CN2097839U - Seal multi-layer plate type no-diaphragm electrolysis generator - Google Patents
Seal multi-layer plate type no-diaphragm electrolysis generator Download PDFInfo
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- CN2097839U CN2097839U CN 91202408 CN91202408U CN2097839U CN 2097839 U CN2097839 U CN 2097839U CN 91202408 CN91202408 CN 91202408 CN 91202408 U CN91202408 U CN 91202408U CN 2097839 U CN2097839 U CN 2097839U
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Abstract
The utility model relates to a seal multi-layer plate type no-diaphragm electrolysis generator, which belongs to the field of environmental sanitation equipment, comprising a control unit (mainly including instruments, switches, conducting wires) and an electrolytic unit. The utility model presents a new structure of the electrolytic unit, comprising a plastic cap plate (5), rubber gaskets (6) and (7), cathode metal plates (4), cathodes metal plates with coating layer (1), a plastic bowl construction (2), bipolarity metal plates with coating layer (3), locating pieces (11), plastic insulation jacket tubes (12), screw bolts (8), nuts (9), gaskets (10). Different ends of the metal plates have diversion holes (14), the parts, which are the cathodes metal plates with coating layer (1), the cathodes metal plates (4) and the bipolarity metal plates with coating layer (3), are formed into many pairs of anode and cathode poles, the electrolytic solution can flow backfoldingly between polar plates, and the electrolytic area is increased, but the electrolytic current value is not changed.
Description
Airtight multi-layer plate-type diaphragm-free electrolysis producer belongs to the sanitation equipment field.
Airtight multi-layer plate-type diaphragm-free electrolysis producer is to utilize lower concentration salt solution to connect electrolysis under the galvanic situation as electrolytic solution at electrode, is used for multiple uses such as sterilization and disinfection and produce the chlorine bleach liquor.(clorox) producer main composition of known a kind of airtight tubular type diaphragm-free electrolysis is as follows: it (mainly comprises instrument by electric control unit, switch, lead) and electrolysis cells (mainly comprise electrolyzer, electrode, sealing member, positioning element, fastening piece) forms, its electrode is a hollow edged electrode, the producer of this structure has used in some departments, but the increase of the area that its Faradaic current value will be used with metal electrode increases, its electrolysis significant part space availability ratio is low, thereby the volume of producer is bigger, location and seal structure complex between its electrode, thereby be not easy to make.
The purpose of this utility model is to be to overcome weak point of the prior art, a kind of novel airtight multi-layer plate-type diaphragm-free electrolysis producer is provided, it not only can be under the prerequisite that does not increase the Faradaic current value, method with the number that increases the bipolarity metal sheet reaches the purpose that increases the metal electrode board usable floor area, and its electrolysis significant part space availability ratio height, thereby dwindled the volume of producer effectively, the location is simple with sealed structure between the electrode metal plate that is adopted simultaneously, thereby makes easily.
The utility model is achieved in that sees that accompanying drawing 1 is to accompanying drawing 3, during as the producer horizontal positioned, (mainly comprise instrument by electric control unit, switch, lead) and electrolysis cells (mainly comprise electrolyzer, electrode, sealing member, positioning element, fastening piece) the airtight multi-layer plate-type of Zu Chenging does not have PT film electrolysis generator, it is characterized in that having the structure of a novel electrolysis cells, it is by having fluid guidance port (15) on it and wearing plastic insulation sleeve pipe (12) and wear the two piece outside plastic cover plates (5) of bolt with the hole, two outside rubber gaskets (7), inboard rubber gasket (6), a cathodic metal plate (4), cated anode metal plate (1) is gone up in its working face one side (upper surface), plastic groove (2), there is coating can do anode on a side (upper surface) on its plate and opposite side (lower surface) face can be done the bipolarity metal sheet (3) of negative electrode, be used for determining the positioning element (11) of distance between metal sheet, plastic insulation sleeve pipe (12), bolt (8), nut (9) and packing ring (10) are formed.Electrolytic solution pod apertures (14) is arranged on the electrode metal plate, plastic insulation sleeve pipe and bolt are with hole and electrolyzer apertura lateralis (16), electrolytic solution pod apertures (14) is also arranged on the bipolarity metal sheet, for two adjacent metal sheets, hole (a 14) end disposed thereon on metal sheet, and the other end that the hole (14) on another piece metal sheet should be disposed thereon (be on the two boards hole (14) not at same end).
