US1798575A - Electrolytic cell - Google Patents
Electrolytic cell Download PDFInfo
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- US1798575A US1798575A US120421A US12042126A US1798575A US 1798575 A US1798575 A US 1798575A US 120421 A US120421 A US 120421A US 12042126 A US12042126 A US 12042126A US 1798575 A US1798575 A US 1798575A
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- cathode
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/17—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
- C25B9/19—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms
Definitions
- This invention relates to electrolytic cells, more particularly to the so-called non-submerged cathode and diaphragm type such as are used for the decomposition of brine in the formation of caustic soda.
- One of the objects of this invention is to increase the eiciency and capacity of the cell. By increasing the capacity, less ioor space is required for the same output, thus decreas- 1o ing the cost oconstruction of the building for housing the cells and of the cell equipment for a given capacity.
- the increase in eiciency and output capacity of the cell is produced to a large extent by so forming the cell that an increased proportion of total anode area is rendered eii'ective, and by so forming the anode that flow of current is facilitated.
- the cathode formed as abox of foraminous metal such as iron, is so shaped as to present afplaitedsurface between adjacent stretches o which the anodes are positioned.
- each anode has positioned portions of the cathode closely adjacentthereto Von opposite sides so that both sides of the anode are active, and the plaiting of the cathode permits a larger active proportion of total anode area to be used for each cell.
- v To increase the effectiveness of the anodes to a further extent, they are so formed as to present a considerably increased length of edge portions.
- F11gure 1 1s a somewhat diagrammatic view part y in side elevation and partly in vertical section through a cell embodying this invention.
- Figure2 isatop plan view.
- Figure 3 is a transverse vertical section on line 3-3 of Figure 1.
- Fi re 4 is a diagrammatic view illustratt e manner of cutting a pair of anodes.
- gure 5 is a perspective of the cathode baske
- a F Figure 6 is a detail section on line 6 6 of eferring to these drawings, at 1- is opposite sides 12 and a reentrant loo shown more particularly in Fi dicated a tank of suitable construction suchas iron and having an "inturned marginal flange 2 on its upper edge on which is supported the freeboard section 3.
- This freeboard section is preferably formed of concrete and is clamped to the tank by any suitable means, such, for example, as the tie bolts 4, having looped lower extremities engaging about hooks 5 extending from the outer face of the tank and having their upper ends threaded and extended through bars 6' resting on the upper face of the freeboard section, nuts 7' being shown as threaded on the upper ends of the tie bolts above the bars.
- any suitable means such as the tie bolts 4, having looped lower extremities engaging about hooks 5 extending from the outer face of the tank and having their upper ends threaded and extended through bars 6' resting on the upper face of the freeboard section, nuts 7' being shown as threaded on the upper ends of the tie bolts above the bars.
- the out-turned v flanges 8 ofthe cathode Interposed between the tank and the freeboard section at the joint are the out-turned v flanges 8 ofthe cathode which are overlaid by the upper ⁇ ends of a porous diaphragm 9 of asbestos paper or like material', the flange 8 and the dia hra being so clamped between the free oar section and the tank as to produce a liquid and gas tight joint therebetween.
- the cathode 10 comprises a foraminous plate 11 bent into vertically plaited form having portion 13. Bridging the edges of the p ate 11 are end lates 14, which are fixed to the edges of the p ate 11, as by spot welding at intervals so as to produce a general box shaped foraminous tank having two compartments 15 separated from each other by the upwardly looped portion 13 formed by the plaiting of the sheet.
- each of these' cclmpartmentls is lirpd vvithlalnl abeltos diap ragm over ying-t ep ate an t eu r edges of the diaphra beingmclampetbatween the cathode an the free ard sections as previously described.
- the sides, ends and bottom are each electrically active.
- each of the compartments 1 5,- which contain electrolyte are s nded anodes 20, there being two series o anodes as s 1 .and 91s 3.
- Each of the anodes comprises a lower substantially rectangular portion 21 having vintegrally therewith andl eccentricall or otherwise disposed relative thereto a le member 22- which extends through the free- 10o tor.
- cover 19 which may if desired be formed of concrete similar to the side and end walls of the freeboard section.
