US2257746A - Electrolytic process of preparing arsenates - Google Patents
Electrolytic process of preparing arsenates Download PDFInfo
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- US2257746A US2257746A US246280A US24628038A US2257746A US 2257746 A US2257746 A US 2257746A US 246280 A US246280 A US 246280A US 24628038 A US24628038 A US 24628038A US 2257746 A US2257746 A US 2257746A
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- arsenate
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- 238000000034 method Methods 0.000 title description 23
- DJHGAFSJWGLOIV-UHFFFAOYSA-K Arsenate3- Chemical class [O-][As]([O-])([O-])=O DJHGAFSJWGLOIV-UHFFFAOYSA-K 0.000 title description 21
- AQLMHYSWFMLWBS-UHFFFAOYSA-N arsenite(1-) Chemical compound O[As](O)[O-] AQLMHYSWFMLWBS-UHFFFAOYSA-N 0.000 description 21
- 229940000489 arsenate Drugs 0.000 description 16
- 239000003792 electrolyte Substances 0.000 description 13
- 239000000463 material Substances 0.000 description 11
- MHUWZNTUIIFHAS-XPWSMXQVSA-N 9-octadecenoic acid 1-[(phosphonoxy)methyl]-1,2-ethanediyl ester Chemical compound CCCCCCCC\C=C\CCCCCCCC(=O)OCC(COP(O)(O)=O)OC(=O)CCCCCCC\C=C\CCCCCCCC MHUWZNTUIIFHAS-XPWSMXQVSA-N 0.000 description 8
- 230000001590 oxidative effect Effects 0.000 description 8
- 229940047047 sodium arsenate Drugs 0.000 description 8
- 239000003575 carbonaceous material Substances 0.000 description 7
- 239000011148 porous material Substances 0.000 description 7
- PTLRDCMBXHILCL-UHFFFAOYSA-M sodium arsenite Chemical compound [Na+].[O-][As]=O PTLRDCMBXHILCL-UHFFFAOYSA-M 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 6
- 230000028161 membrane depolarization Effects 0.000 description 5
- 230000035699 permeability Effects 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 239000011233 carbonaceous binding agent Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 229910052785 arsenic Inorganic materials 0.000 description 3
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 230000008030 elimination Effects 0.000 description 3
- 238000003379 elimination reaction Methods 0.000 description 3
- 229910002804 graphite Inorganic materials 0.000 description 3
- 239000010439 graphite Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- GOLCXWYRSKYTSP-UHFFFAOYSA-N Arsenious Acid Chemical compound O1[As]2O[As]1O2 GOLCXWYRSKYTSP-UHFFFAOYSA-N 0.000 description 2
- 229960002594 arsenic trioxide Drugs 0.000 description 2
- GCPXMJHSNVMWNM-UHFFFAOYSA-N arsenous acid Chemical class O[As](O)O GCPXMJHSNVMWNM-UHFFFAOYSA-N 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000002999 depolarising effect Effects 0.000 description 2
- 239000007772 electrode material Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 239000010405 anode material Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- LULLIKNODDLMDQ-UHFFFAOYSA-N arsenic(3+) Chemical compound [As+3] LULLIKNODDLMDQ-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 230000003134 recirculating effect Effects 0.000 description 1
- 230000002940 repellent Effects 0.000 description 1
- 239000005871 repellent Substances 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- CDBAKLRDFBGJOX-UHFFFAOYSA-K sodium arsenate Chemical compound [Na+].[Na+].[Na+].[O-][As]([O-])([O-])=O CDBAKLRDFBGJOX-UHFFFAOYSA-K 0.000 description 1
- 229960004793 sucrose Drugs 0.000 description 1
- -1 when Substances 0.000 description 1
Images
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
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
Definitions
- This invention relates to an electrolytic process in which an impressed electric current is passed through a cell having insoluble electrodes immersed in an aqueous electrolyte. More specifl cally, the invention is a process for electrolytically oxidizing a water soluble arsenite, such as sodium or other alkaline metal arsenite, to the corresponding arsenate.
