US1144271A - Apparatus for the continuous production by synthesis of hydrogen peroxid. - Google Patents
Apparatus for the continuous production by synthesis of hydrogen peroxid. Download PDFInfo
- Publication number
- US1144271A US1144271A US87570414A US1914875704A US1144271A US 1144271 A US1144271 A US 1144271A US 87570414 A US87570414 A US 87570414A US 1914875704 A US1914875704 A US 1914875704A US 1144271 A US1144271 A US 1144271A
- Authority
- US
- United States
- Prior art keywords
- tube
- hydrogen peroxid
- anode
- synthesis
- continuous production
- 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
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 title description 13
- 230000015572 biosynthetic process Effects 0.000 title description 4
- 238000010924 continuous production Methods 0.000 title description 4
- 238000003786 synthesis reaction Methods 0.000 title description 4
- 239000003792 electrolyte Substances 0.000 description 7
- 239000010406 cathode material Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000004020 conductor Substances 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 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
- C25B1/01—Products
- C25B1/28—Per-compounds
- C25B1/30—Peroxides
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/46—Apparatus for electrochemical processes
- C02F2201/461—Electrolysis apparatus
- C02F2201/46105—Details relating to the electrolytic devices
- C02F2201/46155—Heating or cooling
Definitions
- My invention relates to apparatus for the continuous production, by synthesis, of hydrogen peroxid.
- the improved apparatus described in the present specification offers the advantage of avoiding all the draw-backs aforesaid.
- the inner surface of a tube consisting of a suitable metal adapted to withstand high pressure is coated with a suitable electrode material serving as cathode, while the anode covered with a suitable tubular diaphragm is arranged in the middle axis of the tube aforesaid.
- This arrangement of parts ren- (lets it possible to either cause the electrolyte to circulate within the apparatus by aid of a pump, or else to pass through a plurality of such devices, one after the other without passing through the anode chamber, so that the hydrogen peroxid formed is not decomposed again.
- a tube A of a suitable metal having walls 2% to 3 in. thick is coated inwardly with a thin layer of cathode substance. It is closed at both ends by screw-caps B B inwardly coated with some substance resisting the action of the electrolyte.
- a rod shaped anode C covered by a tubular diaphragm K passes through cap B.
- the electrolyte is pressed through an inlet D into the tube A and leaves it through an outlet E.
- Oxygen forced in through a flanged socket F pr0- vided with a suitable nozzle is made to rise in the liquid in minute bubbles.
- the elec trolyte and the oxygen are then conducted through the tube G into a second apparatus of the same type, a'nd so on. It is, however. quite feasible to cause the electrolyte to circulate within a single apparatus, the tube G being then connected both to the outi to the compressor, while the solution of hydrogen peroxid may be either removed or else be passed through the battery of apparatus once more
- a metallic vessel adapted to withstand high pressure, a layer of suitable cathode material on the inner surface of said vessel, an anode within said vessel and a diaphragm surrounding the anode.
- a metal tube adapted to withstand high pressure, screw-ca s on the ends of said tube, a layer of suita le cathode material on the inner surface of said tube, an anode passing through one of said screw-caps and extendin the middle axis of said tube, a
- a plurality of metallic vessels adapted to Withstandhigh pressure, coated inwardly with cathode material, surrounding an anode covered with a tubular diaphra m, each vessel provided with liquid and gas inlets and outlets and tubes connecting the liquid outlet of a vessel with the li uid inlet of another vessel.
Landscapes
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (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
W. WEBER.
APPARATUS FOR THE CONTINUOUS PRODUCTION BY SYNTHESIS OF HYDROGEN PEROXID.
' APPLICATION FILED DEC.5, 1914- Wfinesses: Invenlur Patented June 22, 1915.
WALTER WEBER, 0F DUSSELDORF, GERMANY, ASSIG-NOR TO THE FIRM OF HENKEL & CIE., OF DUSSELDORF, GERMANY.
APPARATUS FOR THE CONTINUOUS PRODUCTION BY SYNTHESIS OF HYDROGEN PEROXID.
Specification of LettersPatent.
Patented June 22, 1915.
