US2683116A - Method for starting multicellular pressure electrolyzers - Google Patents
Method for starting multicellular pressure electrolyzers Download PDFInfo
- Publication number
- US2683116A US2683116A US198220A US19822050A US2683116A US 2683116 A US2683116 A US 2683116A US 198220 A US198220 A US 198220A US 19822050 A US19822050 A US 19822050A US 2683116 A US2683116 A US 2683116A
- Authority
- US
- United States
- Prior art keywords
- gas
- pressure
- starting
- spaces
- anode
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title claims description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 16
- 229910052757 nitrogen Inorganic materials 0.000 claims description 8
- 238000005868 electrolysis reaction Methods 0.000 claims description 4
- 239000007789 gas Substances 0.000 description 23
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 6
- 239000001257 hydrogen Substances 0.000 description 6
- 229910052739 hydrogen Inorganic materials 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 4
- 239000011261 inert gas Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 238000004880 explosion Methods 0.000 description 3
- 230000007935 neutral effect Effects 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 230000002000 scavenging effect Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000013016 damping Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000001066 destructive effect Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 230000014509 gene expression Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 230000001052 transient effect Effects 0.000 description 1
Classifications
-
- 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
- C25B15/00—Operating or servicing cells
Definitions
- My invention relates to a method of starting pressure-operated multicell electrolytic apparatus having aplurality of individual pressure-resistant cells each containing a diaphragm so as to form therein an anode chamber and a cathode chamber, and having two systems of gas channels, one for connecting the gas-spaces of said anode chambers to a first receptacle and'the other for connecting the gas-spaces ofsaid cathode chambers to a second receptacle.
- Structures of this type are well-known for use under normal atmospheric pressure and may be used for producing hydrogen and oxygen or hydrogen and chlorine or the like. The use of such structures under pressure has, until now, been very dangerous.
- inert or neutral are used herein in the customary sense, to designate a gas which does not produce a chemical reaction in the system. Nitrogen is given as an example of such a gas. It is inert or neutral in the sense that it does not produce an explosive mixture either with oxygen orwith hydrogen or with chlorme.
- the invention permits the starting of such electrolyzers without danger of destroying its diaphragms and without any danger of explosion.
- the method according to the invention is very simple and enables anyone skilled in the art, to start such structures rapidly and safely.
- the gas spaces of the electrolyzer are initially filled with an inert or neutral gas such as nitrogen at a gauge pressure of not less than 2 atmospheres (abs) and These conditions may the full valueof the intended final working pres- 7 sure.
- the apparatus can in such case be started with the correct final setting of all regulating and safety valves which previously had to be adon at the time when the full Working pressure is attained, it is not only permissible but in fact particularly advantageous to increase the current intensity immediately to the full working value, because irregularities in the starting operation will then be contained within the time interval during which the inert gas filling is predominantly present which suppresses the decisive danger factors by its detonation-damping effect.
- multicell pressure electrolyz-ers having a plurality of cells each con-t taining an individual diaphragm for subdividing its associated cell into an anode and a cathode chamber and having two gas collecting systems
- the method of starting the operation of such apparatus which consists of the following steps, namely, (1) filling all gas spaces of both of said collecting systems with nitrogen at an equal pressure of at least 10 atmospheres abs; and (2) thereafter switching on the current to commence electrolysis.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Description
Patented July 6, '1954 METHOD FOR STARTING MULTICELLULAR PRESSURE ELECTROLYZERS Ewald A. Zdansky, Monthey, Switzerland, as-
Signor to Lonza Elektrizitaetswerke und Chemische Fabriken Aktienges'ellschaft, Gampel (Wallis), Switzerland, a company of Switzerland No Drawing. Application November 29,- 1950,
' Serial No. 198,220
Claims priority, application Switzerland November 30, 1949 3 Claims.
1 My invention relates to a method of starting pressure-operated multicell electrolytic apparatus having aplurality of individual pressure-resistant cells each containing a diaphragm so as to form therein an anode chamber and a cathode chamber, and having two systems of gas channels, one for connecting the gas-spaces of said anode chambers to a first receptacle and'the other for connecting the gas-spaces ofsaid cathode chambers to a second receptacle. Structures of this type are well-known for use under normal atmospheric pressure and may be used for producing hydrogen and oxygen or hydrogen and chlorine or the like. The use of such structures under pressure has, until now, been very dangerous.
The starting of such apparatus requires particular care because when the gas evolution commences, considerable quantities of the produced hydrogen go into solution or are held occluded fact that, since the volume of the generated gas the current is connected only under such pressure. The first gas bubbles are in this manner generated under pressure and their volume remains small, thus avoiding the occurrence of destructive turbulence in the electrolyte. Furthermore, the proportional influence of the hydrogen volume initially trapped by the solution and by occlusion, on the total pressures in the individual gas spaces, is appreciably reduced and even the restricted, transient formation of a gas mixture is rendered innocuous, by the admixture of inert gas, thus suppressing the danger of explosion. All these effects are of course enhanced with increasing pressure of the introduced inert gas and it is therefore in practice advisable to apply a starting pressure of not less than 10 to 20 percent of the ultimate working pressure, amounting in accordance with indivdual structures to 10 to 50 atmospheres or more.