- the leads 22 eccentric to the longitudinal axis of portion 21 By forming the leads 22 eccentric to the longitudinal axis of portion 21 the'anodes can be cut from .plates of graphite or other suitable material in a manner shown in Figure 4, the plates being of combined widths no greater than the width of the ⁇ portions 21 and 22. By this means there is little waste in cutting the anodes from the material.
- the upper edge of the rectangular portion 21 is positioned slightly below the joint between the tank and freeboard section in order that during the normal operation of the cell the level of the electrolyte is above it. This permits circulation of the electrolyte beneath the lower edge of each anode and over the upper edge adjacent to the lead member 22.
- anodes extending into the two compartments 15 are fixed together in suitably spaced relation by spacing elements 25, each having reduced extremities extending into perforations in the lead members as at 26 and a central enlarged portion 27 which acts to space the anodes apart.
- the anodes are supported from opposite side walls of the freeboard section by means of pins 28 extending through each anode of each opposed pair and resting in suitable recesses 29 in the inner face of the freeboard wall 3.
- pins 28 extending through each anode of each opposed pair and resting in suitable recesses 29 in the inner face of the freeboard wall 3.
- These anode lead portions extend through the openings 23 of the cover and are connected to a bus bar 30 extending'along the top of the cell as by means of the conductors 24.
- pins 28 pass eccentrically through the anode lead portions, this being for the purpose of permitting a proper balance of the anodes so that they tend to take a substantially vertical position, the pins 28 passing through the anodes substantially above their gravity axes when they are vertical.
- an edge or a point facilitates the discharge of current from a conduc-
- the edges 37 defined by the kerfs 35 are subject to active current emission and gradually become wasted away so that the portions 36 take a general oval form as shown in the dotted ⁇ lines at 38 in Figure 6. These oval portions however are still more eliicient in permitting the discharge of current than a flat plate would be.
- a gas escape and at 41 is shown a supply pipe through which brine may be passes
- the central compartment formed Within the looped portion 15 and the side compartments between the compartments 15 and the tank- 1 are free from electrolyte, but receive the eiiluent from the anode compartments and the gas liberated at the cathode.
- the eiiluent may be led off from the cell after passing throu h the A diaphragm and the cathode throug the pipe 42..
- the top of the central compartment formed between the sides of the central plait and looped portion 13 and covered by the diaphragm should be below the out-turned cathode flanges 8, as shown in Figure 3, so that the hydrogen accumulating in the central compartment may flow freely through the foraminous end walls thereof and be taken olfv from the cell outwardly of the cathode.
- the cathode compartment in which the hydrogen accumulates has its highest part along the exterior wa-ll in direct communication with the exit (not shown) always provided at the top of the tank just below the cathode flanges in cells of the freeboard type.
- the increased hydrostatic head over the top of the middle cathode compartment also aids to prevent the escape of hydrogen into the freeboard section.
- the cathode is plaited to, provide a pair of compartments 15 which areV they might be positioned laterally rather than longitudinally of the cell.
- Current connections may be made to the cathode by any suitable means, but as shown in Figure 5 a portion of one of the flanges 8, has been extended as at 43, its outer end being upwardly turned as at 44 and fixedV to the bus bar 45.
- a cathode comprising a foraminous sheet formed vertically in plaits and having end flanges resting on the walls of said tank, plates of foraminous material bridging the ends of said plaits and.iixed thereto, a free'- board section supported on said tank, and rows of anodes supported by said freeboard section and depending between the plaits of said sheet, said plaits forming a chamber between said anodes open at its bottom.
- a cathode comprising a box having electrically active foraminous sides, ends, and bottom, said sides and ends forming a substantially rectangular frame, andI said bottom being plaited to form with said sides and ends a plurality of compartments open alternately at top and bottom, the edges ofsaid bottoni between said sides being fixed to the inner.
- a cathode comprising a box having electrically active foraminous sides, ends, and bottom, each of said ends being rectangular and said sides and bottom being formed of a single sheet plaited to form with said ends a plurality of compartments open alternately at top and bottom, theedges of said sheet .engaging and being fixed to the inner faces of said ends, and an anode between adjacent faces of each plait in each of said compartments open at its top, said anodes being in operative relation to said sides, ends and cathode bottom.
- a cathode comprising electrically active foraminous sides, ends and a bottom, said bottom' being plaited and having its edges secured to the inner faces of said ends and forming with said ends and sides a plurality .of cornpartments open alternately at top and bottoni.