Application filed December 5, 1914. Serial No. 8%,704.
To all whom it may concern Be it known that I, WALTER WVEBER, citizen of the German Empire, residing at Dusseldorf, Germany, have invented certain new and useful Improvements in an Apparatus for-the Continuous Production by Synthesis of Hydrogen Peroxid, of which the following is a specification.
My invention relates to apparatus for the continuous production, by synthesis, of hydrogen peroxid. V
In a former application for Letters Patent of the United States, filed June 16, 1913, Serial No. 774053, and for which a patent was issued on the thirtieth day of September, 1913, numbered 1,074,549, an apparatus has been described which consists of a tubular anode inclosed within a tube adapted to stand high pressure and surrounding the cathode, all these parts being separated from each other by tubular diaphragms.
In using the aforesaid apparatus for the production of hydrogen peroxid on a commercial scale there arose the difficulty that it was not possible to make the electrolyte pass through it several timesso as to increase its percentage of peroxid. Such a mode of operation was out of question for the simple reason that the hydrogen peroxid formed in the first operation would, if introduced into the apparatus anew, passalso through the anode chamber and, in passing therethrough, be decomposed instantaneously. For this same reason it proved impossible also to connect a plurality of such apparatus in series inorder to gradually increase the percentage of hydrogen peroxid. Although the concentration of about three per cent. obtainable in an apparatus of this kind is sufficiently high for most technical purposes, a higher concentration is very desirable indeed, but it is impossible to obtain it except by causin the electrolyte to circulate with1n a sing e apparatus or to pass through a series of apparatus connected with each other. Another draw-back connected with the old device is the impossibility of cooling the anode itself although" considering the current density preferably used such a cooling would greatly contribute to an increase in output.
The improved apparatus described in the present specification offers the advantage of avoiding all the draw-backs aforesaid.
According to the present invention the inner surface of a tube consisting of a suitable metal adapted to withstand high pressure is coated with a suitable electrode material serving as cathode, while the anode covered with a suitable tubular diaphragm is arranged in the middle axis of the tube aforesaid. This arrangement of parts ren- (lets it possible to either cause the electrolyte to circulate within the apparatus by aid of a pump, or else to pass through a plurality of such devices, one after the other without passing through the anode chamber, so that the hydrogen peroxid formed is not decomposed again. It is further possible to effect an electrical connection of a plurality of such apparatus in series so as to cause the electrical current to pass through one after the other, in order to diminish the costs for the generator and the conductors. Moreover the metallic tube being easily inclosed within a water jacket a very effective cooling of the whole cathode is rendered possible. The surface of the cathode employed is exceedingly great as compared with the cathode substance.
The drawings show in section the form of my new apparatus at present preferred by me. o
A tube A of a suitable metal having walls 2% to 3 in. thick is coated inwardly with a thin layer of cathode substance. It is closed at both ends by screw-caps B B inwardly coated with some substance resisting the action of the electrolyte. A rod shaped anode C covered by a tubular diaphragm K passes through cap B. The electrolyte is pressed through an inlet D into the tube A and leaves it through an outlet E. Oxygen forced in through a flanged socket F pr0- vided with a suitable nozzle is made to rise in the liquid in minute bubbles. The elec trolyte and the oxygen are then conducted through the tube G into a second apparatus of the same type, a'nd so on. It is, however. quite feasible to cause the electrolyte to circulate within a single apparatus, the tube G being then connected both to the outi to the compressor, while the solution of hydrogen peroxid may be either removed or else be passed through the battery of apparatus once more in order to increase the concentration. I
I claim:
1. In electrolytic apparatus for making hydrogen peroxid, in combination, a metallic vessel adapted to withstand high pressure, a layer of suitable cathode material on the inner surface of said vessel, an anode within said vessel and a diaphragm surrounding the anode.
2. In electrolytic hydro en peroxid, in combination a meta tube c osed at both ends and adapted to withstand high pressure, a layer of suitable cathode material on the inner surface of said tube, an anode arranged in the middle axis of said tube and a tubular diaphragm surrounding the anode.