Expressions such as inert or neutral are used herein in the customary sense, to designate a gas which does not produce a chemical reaction in the system. Nitrogen is given as an example of such a gas. It is inert or neutral in the sense that it does not produce an explosive mixture either with oxygen orwith hydrogen or with chlorme.
It has been found even more advantageous to increase the pressure of the inert gas charge to decreases in such apparatus with increasing pressiderable turbulence is set up within the indi- -1i vidual cells endangering the diaphragms and causing pressure differences in the narrow gas and electrolyte passages. lead to the formation of a detonable oxy-hydrogen gas mixture.
The invention permits the starting of such electrolyzers without danger of destroying its diaphragms and without any danger of explosion. The method according to the invention is very simple and enables anyone skilled in the art, to start such structures rapidly and safely.
According to the invention the gas spaces of the electrolyzer are initially filled with an inert or neutral gas such as nitrogen at a gauge pressure of not less than 2 atmospheres (abs) and These conditions may the full valueof the intended final working pres- 7 sure. The apparatus can in such case be started with the correct final setting of all regulating and safety valves which previously had to be adon at the time when the full Working pressure is attained, it is not only permissible but in fact particularly advantageous to increase the current intensity immediately to the full working value, because irregularities in the starting operation will then be contained within the time interval during which the inert gas filling is predominantly present which suppresses the decisive danger factors by its detonation-damping effect.
It may be mentioned in conclusion that it has been suggested to scavenge electrolyzers with nitrogen before starting in order to expel atmospheric oxygen from the spaces provided for receiving the generated hydrogen. Such previously proposed scavenging is in practice inefiective for and does not in any way benefit the starting operation because the danger of explosion, which has been eliminated by the scavenging, immediately reappears during the starting due to the inevitable formation of an oxy-hydrogen gas mixture the formation of which cannot be prevented by the small partial pressure of the residual nitrogen remaining in the apparatus after the scavenging.
I claim:
1. In the operation of electrolytic apparatus having a plurality of pressure-re$istant cells each containing an individual diaphragm which subdivides its associated cell into an anode and a cathode chamber and having two gas collecting systems, one for the gas spaces of all anode chambers and the other for the gas spaces of all cathode chambers, the method of starting the operation of such apparatus which consists of the following steps, namely, (1) filling all gas spaces of both of said collecting systems with nitrogen at an equal pressure of at least two atmospheres abs; and (2) thereafter switching on the current to commence electrolysis.
.2. In the operation of multicell pressure electrolyz-ers having a plurality of cells each con-t taining an individual diaphragm for subdividing its associated cell into an anode and a cathode chamber and having two gas collecting systems,
one for the gas spaces of all anode chambers and the other for the gas spaces of all cathode chambers, the method of starting the operation of such apparatus which consists of the following steps, namely, (1) filling all gas spaces of both of said collecting systems with nitrogen at an equal pressure of at least 10 atmospheres abs; and (2) thereafter switching on the current to commence electrolysis.
3. In the operation of multicell pressure electrolyzers having a plurality of cells each containing an individual diaphragm forsubdividing its associated cell into an anode and a cathode chamber and. having two gas collecting systems, one for the gas spaces of all anode chambers and :the other for the :gas spaces of all cathode chambers, the method of starting the operation of such apparatus which consists of the following steps, namely, (1) filling all gas spaces of both of said collecting systems with nitrogen at a pressure of at least 10 atmospheres abs.; and (2) thereafter switching on the current required for electrolysis at a magnitude which corresponds to full working conditions.