- a cathode comprising "a box having electrically active fo'raminous sides", ends and bottom, said bottom being plaited to forni with said sides and ends aj pair of side compartments having open tops and a central compartment having a closed top, said central compartment being open through said ends for the free passage of gaseous products of electrolysis.
- a cathode comprising abox having electrically active foraminous sides, ends and bottom, said bottom being plaited to form with said sides and ends avpair of side compartments having open tops and a'central compartment having a closed top, said central compartment having ⁇ perforations distributed over substantially'its entire end areas for the free passage of gaseous products of electrolysis.
- a device of the class described comprising a container,a cathode suspended in said container and comprising two spaced apart parallel electrolyte containing chambers, a diaphragm lining each chamber, the four sides and bottom of each chamber being active, a chamber free'from electrolyte located between the electrolyte chambers, and anodes extending into said electrolyte chambers, said 'chamber free from electrolyte having end openings for the free escape ofvgaseous products of electrolysis therefrom.
- An electrolytic cell comprising a container, a ⁇ cathode suspended therein, said cathode comprising two spaced apart elec'- trolyte-containing chambers, anodes in said electrolyte-containing chambers, said la'st mentioned chambers being closed at their tops, the top end of said chamber between said electrolyte-containing chambers bein below the tops of said outwardly positione chainbers, and said chambers free from electrolyte being in free communication with each other for the passagev of roducts of'electrolysis.
- a cathode comprisng a box having electrically active foraminous sides, ends and bottom, said sides and ends forming a substantially rectangular frame, said bottom being plaited to form with said sides and ends a pair of anode compartments for the reception of electrolyte spaced by a compartment free from electrol te, said bottom being fixed to said end wa ls which provide free exit from said spacing compartment through the openings in said end walls for the products of eleciao ⁇ ..tiYee-:foraminous si'des, ends and bottom,
- said sides and ends forming a substantially rectangular frame, said bottom being plaited to form with said sides and ends a pair of 5 anode compartment-s for the reception of electrolyte spaced by a compartment free from electrolyte, said bottom being xed to said end walls Which'provide free exit from said spacing compartment through the openings in said end Walls for the products of'electrolysis entering said spacing compartment, and a diaphragm lining said anode-compartment-s, and extending over said spacing compartment, said spacing compartment having an open bottom and its top being below the top of said cathode.
Description
ELECTROLYTIC CELL Filed July 5, 1926 ,mw-m U /mw Patented Mar. 31, 1931 UNITED STATES PATENT ori-ICE y HERBERT I. ALLEN .AND :DOUGLAS B. AYERST, OF PORTLAAND, MAINE, ASSIGNOBS TO ELECTRON CHEMICAL CQMPANY, F PORTLAND, MAINE, A CORPVORATION' 0F ELEoTRoLYTIo CELL Application led July 3, 1926. Serial No. 120,421.
This invention relates to electrolytic cells, more particularly to the so-called non-submerged cathode and diaphragm type such as are used for the decomposition of brine in the formation of caustic soda. I
One of the objects of this invention is to increase the eiciency and capacity of the cell. By increasing the capacity, less ioor space is required for the same output, thus decreas- 1o ing the cost oconstruction of the building for housing the cells and of the cell equipment for a given capacity.
The increase in eiciency and output capacity of the cell is produced to a large extent by so forming the cell that an increased proportion of total anode area is rendered eii'ective, and by so forming the anode that flow of current is facilitated.
To provide increased active-anode area,
the cathode, formed as abox of foraminous metal such as iron, is so shaped as to present afplaitedsurface between adjacent stretches o which the anodes are positioned. Thus each anode has positioned portions of the cathode closely adjacentthereto Von opposite sides so that both sides of the anode are active, and the plaiting of the cathode permits a larger active proportion of total anode area to be used for each cell. v To increase the effectiveness of the anodes to a further extent, they are so formed as to present a considerably increased length of edge portions.