- a water soluble arsenite such as sodium or other alkaline metal arsenite
- a further object is to lower the operating voltage in such a process.
- Another object is to make possible the elimination of diaphragms in the .process.
- Still another object is to provide a process in which a high percentage conversion of arsenite to arsenate is attained.
- Another object is to provide a process of the kind described wherein high current densities may be used at the anode without seriously lowering either the current efiiciency or the percentage conversion of arsenite to arsenate.
- Another objects of the invention include the provision of a process in which deposition of elemental arsenic is avoided, and in which arsenate is produced at the cathode as well as at the anode.
- a porous carbonaceous anode is used.
- a nonporous insoluble cathode is Fig. 2 represents diagrammatically in vertical cross-section an electrolytic cell similar to that shown in Fig. '1 except that it contains two porous electrodes I2 and 22.
- electrolyte ll containing dissolved arsenite is electrolyzed by passage of electric current between a cathode I3 and a porous carbonaceous'anode 12, whereby arsenate is formed at the anode.
- Anolyte containing the arsenate is removed continuously from the cell Ill through the porous anode I2 as it is formed, and arsenite is fed to the cell ID from time to time or continuously. Diffusion of arsenate into the main body of the electrolyte ll may thus be prevented more or less completely. Evolution of oxygen may be avoided, high current densities may be employed, and a low operating cell voltage is obtained.
- the electrolyte composition remains unchanged, a uniform high concentration of arsenite is maintained at the active electrode surface,
- alkaline electrolyte containing the arsenite may be introduced into the cell l0 through the porous anode I2.
- the cathode is porous and carbonaceous.
- Fig. 1 represents diagrammatically in vertical cross-section an electrolytic cell container l0 containing an aqueous electrolyte l l in which are immersed a porous carbonaceous anode l2 and a nonporous cathode l3, and
- sodium arsenate may be continuously produced from the arsenite without recirculating the electrolyte solution.
- a carbonaceous material having a porosity above 35% preferably between 40% and 70%
- Percent porosity 100 (real density-apparent density) +real density
- an air permeability above 15, preferably above 30 preferably above 30.
- air permeability means the number of cubic inches of air per minute passing through one square inch cross-section of electrode material, when ,air at a pressure of one pound per square inch is blown through a block of the material one inch thick.
- the following table shows, for purposes of comparison, the porosity and permeability of ordinary electrode carbons (Types 1, 2, and 3) and of the special electrode carbons preferably used in the process of this invention (Types 4, 5, 6, and '7).
- Percent Air per- Type porosity meability tribution of the pores in the two kinds of materials may be distinguished by a simple test: if air is forced through a thin block of the material under water, at about the minimum air pressure required to obtain bubbles in the water, the porous material gives forth a cloud of small bubbles over its entire surface, while the leaky material gives a number of separate streams of bubbles issuing from the larger fissures and voids.
- Another test for uniformity of porosity of these materials comprises determining the flow of a viscous liquid, such as a concentrated aqueous solution of cane sugar, under a moderate pressure, for instance a head of about six inches, through a thin (e. g. one-eighth inch) section of the material. Any relatively large fissures permit flow of the solution and are there by made evident.
- a viscous liquid such as a concentrated aqueous solution of cane sugar
- Porous anode material for use in the process of" this invention may suitably be made: from comminuted solid carbonaceous material (for example, coke, graphite, or charcoal) and a porous carbonaceous binder (for instance, baked tar or pitch). Suitable methods for making such electrode material are described in'U. S. Patent 1,988,478, issued on January 22, 1935, to B. E. Broadwell and L. C. Working.
- Fig. 2 wherein a porous carbonaceous cathode 22 is employed and a cathodic depolarizer is introduced into the cell through the cathode.