The utility model is made up of electric control unit and electrolysis cells, and electric control unit is a known technology, and electrolysis cells has provided new structure.
Different according to different needs electrolysis cells size and shape.The bipolarity metal sheet can parallel placement several, but is at least one.
Can connect to form the multiple-unit electrolysis generator to the fluid guidance port of several electrolysis cells (15) with flexible pipe or hard tube as required.Inboard fluted (13) of the plate that the fluid guidance port (15) on plastic cover plate (5) is located are used to improve electrolyte flow.
Part (1), part (2), part (3), part (4), part (5), part (6), part (7), part (8), part (9), part (10), part (11), part (12) have been formed electrolyzer after attaching together.
Only positive and negative utmost point metal sheet is connected direct supply, the not direct feed of bipolar electrode metal sheet, bipolarity metal sheet top is metal anode, followingly is metallic cathode, only depend on the electrolytic solution conduction between metal polar plate, because the difference end at each metal sheet has flow-guiding mouth (14), flow through so electrolytic solution can repeatedly be turned back between anode metal plate and cathodic metal plate, using less Faradaic current to carry out to obtain under the electrolytic situation chlorine bleach liquor of high yield.
Advantage of the present utility model: this producer can be under the prerequisite that does not increase the Faradaic current value, reached the purpose that increases the metal electrode usable floor area with the number that increases the bipolarity metal electrode board, its significant part space availability ratio height, thereby dwindled the volume of producer effectively, clorox productive rate height, the location is simple with sealed structure between metal electrode board simultaneously, is easy to make, and maintenance is convenient.Can change the number of bipolarity metal electrode board as required, and the fluid guidance port of several electrolysis cells can be connected into multiple-unit combination use with pipe, carry out electrolysis as making the electrolytic solution high speed flow cross by the horizontal positioned producer.Also can obtain the effect of metallic cathode surface non flouling behaviour.
Description of drawings: Fig. 1 is the internal structure synoptic diagram of the B-B sectional view of the utility model Fig. 2 with the explanation producer, Fig. 2 is the synoptic diagram of the vertical view of Fig. 1 with the contour structures of explanation producer, and Fig. 3 is the layout synoptic diagram of the A-A sectional view of Fig. 1 with electrolytic solution pod apertures (14) on the explanation producer metal polar plate.Fig. 1 shown position is the producer horizontal positioned, (1) is the anode metal pole plate, (2) be plastic groove, (3) be the bipolarity metal polar plate, (4) be the cathodic metal pole plate, (5) be plastic cover plate, (6) are inboard rubber gasket, and (7) are outside rubber gasket, (8) be bolt, (9) be nut, (10) are packing ring, and (11) are positioning element, (12) be the plastic insulation sleeve pipe, (13) the plate inboard groove of locating at fluid guidance port (15) for plastic cover plate (5), (14) are the electrolytic solution pod apertures on each metal polar plate, and (15) advance or go out the fluid guidance port of producer for electrolytic solution, (16) be sun, perforate on the cathodic metal pole plate electrolyzer overhanging end, for simplifying, the bolt at a place only draws, nut and packing ring, and all the other are represented with medullary ray, dotted line on Fig. 2 has been represented the length of groove (13) and wide synoptic diagram, because the restriction of breadth, clear for drawing, the centre has adopted rupture line not destroy the integrity of producer.