For a more complete understanding of this invention, reference may be had to the accompanying drawings in which F11gure 1 1s a somewhat diagrammatic view part y in side elevation and partly in vertical section through a cell embodying this invention. f Figure2isatop plan view. Figure 3 is a transverse vertical section on line 3-3 of Figure 1. Fi re 4 is a diagrammatic view illustratt e manner of cutting a pair of anodes. gure 5 is a perspective of the cathode baske A F Figure 6 is a detail section on line 6 6 of eferring to these drawings, at 1- is opposite sides 12 and a reentrant loo shown more particularly in Fi dicated a tank of suitable construction suchas iron and having an "inturned marginal flange 2 on its upper edge on which is supported the freeboard section 3. This freeboard section is preferably formed of concrete and is clamped to the tank by any suitable means, such, for example, as the tie bolts 4, having looped lower extremities engaging about hooks 5 extending from the outer face of the tank and having their upper ends threaded and extended through bars 6' resting on the upper face of the freeboard section, nuts 7' being shown as threaded on the upper ends of the tie bolts above the bars.
Interposed between the tank and the freeboard section at the joint are the out-turned v flanges 8 ofthe cathode which are overlaid by the upper `ends of a porous diaphragm 9 of asbestos paper or like material', the flange 8 and the dia hra being so clamped between the free oar section and the tank as to produce a liquid and gas tight joint therebetween.
As shown more particularly in Figure 5, the cathode 10 comprises a foraminous plate 11 bent into vertically plaited form having portion 13. Bridging the edges of the p ate 11 are end lates 14, which are fixed to the edges of the p ate 11, as by spot welding at intervals so as to produce a general box shaped foraminous tank having two compartments 15 separated from each other by the upwardly looped portion 13 formed by the plaiting of the sheet. The interior of each of these' cclmpartmentls is lirpd vvithlalnl abeltos diap ragm over ying-t ep ate an t eu r edges of the diaphra beingmclampetbatween the cathode an the free ard sections as previously described. The sides, ends and bottom are each electrically active. v
Within each of the compartments 1 5,- which contain electrolyte, are s nded anodes 20, there being two series o anodes as s 1 .and 91s 3. Each of the anodes comprises a lower substantially rectangular portion 21 having vintegrally therewith andl eccentricall or otherwise disposed relative thereto a le member 22- which extends through the free- 10o tor.
board section and through openings 23 suitably spaced through the cover 19 which may if desired be formed of concrete similar to the side and end walls of the freeboard section.-
By forming the leads 22 eccentric to the longitudinal axis of portion 21 the'anodes can be cut from .plates of graphite or other suitable material in a manner shown in Figure 4, the plates being of combined widths no greater than the width of the` portions 21 and 22. By this means there is little waste in cutting the anodes from the material.' The upper edge of the rectangular portion 21 is positioned slightly below the joint between the tank and freeboard section in order that during the normal operation of the cell the level of the electrolyte is above it. This permits circulation of the electrolyte beneath the lower edge of each anode and over the upper edge adjacent to the lead member 22. As shown, oppositely positioned anodes extending into the two compartments 15 are fixed together in suitably spaced relation by spacing elements 25, each having reduced extremities extending into perforations in the lead members as at 26 and a central enlarged portion 27 which acts to space the anodes apart. The anodes are supported from opposite side walls of the freeboard section by means of pins 28 extending through each anode of each opposed pair and resting in suitable recesses 29 in the inner face of the freeboard wall 3. These anode lead portions extend through the openings 23 of the cover and are connected to a bus bar 30 extending'along the top of the cell as by means of the conductors 24. It will be noted that the pins 28 pass eccentrically through the anode lead portions, this being for the purpose of permitting a proper balance of the anodes so that they tend to take a substantially vertical position, the pins 28 passing through the anodes substantially above their gravity axes when they are vertical.
To further facilitate the passage of current from the anodes they are preferably formed to present a multiplicity of corners, it being well known that an edge or a point facilitates the discharge of current from a conduc- For this purpose the body portions 21 of the anodes-are shown as cut upwardly as by means of a saw to form a series of closely spaced kerfs 35 to divide the major portion of the active anode into a series of relatively narrow bars 36 as shown more particularly in Figure 6. In operation the edges 37 defined by the kerfs 35 are subject to active current emission and gradually become wasted away so that the portions 36 take a general oval form as shown in the dotted` lines at 38 in Figure 6. These oval portions however are still more eliicient in permitting the discharge of current than a flat plate would be. While anodes might be made in small slabs to obtain an extensive edge len h, this would require fabrication and woul be more expensive than formin kerfs in anodes of substantial size. At 40 1s shown a gas escape and at 41 is shown a supply pipe through which brine may be passe The central compartment formed Within the looped portion 15 and the side compartments between the compartments 15 and the tank- 1 are free from electrolyte, but receive the eiiluent from the anode compartments and the gas liberated at the cathode. The eiiluent may be led off from the cell after passing throu h the A diaphragm and the cathode throug the pipe 42..