- a suitable cathodic depolarizer is air blown through the cathode, and the oxygen of the air may be used very eifectively for depolarization if the cathode is made of carbonaceous material of the type used as electrodes in air-depolarized primary galvanic cells. Material of this type is disclosed for instance in U. S. Patent 2,010,608 issued August 6, 1935, to Erwin A. Schumacher, et al. A cathode of material of this kind may, if desired, be made repellent to electrolyte; several methods of achieving this object are well known.
- Depolarization of the cathode with oxygen maintains the cathode potentialat a level lower than that at which elemental arsenic can be deposited, thereby making feasible the complete elimination of diaphragms.
- the reduction in cathode potential and the elimination of diaphragms decrease the operating voltage of the cell more than fifty per cent.
- the cathode potential may be kept low enough to permit chemical oxidation of arsenite to arsenate.
- Method of oxidizing a water soluble arsenite to the correspondingarsenate which comprises passing an electric current through an aqueous electrolyte, containing said arsenite, between a cathode and a porous anode, whereby the arsenite is oxidized to arsenate at said anode, and promptly withdrawing through the pores of said anode anolyte containing said arsenate.
- Method of oxidizing a water soluble arsenite to the corresponding arsenate which comprises passing an electric current through an aqueous electrolyte, containing said arsenite, between a cathode and a porous anode, whereby the arsenite is oxidized to arsenate at said anode, and promptly withdrawing through said anode anolyte containing said arsenate; said porous anode ability above 15 and comprising comminuted solid carbonaceous material and a porous carbona ceous binder having uniformly distributed pores.
- Method of oxidizing sodium arsenite to sodium arsenate which comprises passing an electric current through an aqueous-electrolyte, containing sodium arsenite, between a cathode and a porous anode, said anode having a porosity between 40% and 70% and an air permeability above 30 and comprising comminuted solid carbonaceous material and a porous carbonaceous binder having uniformly distributed pores, whereby sodium arsenite is oxidized to sodium arsenate at the porous anode, and continuously withdrawing through said porous anode anolyte containing said sodium arsenate.
- Method of oxidizing a water soluble arsenite to the corresponding arsenate which comprises passing an electric current through an aqueous electrolyte, containing said sodium arsenite, between a porous cathode and a porous anode of an electrolytic cell, passing a cathodic depolarizing fluid through the porous cathode into the.
- Method of oxidizing sodium arsenite to sodium arsenate which comprises passing an electric current through an aqueous electrolyte,
- porous cathode being composed of carbonaceous material capable of depolarization by air and said cathode and anode having a porosity between 40% and 70% and an air permeability above 30 and comprising comminuted solid carbonaceous material and a porous carbonaceous binder having uniformly distributed pores, passing air through said cathode into the cell, and continuously removing through said anode anolyte containing sodium arsenate.
- Method of oxidizing a water soluble arsenite to the corresponding arsenate which comprises passing an electrolyte containing said arsenite through a porous anode of an electrolytic cell containing said anode and an air depolarizable porous carbon cathode, passing air through the porous carbon cathode into the cell in an amount sufficient to depolarize the cathode, and passing an electric current through said anode and cathode.
Description
INVENTORS GEORGE W. HEISE MILTON JANES BY ATTORNEY FIG.
FIG. 2
M. JANES ETAL ELECTROLYTIC PROCESS OF PREPARING ARSENATES Filed Dec. 17, 1938 Oct. 7, 1941.
Patented Oct. 7, 1941 ELECTROLYTIC PROCESS OF PREPARING ARSENATES Milton Janes, Lakewood, and George W.
Heise,
Rocky River, Ohio, assignors to National Carbon Company, Inc., a corporation of New York Application December 17, 1938, Serial No. 246,280
'1 Claims.
