely arranged including：Anode electrode in combination electrode negative electrode and the first electrolysis bath is vertically arranged and is parallel to each other, Huo Zhefu
Anode electrode in composite electrode negative electrode and the first electrolysis bath is vertically arranged and is parallel to each other.
6. the diaphragm type electrolysis system of many pole rooms as claimed in claim 1, it is characterised in that the cathode electrode, anode electricity
Pole, combination electrode, the material of dividing plate are titanium alloy.
7. the diaphragm type electrolysis system of many pole rooms as claimed in claim 1, it is characterised in that the anode electrode and negative electrode electricity
The surface of pole is provided with scale prevention coating.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621233508.7U CN206173454U (en) | 2016-11-17 | 2016-11-17 | Diaphragm type electrolysis system of multipolar room |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621233508.7U CN206173454U (en) | 2016-11-17 | 2016-11-17 | Diaphragm type electrolysis system of multipolar room |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206173454U true CN206173454U (en) | 2017-05-17 |
Family
ID=58685390
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621233508.7U Active CN206173454U (en) | 2016-11-17 | 2016-11-17 | Diaphragm type electrolysis system of multipolar room |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206173454U (en) |
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2016
- 2016-11-17 CN CN201621233508.7U patent/CN206173454U/en active Active
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Address after: Cangshan District of Fuzhou City, Fujian province 350000 to build a new town, Jinshan Road No. 618 Jinshan Industrial Zone juyuanzhou Park 62 floor Patentee after: Fujian Haoda intelligent Polytron Technologies Inc Address before: Cangshan District of Fuzhou City, Fujian province 350000 to build a new town, Jinshan Road No. 618 Jinshan Industrial Zone juyuanzhou Park 62 floor Patentee before: FUJIAN HADA INTELLIGENCE TECHNOLOGY CO., LTD. |
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