Particularly when this cell is used for electrolysis of brine to form caustic soda, hydrogen and chlorine, the top of the central compartment formed between the sides of the central plait and looped portion 13 and covered by the diaphragm should be below the out-turned cathode flanges 8, as shown in Figure 3, so that the hydrogen accumulating in the central compartment may flow freely through the foraminous end walls thereof and be taken olfv from the cell outwardly of the cathode. Thus the cathode compartment in which the hydrogen accumulates has its highest part along the exterior wa-ll in direct communication with the exit (not shown) always provided at the top of the tank just below the cathode flanges in cells of the freeboard type. Hydrogen being a very light, tenuous gas, is diiicult to confine and handle and if, -for example, the top of the central cathode compartment formed by the plating of the cathode were higher than the side compartments, hydrogen would tend to accumulate from the outer compartment in this inner compartment and exert an upward pressure, which would result in hydrogen passing through the diaphragm and through the superimposed electrolyte into the anode chamber where it might mix in explosive proportions with the chlorine. The increased hydrostatic head over the top of the middle cathode compartment also aids to prevent the escape of hydrogen into the freeboard section. Moreover, it is exceedingly important inasmuch as substantially-half of the hydrogen producedby the cell is collected in this central compartment that there be absolutely free communication between this central cathode compartment and the two outer c athode compartments to prevent the trapping of hydrogen. It is also important that the central compartment between the anode compartments be open at its lower end or bottom so as to permit free escape therefrom of the eiiiuent from the anode compartments. 'lhis prevents the return of the effluent to the anode compartments which would contaminate the electrolyte and cause side reactions with resultant loss in cell eiiiciency, im-
d mto the cell.
purity of reaction products, and shortened life of the anodes.
Whi-le as shown the cathode is plaited to, provide a pair of compartments 15 which areV they might be positioned laterally rather than longitudinally of the cell. Current connections may be made to the cathode by any suitable means, but as shown in Figure 5 a portion of one of the flanges 8, has been extended as at 43, its outer end being upwardly turned as at 44 and fixedV to the bus bar 45.
An embodiment of this invention having thus been described, it should be evident to those skilled in the art that many other changes and modifications might be lmade therein without departing from the spirit or scope ofthe invention as defined by the appended claims.
We claim:
1./An electrolytic cell comprising a tank, a cathode comprising a foraminous sheet formed vertically in plaits and having end flanges resting on the walls of said tank, plates of foraminous material bridging the ends of said plaits and.iixed thereto, a free'- board section supported on said tank, and rows of anodes supported by said freeboard section and depending between the plaits of said sheet, said plaits forming a chamber between said anodes open at its bottom.
2. In a divice of the class described, a cathode comprising a box having electrically active foraminous sides, ends, and bottom, said sides and ends forming a substantially rectangular frame, andI said bottom being plaited to form with said sides and ends a plurality of compartments open alternately at top and bottom, the edges ofsaid bottoni between said sides being fixed to the inner.
faces of said ends.
3. In a device of the class described, a cathode comprising a box having electrically active foraminous sides, ends, and bottom, each of said ends being rectangular and said sides and bottom being formed of a single sheet plaited to form with said ends a plurality of compartments open alternately at top and bottom, theedges of said sheet .engaging and being fixed to the inner faces of said ends, and an anode between adjacent faces of each plait in each of said compartments open at its top, said anodes being in operative relation to said sides, ends and cathode bottom.
4. In a device ofthe class described, a cathode .comprising electrically active foraminous sides, ends and a bottom, said bottom' being plaited and having its edges secured to the inner faces of said ends and forming with said ends and sides a plurality .of cornpartments open alternately at top and bottoni.
5. In a device of the class described, a cathode comprising "a box having electrically active fo'raminous sides", ends and bottom, said bottom being plaited to forni with said sides and ends aj pair of side compartments having open tops and a central compartment having a closed top, said central compartment being open through said ends for the free passage of gaseous products of electrolysis.