This invention relates to an electrolytic process in which an impressed electric current is passed through a cell having insoluble electrodes immersed in an aqueous electrolyte. More specifl cally, the invention is a process for electrolytically oxidizing a water soluble arsenite, such as sodium or other alkaline metal arsenite, to the corresponding arsenate.
It has heretofore been proposed to oxidize arsenites, obtained for instance by dissolving arsenious oxide in an alkaline solution, to arsenates by anodic oxidation at a solid anode accord-,
ing to the reaction:
Na3AsOs+H2O+ (2F) :Na3AsO4+H2 High current efficiency has been attained only by the use of diaphragms which increase the operating voltage, of low current density,.and of agitation oi! the solution. Formation of elemental arsenic at the cathode involves a loss of product and tends to foul the diaphragms. I Current efliclency decreases with decreased concentration of arsenite, and batch operation has been customary.
It is an object of this invention to provide a continuous process for oxidizing arsenites to arsenates at a high current efllciency. A further object is to lower the operating voltage in such a process. Another object is to make possible the elimination of diaphragms in the .process. Still another object is to provide a process in which a high percentage conversion of arsenite to arsenate is attained. Another object is to provide a process of the kind described wherein high current densities may be used at the anode without seriously lowering either the current efiiciency or the percentage conversion of arsenite to arsenate.
Other objects of the invention include the provision of a process in which deposition of elemental arsenic is avoided, and in which arsenate is produced at the cathode as well as at the anode.
These and other objects of the invention are attained by a process in which a porous carbonaceous anode is used. In one embodiment of the invention a nonporous insoluble cathode is Fig. 2 represents diagrammatically in vertical cross-section an electrolytic cell similar to that shown in Fig. '1 except that it contains two porous electrodes I2 and 22.
In accordance with one application of the invention, illustrated by Fig. 1, electrolyte ll containing dissolved arsenite is electrolyzed by passage of electric current between a cathode I3 and a porous carbonaceous'anode 12, whereby arsenate is formed at the anode. Anolyte containing the arsenate is removed continuously from the cell Ill through the porous anode I2 as it is formed, and arsenite is fed to the cell ID from time to time or continuously. Diffusion of arsenate into the main body of the electrolyte ll may thus be prevented more or less completely. Evolution of oxygen may be avoided, high current densities may be employed, and a low operating cell voltage is obtained. I
It will ordinarily be desirable to use a diaphragm to isolate the catholyte in this application of the invention.
During continuous or prolonged operation of the cell, the electrolyte composition remains unchanged, a uniform high concentration of arsenite is maintained at the active electrode surface,
and both a high current efficiency and a high percentage conversion are obtained.
In an alternative embodiment, alkaline electrolyte containing the arsenite may be introduced into the cell l0 through the porous anode I2.
In actual practice-of the above-described embodlmentvof the invention, current densities as high as 100 amperes per square foot of anode superficial area have been used successfully, andeven at this current density an overall current efllciency of 92% to 99% and a 90% conversion of sodium arsenite to sodium arsenate have been maintained.
used; in another embodiment the cathode is porous and carbonaceous. I
The invention will be more particularly described with reference to the accompanying drawing in which:
Fig. 1 represents diagrammatically in vertical cross-section an electrolytic cell container l0 containing an aqueous electrolyte l l in which are immersed a porous carbonaceous anode l2 and a nonporous cathode l3, and
In typical experiments a solution containing 40 grams of arsenious oxide and 54 grams of sodium hydroxide per liter was electrolyzed at 28 C. and
at an anode current density of l4-'amperes per square foot. Using a nonporous graphite anode and an iron cathode the cell operating voltage was 3.17; whereas when a porous graphite anode and an iron cathode were usedthe cell operating voltage was 2.45. In each instance, a single diaphragm was used.
Because of the high conversiun-efiiciency, sodium arsenate may be continuously produced from the arsenite without recirculating the electrolyte solution.