References Cited in the file of this patent UNITED STATES PATENTS Number Name Date 1,581,944 Hausmeister Apr. 20, 1926 1,983,296 Lacher Dec. 4, 1934
Claims (1)
1. IN THE OPERATTION OF ELECTROLYTIC APPARATUS HAVING A PLURALITY OF PRESSURE-RESISTANT CELLS EACH CONTAINING AN INDIVIDUAL DIAPHRAGM WHICH SUBDIVIDES ITS ASSOCIATED CELL INTO AN ANODE AND A CATHODE CHAMBER AND HAVING TWO GAS COLLECTING SYSTEMS, ONE FOR THE GAS SPACES OF ALL ANODE CHAMBERS AND THE OTHER FOR THE GAS SPACES OF ALL CATHODE CHAMBERS, THE METHOD OF STARTING THE OPERATION OF SUCH APPARATUS WHICH CONSISTS OF THE FOLLOWING STEPS, NAMELY, (1) FILLING ALL GAS SPACES OF BOTH OF SAID COLLECTING SYSTEMS WITH NITROGEN AT AN EQUAL PRESSURE OF AT LEAST TWO ATMOSPHERES ABS.; AND (2) THEREAFTER SWITCHING ON THE CURRENT TO COMMENCE ELECTROLYSIS.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CH2683116X | 1949-11-30 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2683116A true US2683116A (en) | 1954-07-06 |
Family
ID=4571042
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US198220A Expired - Lifetime US2683116A (en) | 1949-11-30 | 1950-11-29 | Method for starting multicellular pressure electrolyzers |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US2683116A (en) |
| CH (1) | CH280175A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3188283A (en) * | 1961-01-03 | 1965-06-08 | Cons Electrodynamics Corp | Electrolytic process for removing moisture |
| US3291714A (en) * | 1961-01-13 | 1966-12-13 | Ici Australia Ltd | Electrodes |
| US20100012503A1 (en) * | 2008-07-15 | 2010-01-21 | Next Hydrogen Corporation | Electrolyser module |
| WO2012116994A1 (en) | 2011-02-28 | 2012-09-07 | Vito Nv | Novel separator, an electrochemical cell therewith and use thereof therein |
| US8864962B2 (en) | 2008-07-15 | 2014-10-21 | Next Hydrogen Corporation | Electrolyser module |
| US9133553B2 (en) | 2012-09-13 | 2015-09-15 | Next Hydrogen Corporation | Externally-reinforced water electrolyzer module |
| US9187833B2 (en) | 2012-09-13 | 2015-11-17 | Next Hydrogen Corporation | Internally-reinforced water electrolyser module |
| US11005117B2 (en) | 2019-02-01 | 2021-05-11 | Aquahydrex, Inc. | Electrochemical system with confined electrolyte |
| US11018345B2 (en) | 2013-07-31 | 2021-05-25 | Aquahydrex, Inc. | Method and electrochemical cell for managing electrochemical reactions |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1581944A (en) * | 1923-11-17 | 1926-04-20 | Hausmeister Paul | Production of compressed gases by electrolysis |
| US1983296A (en) * | 1931-08-28 | 1934-12-04 | Firm Lawaczeck Gmbh | Arrangement in multicell electrolyzers |
-
1949
- 1949-11-30 CH CH280175D patent/CH280175A/en unknown
-
1950
- 1950-11-29 US US198220A patent/US2683116A/en not_active Expired - Lifetime
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1581944A (en) * | 1923-11-17 | 1926-04-20 | Hausmeister Paul | Production of compressed gases by electrolysis |
| US1983296A (en) * | 1931-08-28 | 1934-12-04 | Firm Lawaczeck Gmbh | Arrangement in multicell electrolyzers |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3188283A (en) * | 1961-01-03 | 1965-06-08 | Cons Electrodynamics Corp | Electrolytic process for removing moisture |
| US3291714A (en) * | 1961-01-13 | 1966-12-13 | Ici Australia Ltd | Electrodes |
| US8864962B2 (en) | 2008-07-15 | 2014-10-21 | Next Hydrogen Corporation | Electrolyser module |
| US20100012503A1 (en) * | 2008-07-15 | 2010-01-21 | Next Hydrogen Corporation | Electrolyser module |
| US8308917B2 (en) * | 2008-07-15 | 2012-11-13 | Next Hydrogen Corporation | Electrolyser module |
| EP2300640A4 (en) * | 2008-07-15 | 2014-06-25 | Next Hydrogen Corp | ELECTROLYSIS MODULE |
| WO2012116994A1 (en) | 2011-02-28 | 2012-09-07 | Vito Nv | Novel separator, an electrochemical cell therewith and use thereof therein |
| US9133553B2 (en) | 2012-09-13 | 2015-09-15 | Next Hydrogen Corporation | Externally-reinforced water electrolyzer module |
| US9187833B2 (en) | 2012-09-13 | 2015-11-17 | Next Hydrogen Corporation | Internally-reinforced water electrolyser module |
| US11018345B2 (en) | 2013-07-31 | 2021-05-25 | Aquahydrex, Inc. | Method and electrochemical cell for managing electrochemical reactions |
| US11005117B2 (en) | 2019-02-01 | 2021-05-11 | Aquahydrex, Inc. | Electrochemical system with confined electrolyte |
| US11682783B2 (en) | 2019-02-01 | 2023-06-20 | Aquahydrex, Inc. | Electrochemical system with confined electrolyte |
| US12080928B2 (en) | 2019-02-01 | 2024-09-03 | Edac Labs, Inc. | Electrochemical system with confined electrolyte |
Also Published As
| Publication number | Publication date |
|---|---|
| CH280175A (en) | 1952-01-15 |
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