Embodiment: see accompanying drawing 1 to Fig. 3, producer is a horizontal positioned, the inboard section form of a plastic groove (2) is a convex, on it, following two grooves be used for two of setting-ins above it cated do anodic and below it (back side) as the bipolarity metal electrode board (3) of negative electrode, perforate is arranged in order to wear plastic insulation sleeve pipe (11) and to wear bolt (8) and use (2), on the part (2), an inboard rubber gasket (6) is respectively arranged below, perforate is arranged in order to wear the plastic insulation sleeve pipe (6), bolt and put retaining ring (L) and use, it below the part below (6) one cated one anode metal pole plate (1) that faces up, it above superincumbent (6) a cathodic metal pole plate (4), part (1), perforate (16) is arranged (4), (14), part (12) reaches the hole of using of (8), following and the part (4) of part (1) top respectively has an outside rubber gasket (7), (7) be useful on the hole of part (12) and part (8) on, the outside in (7) respectively has a plastic cover plate (5) up and down, (5) flow-guiding mouth (15) that has electrolytic solution to advance or go out on is in fluid guidance port place part (5) inboard fluted (13), (5) also be useful on the hole of part (12) and part (8) on.Retaining ring is as positioning element (11), it is placed in the hole of bolt of part (6) to guarantee that when the fitting nut polar plate spacing is from being certain value behind the rubber gasket compressive deformation, part (12) is the plastic insulation sleeve pipe, penetrate 30 stainless steel bolts after all each parts install in certain sequence, put packing ring (10), fastening nut (9) has promptly constituted airtight multi-layer plate-type diaphragm-free electrolysis producer.See Fig. 1 and Fig. 3, (1) right-hand member on have delegation totally 5 pod apertures (14) near the left end of the top bipolarity metal polar plate (3) of (1) delegation's totally 5 pod apertures (14) and delegation's totally 5 pod apertures (14) are arranged near the right-hand member of that bipolarity metal polar plate (3) of cathodic metal battery lead plate (4) are arranged, the left end of (4) has delegation's totally 5 pod apertures (14).Fluid guidance port (15) should be in the pod apertures (14) on part (1) and the part (4) at corresponding same end separately.To form electrolytic solution like this and between metal polar plate, turn back and flow through, thereby the electrolysis area increases, significant part space availability ratio height.Do not increase under the situation of Faradaic current value and improved the clorox productive rate.
Anode metal pole plate upper surface has coating, two bipolarity metal electrode board upper surfaces also have coating, this (1) two part of exemplar (3), part (4) are formed three pairs of positive negative electrodes altogether, when (1) and (4) connects direct supply, when flowing through the gap of metal anode and negative plate as the lower concentration salt solution of electrolytic solution, under (+) that direct supply provides, (-) electric field action, the effect that when voltage increases to certain value, just produces electrolysis, formulation is expressed as follows:
F: faraday constant e: electronics
The working process significant parameter:
Clorox productive rate: 150 grams/1 hour
Current efficiency: η=69%
Faradaic current: 60 amperes
Total groove is pressed: 13 volts
Consumption:4.7 kilowatt of time/1 kilogram of Direct current clorox
Salt consumption: 6 kilograms/1 kilogram clorox.
Coated material is a titanium iridium ruthenium cobalt, and the metal polar plate material is an industrially pure titanium.
Claims (4)
1, a kind of belong to the sanitation equipment field (mainly comprise instrument by electric control unit, switch, lead) and electrolysis cells (mainly comprise electrolyzer, electrode, sealing member, positioning element, fastening piece) the airtight multi-layer plate-type diaphragm-free electrolysis producer of Zu Chenging, it is characterized in that having the structure of a novel electrolysis cells, it is by having fluid guidance port [15] on it and wearing plastic insulation sleeve pipe [12] and wear the two piece outside plastic cover plates [5] of bolt with the hole, two outside rubber gaskets [7], inboard [6] cathodic metal plates of rubber gasket [4], its working face one side (upper surface) goes up cated anode metal plate [1], plastic groove [2], there is coating can do anode on a side (upper surface) on its plate and its opposite side (lower surface) face can be done the bipolarity metal sheet [3] of negative electrode, be used for determining the positioning element [11] of distance between metal sheet, plastic insulation sleeve pipe [12], bolt [8], nut [9] and packing ring [10] are formed, electrolytic solution pod apertures [14] is arranged on the electrode metal plate, plastic insulation sleeve pipe and bolt are with hole and electrolyzer apertura lateralis [16], electrolytic solution pod apertures [14] is also arranged on the bipolarity metal sheet, for two adjacent metal sheets, hole [a 14] end disposed thereon on metal sheet, and the hole [14] on another piece metal sheet should the other end disposed thereon.(be on the two boards hole [14] not at same end)
2, electrolysis generator as claimed in claim 1 is characterized in that the bipolarity metal sheet can parallel placement several, but is at least one.