Although various materials may be used more ,or less successfully as the anode l2, we prefer a carbonaceous material having a porosity above 35% (preferably between 40% and 70%), calculated as follows: Percent porosity=100 (real density-apparent density) +real density; and an air permeability above 15, preferably above 30. Whenever used herein and in the appended claims, the term air permeability means the number of cubic inches of air per minute passing through one square inch cross-section of electrode material, when ,air at a pressure of one pound per square inch is blown through a block of the material one inch thick. The following table shows, for purposes of comparison, the porosity and permeability of ordinary electrode carbons (Types 1, 2, and 3) and of the special electrode carbons preferably used in the process of this invention (Types 4, 5, 6, and '7).
Percent Air per- Type porosity meability tribution of the pores in the two kinds of materials may be distinguished by a simple test: if air is forced through a thin block of the material under water, at about the minimum air pressure required to obtain bubbles in the water, the porous material gives forth a cloud of small bubbles over its entire surface, while the leaky material gives a number of separate streams of bubbles issuing from the larger fissures and voids.
Another test for uniformity of porosity of these materials comprises determining the flow of a viscous liquid, such as a concentrated aqueous solution of cane sugar, under a moderate pressure, for instance a head of about six inches, through a thin (e. g. one-eighth inch) section of the material. Any relatively large fissures permit flow of the solution and are there by made evident.
Porous anode material for use in the process of" this invention may suitably be made: from comminuted solid carbonaceous material (for example, coke, graphite, or charcoal) and a porous carbonaceous binder (for instance, baked tar or pitch). Suitable methods for making such electrode material are described in'U. S. Patent 1,988,478, issued on January 22, 1935, to B. E. Broadwell and L. C. Working.
If the process of the invention is operated as described above, some metallic arsenic is deposited at the cathode by a side reaction:
' trated. by Fig. 2, wherein a porous carbonaceous cathode 22 is employed and a cathodic depolarizer is introduced into the cell through the cathode.
A suitable cathodic depolarizer is air blown through the cathode, and the oxygen of the air may be used very eifectively for depolarization if the cathode is made of carbonaceous material of the type used as electrodes in air-depolarized primary galvanic cells. Material of this type is disclosed for instance in U. S. Patent 2,010,608 issued August 6, 1935, to Erwin A. Schumacher, et al. A cathode of material of this kind may, if desired, be made repellent to electrolyte; several methods of achieving this object are well known.
Depolarization of the cathode with oxygen maintains the cathode potentialat a level lower than that at which elemental arsenic can be deposited, thereby making feasible the complete elimination of diaphragms. The reduction in cathode potential and the elimination of diaphragms decrease the operating voltage of the cell more than fifty per cent.
If a moderate current density is used, the cathode potential may be kept low enough to permit chemical oxidation of arsenite to arsenate.
anode current density of 28 amperes per square foot the cell voltage was 1.37. Current efliciencies 103% to 168% of theoretical were attained, and arsenite to arsenate conversions of 57% to It is ordinarily advantageous'to pass material through the respective porous electrodes at at least that .rate which is required to supply that amount of reactant, which can theoretically be acted upon by the current used, and a greater rate is usually preferable. For example, it is obvious that with an air depolarized cathode, enough oxygen must be provided to permit chemical oxidation as well as cathodic depolarization, and a rate several hundred per cent the electrochemical requirement may be desirable.
It will readily be understood that the specific descriptions of operating conditions disclosed herein are only by way of example, and that the invention is not limited to such specific examples.
We claim:
1. Method of oxidizing a water soluble arsenite to the correspondingarsenate which comprises passing an electric current through an aqueous electrolyte, containing said arsenite, between a cathode and a porous anode, whereby the arsenite is oxidized to arsenate at said anode, and promptly withdrawing through the pores of said anode anolyte containing said arsenate.