3. In electrolytic apparatus for makin hydrogen peroxid, in combination a metafi tube closed at both ends and adapted to withapparatus for makin stand 'high pressure, a layer of suitable cathode material on the inner surface of said tube, an anode arranged in the middle axis of said tube,.a tubular diaphra surrounding the anode and a water jac et surrounding said tube.
4. In electrolytic apparatus for making hydrogen peroxid, in combination, a metal tube adapted to withstand high pressure, screw-ca s on the ends of said tube, a layer of suita le cathode material on the inner surface of said tube, an anode passing through one of said screw-caps and extendin the middle axis of said tube, a
along tubular iaphragm surrounding the anode,
a li uid inlet and a gas inlet in one and a liquid outlet in the other screw-cap and a water jacket surrounding said tube.
5. In electrolytic apparatus for making hydrogen peroxid, a plurality of metallic vessels adapted to Withstandhigh pressure, coated inwardly with cathode material, surrounding an anode covered with a tubular diaphra m, each vessel provided with liquid and gas inlets and outlets and tubes connecting the liquid outlet of a vessel with the li uid inlet of another vessel.
n testimony whereof I have hereunto set my hand in presence of two subscribing witnesses.
HELEN NUFER, CLARIoE EAGER.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US87570414A US1144271A (en) | 1914-12-05 | 1914-12-05 | Apparatus for the continuous production by synthesis of hydrogen peroxid. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US87570414A US1144271A (en) | 1914-12-05 | 1914-12-05 | Apparatus for the continuous production by synthesis of hydrogen peroxid. |
Publications (1)
Publication Number | Publication Date |
---|---|
US1144271A true US1144271A (en) | 1915-06-22 |
Family
ID=3212360
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US87570414A Expired - Lifetime US1144271A (en) | 1914-12-05 | 1914-12-05 | Apparatus for the continuous production by synthesis of hydrogen peroxid. |
Country Status (1)
Country | Link |
---|---|
US (1) | US1144271A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2439491A (en) * | 1942-06-02 | 1948-04-13 | Schiffl Charles | Enclosed electroplating tank |
-
1914
- 1914-12-05 US US87570414A patent/US1144271A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2439491A (en) * | 1942-06-02 | 1948-04-13 | Schiffl Charles | Enclosed electroplating tank |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2070612A (en) | Method of producing, storing, and distributing electrical energy by operating gas batteries, particularly oxy-hydrogen gas batteries and electrolyzers | |
JP2019500498A (en) | Stand-alone system for clamping high temperature SOEC / SOFC stacks | |
SU971110A3 (en) | Electrolyzer for producing chlorine and alkali | |
US5378324A (en) | Process and an electrolytic cell for the production of fluorine | |
JPH08246177A (en) | Production of hydride for transporting and storing hydrogen and device therefor | |
US1144271A (en) | Apparatus for the continuous production by synthesis of hydrogen peroxid. | |
US4824534A (en) | Process for electrically separating the electrolyte-bearing mains from the electrolyte spaces of an electrochemical cell pile | |
US577523A (en) | Deesso | |
US2219342A (en) | Apparatus for electrolysis | |
US586236A (en) | eulin | |
JP3110555B2 (en) | Ion exchange membrane electrolyzer | |
US1263314A (en) | Apparatus for electrolysis. | |
US1199472A (en) | Electrolytic apparatus. | |
US1250183A (en) | Electrolytic cell. | |
GB191422714A (en) | Improvements in or relating to Apparatus for Manufacturing Hydrogen Peroxide. | |
US587437A (en) | Ferdinand hurter | |
US1806801A (en) | Teners limited | |
US3796647A (en) | Apparatus for hydrogen production | |
US698292A (en) | Process of recovering metals. | |
US1983296A (en) | Arrangement in multicell electrolyzers | |
US528322A (en) | Hamilton young castner | |
US1212229A (en) | Apparatus for the production of oxygen and hydrogen gases. | |
US987717A (en) | Electrolytic cell. | |
US885054A (en) | Gas element for converting the energy of combustible or other suitable reducing substances to electric current. | |
CN208293089U (en) | A kind of hydrogen-rich water generator |