3, electrolysis generator as claimed in claim 1 is characterized in that inboard fluted (13) of the plate that the fluid guidance port (15) on plastic cover plate (5) is located.
4, electrolysis generator as claimed in claim 1 is characterized in that can connecting to form the multiple-unit electrolysis generator to the fluid guidance port of several electrolysis cells (15) with flexible pipe or hard tube as required.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 91202408 CN2097839U (en) | 1991-03-13 | 1991-03-13 | Seal multi-layer plate type no-diaphragm electrolysis generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 91202408 CN2097839U (en) | 1991-03-13 | 1991-03-13 | Seal multi-layer plate type no-diaphragm electrolysis generator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2097839U true CN2097839U (en) | 1992-03-04 |
Family
ID=4912958
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 91202408 Expired - Lifetime CN2097839U (en) | 1991-03-13 | 1991-03-13 | Seal multi-layer plate type no-diaphragm electrolysis generator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2097839U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1699669B (en) * | 2004-05-18 | 2010-09-22 | 海尔集团公司 | Washing machine having a water electrolysis unit and washing method thereof |
| CN101450824B (en) * | 2007-12-07 | 2012-07-18 | 鲁道夫·安东尼奥·M·戈麦斯 | Water electrolysis and activation |
| CN105332001A (en) * | 2015-11-24 | 2016-02-17 | 成都百鸥飞达生物科技有限公司 | Semi-membrane sodium hypochlorite generator |
| CN107416962A (en) * | 2017-07-12 | 2017-12-01 | 连云港亿尚景水务有限公司 | A kind of advanced oxidation equipment and sewage disposal system |
| CN109851001A (en) * | 2019-01-16 | 2019-06-07 | 韦志锋 | A kind of centering type rotating electrode of electrolytic sewage slot |
| CN110484928A (en) * | 2019-09-05 | 2019-11-22 | 青岛双瑞海洋环境工程股份有限公司 | A kind of vertical sodium hypochlorite electrolytic cell |
-
1991
- 1991-03-13 CN CN 91202408 patent/CN2097839U/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1699669B (en) * | 2004-05-18 | 2010-09-22 | 海尔集团公司 | Washing machine having a water electrolysis unit and washing method thereof |
| CN101450824B (en) * | 2007-12-07 | 2012-07-18 | 鲁道夫·安东尼奥·M·戈麦斯 | Water electrolysis and activation |
| CN105332001A (en) * | 2015-11-24 | 2016-02-17 | 成都百鸥飞达生物科技有限公司 | Semi-membrane sodium hypochlorite generator |
| CN105332001B (en) * | 2015-11-24 | 2017-10-27 | 成都百鸥飞达生物科技有限公司 | Half barrier film hypochlorite generator |
| CN107416962A (en) * | 2017-07-12 | 2017-12-01 | 连云港亿尚景水务有限公司 | A kind of advanced oxidation equipment and sewage disposal system |
| CN109851001A (en) * | 2019-01-16 | 2019-06-07 | 韦志锋 | A kind of centering type rotating electrode of electrolytic sewage slot |
| CN110484928A (en) * | 2019-09-05 | 2019-11-22 | 青岛双瑞海洋环境工程股份有限公司 | A kind of vertical sodium hypochlorite electrolytic cell |
| CN110484928B (en) * | 2019-09-05 | 2020-11-20 | 青岛双瑞海洋环境工程股份有限公司 | Vertical sodium hypochlorite electrolytic cell |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CX01 | Expiry of patent term |