2. Method of oxidizing a water soluble arsenite to the corresponding arsenate which comprises passing an electric current through an aqueous electrolyte, containing said arsenite, between a cathode and a porous anode, whereby the arsenite is oxidized to arsenate at said anode, and promptly withdrawing through said anode anolyte containing said arsenate; said porous anode ability above 15 and comprising comminuted solid carbonaceous material and a porous carbona ceous binder having uniformly distributed pores.
3. Method of oxidizing sodium arsenite to sodium arsenate which comprises passing an electric current through an aqueous-electrolyte, containing sodium arsenite, between a cathode and a porous anode, said anode having a porosity between 40% and 70% and an air permeability above 30 and comprising comminuted solid carbonaceous material and a porous carbonaceous binder having uniformly distributed pores, whereby sodium arsenite is oxidized to sodium arsenate at the porous anode, and continuously withdrawing through said porous anode anolyte containing said sodium arsenate.
4. Method of oxidizing a water soluble arsenite to the corresponding arsenate which comprises passing an electric current through an aqueous electrolyte, containing said sodium arsenite, between a porous cathode and a porous anode of an electrolytic cell, passing a cathodic depolarizing fluid through the porous cathode into the.
cell, and removing through the pores of said anode anolyte containing sodium arsenate.
5. Method as defined in claim 4, wherein the cathode is composed of material capable of depolarization by air and the depolarizing fluid is air.
6. Method of oxidizing sodium arsenite to sodium arsenate which comprises passing an electric current through an aqueous electrolyte,
containing sodium arsenite, between a porous cathode and a porous anode of an electrolytic cell, said porous cathode being composed of carbonaceous material capable of depolarization by air and said cathode and anode having a porosity between 40% and 70% and an air permeability above 30 and comprising comminuted solid carbonaceous material and a porous carbonaceous binder having uniformly distributed pores, passing air through said cathode into the cell, and continuously removing through said anode anolyte containing sodium arsenate.
7. Method of oxidizing a water soluble arsenite to the corresponding arsenate which comprises passing an electrolyte containing said arsenite through a porous anode of an electrolytic cell containing said anode and an air depolarizable porous carbon cathode, passing air through the porous carbon cathode into the cell in an amount sufficient to depolarize the cathode, and passing an electric current through said anode and cathode.
MILTON JANES.
GEORGE W. HEISE.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US246280A US2257746A (en) | 1938-12-17 | 1938-12-17 | Electrolytic process of preparing arsenates |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US246280A US2257746A (en) | 1938-12-17 | 1938-12-17 | Electrolytic process of preparing arsenates |
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| Publication Number | Publication Date |
|---|---|
| US2257746A true US2257746A (en) | 1941-10-07 |
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| US246280A Expired - Lifetime US2257746A (en) | 1938-12-17 | 1938-12-17 | Electrolytic process of preparing arsenates |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2539092A (en) * | 1940-11-12 | 1951-01-23 | Gen Motors Corp | Electrolytic apparatus for reduction of aluminum bromide |
| US2816197A (en) * | 1955-12-12 | 1957-12-10 | Gen Electric | Switch |
| US2862863A (en) * | 1957-09-23 | 1958-12-02 | Kenneth F Griffith | Apparatus for electrolytic production of a metal product from fused salts |
| US3032635A (en) * | 1960-10-03 | 1962-05-01 | August L Kraft | Heater and utilization system for converting small quantities of fusible solids |
-
1938
- 1938-12-17 US US246280A patent/US2257746A/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2539092A (en) * | 1940-11-12 | 1951-01-23 | Gen Motors Corp | Electrolytic apparatus for reduction of aluminum bromide |
| US2816197A (en) * | 1955-12-12 | 1957-12-10 | Gen Electric | Switch |
| US2862863A (en) * | 1957-09-23 | 1958-12-02 | Kenneth F Griffith | Apparatus for electrolytic production of a metal product from fused salts |
| US3032635A (en) * | 1960-10-03 | 1962-05-01 | August L Kraft | Heater and utilization system for converting small quantities of fusible solids |
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