6. In a de vicey ofthe Vclass described, a cathode comprising abox having electrically active foraminous sides, ends and bottom, said bottom being plaited to form with said sides and ends avpair of side compartments having open tops and a'central compartment having a closed top, said central compartment having `perforations distributed over substantially'its entire end areas for the free passage of gaseous products of electrolysis.
7. A device of the class described comprising a container,a cathode suspended in said container and comprising two spaced apart parallel electrolyte containing chambers, a diaphragm lining each chamber, the four sides and bottom of each chamber being active, a chamber free'from electrolyte located between the electrolyte chambers, and anodes extending into said electrolyte chambers, said 'chamber free from electrolyte having end openings for the free escape ofvgaseous products of electrolysis therefrom.
' 8. An electrolytic cell comprising a container, a` cathode suspended therein, said cathode comprising two spaced apart elec'- trolyte-containing chambers, anodes in said electrolyte-containing chambers, said la'st mentioned chambers being closed at their tops, the top end of said chamber between said electrolyte-containing chambers bein below the tops of said outwardly positione chainbers, and said chambers free from electrolyte being in free communication with each other for the passagev of roducts of'electrolysis.
9.`In a device '0F the class described, a cathode comprisng a box having electrically active foraminous sides, ends and bottom, said sides and ends forming a substantially rectangular frame, said bottom being plaited to form with said sides and ends a pair of anode compartments for the reception of electrolyte spaced by a compartment free from electrol te, said bottom being fixed to said end wa ls which provide free exit from said spacing compartment through the openings in said end walls for the products of eleciao ` ..tiYee-:foraminous si'des, ends and bottom,
said sides and ends forming a substantially rectangular frame, said bottom being plaited to form with said sides and ends a pair of 5 anode compartment-s for the reception of electrolyte spaced by a compartment free from electrolyte, said bottom being xed to said end walls Which'provide free exit from said spacing compartment through the openings in said end Walls for the products of'electrolysis entering said spacing compartment, and a diaphragm lining said anode-compartment-s, and extending over said spacing compartment, said spacing compartment having an open bottom and its top being below the top of said cathode. Y
In testimony whereof we have aiiixed ou signatures.
HERBERT I. ALLEN. DOUGLAS B. AYERST.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BE343061D BE343061A (en) | 1926-07-03 | ||
US120421A US1798575A (en) | 1926-07-03 | 1926-07-03 | Electrolytic cell |
GB14429/27A GB273672A (en) | 1926-07-03 | 1927-05-28 | Improvements in or relating to electrolytic cells |
FR635492D FR635492A (en) | 1926-07-03 | 1927-06-03 | Improvements to electrolytic tanks |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US120421A US1798575A (en) | 1926-07-03 | 1926-07-03 | Electrolytic cell |
Publications (1)
Publication Number | Publication Date |
---|---|
US1798575A true US1798575A (en) | 1931-03-31 |
Family
ID=22390164
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US120421A Expired - Lifetime US1798575A (en) | 1926-07-03 | 1926-07-03 | Electrolytic cell |
Country Status (4)
Country | Link |
---|---|
US (1) | US1798575A (en) |
BE (1) | BE343061A (en) |
FR (1) | FR635492A (en) |
GB (1) | GB273672A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3116227A (en) * | 1960-10-04 | 1963-12-31 | Gulf Oil Corp | Electrolytic cell |
US3116228A (en) * | 1960-05-09 | 1963-12-31 | Pittsburgh Plate Glass Co | Diaphragm type electrolyticcell |
-
0
- BE BE343061D patent/BE343061A/xx unknown
-
1926
- 1926-07-03 US US120421A patent/US1798575A/en not_active Expired - Lifetime
-
1927
- 1927-05-28 GB GB14429/27A patent/GB273672A/en not_active Expired
- 1927-06-03 FR FR635492D patent/FR635492A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3116228A (en) * | 1960-05-09 | 1963-12-31 | Pittsburgh Plate Glass Co | Diaphragm type electrolyticcell |
US3116227A (en) * | 1960-10-04 | 1963-12-31 | Gulf Oil Corp | Electrolytic cell |
Also Published As
Publication number | Publication date |
---|---|
FR635492A (en) | 1928-03-16 |
GB273672A (en) | 1928-08-28 |
BE343061A (en) |
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