US2297252A - Process for the purification of solutions that serve as generators for percompounds - Google Patents
Process for the purification of solutions that serve as generators for percompounds Download PDFInfo
- Publication number
- US2297252A US2297252A US214245A US21424538A US2297252A US 2297252 A US2297252 A US 2297252A US 214245 A US214245 A US 214245A US 21424538 A US21424538 A US 21424538A US 2297252 A US2297252 A US 2297252A
- Authority
- US
- United States
- Prior art keywords
- solutions
- cell
- cathode
- persulfate
- solution
- 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 description 22
- 238000000746 purification Methods 0.000 title description 10
- 239000000243 solution Substances 0.000 description 51
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 26
- JRKICGRDRMAZLK-UHFFFAOYSA-L peroxydisulfate Chemical compound [O-]S(=O)(=O)OOS([O-])(=O)=O JRKICGRDRMAZLK-UHFFFAOYSA-L 0.000 description 25
- 238000004821 distillation Methods 0.000 description 16
- 239000012535 impurity Substances 0.000 description 10
- 230000003647 oxidation Effects 0.000 description 10
- 238000007254 oxidation reaction Methods 0.000 description 10
- 238000010405 reoxidation reaction Methods 0.000 description 10
- 125000004122 cyclic group Chemical group 0.000 description 9
- 150000002978 peroxides Chemical class 0.000 description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 239000003792 electrolyte Substances 0.000 description 4
- 150000004968 peroxymonosulfuric acids Chemical class 0.000 description 4
- 238000007865 diluting Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 1
- 235000011130 ammonium sulphate Nutrition 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000010406 cathode material Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
Definitions
- More particularly it relates to a process for the purification and reoxidation of solutions used in a cyclic process for the production of hydrogen peroxide.
- the residual liquor remaining after distillation contains valuable constituents and is, therefore, returned to electrolytic cells for reoxidation to persulfuric acid or persulfate as the case may be.
- the residual liquor obtained after such distillation also contains impurities, such as Caros acid (H2805), hydrogen peroxide itself and metallic impurities which act as catalysts, it has not previously been possible to carry out this reoxidation in a simple diaphragmless cell in which both anode and cathode are in a common chamber.
- a further object of this invention is to provide a. suitable cell in which this process may be carried out ly.
- Another object is to provide a process for the consideration of the specification and the claims and persulfates for the purpose of obtaining hydrogen peroxide therefrom.
- the residual solution obtained as a result of the distillation step after its usual dil'ution to the proper concentration, is first subjected to a cathodic reduction to free the solution from impurities such as Caros acid, hydrogen peroxide, metallic catalytic impurities and the like which detrimentally afiect reoxidation and thereafter reoxidized in one or more simple diaphragmless cells to obtain for redistillation a solution containing the desired amount of persulfuric acid orpersulfate.
- impurities such as Caros acid, hydrogen peroxide, metallic catalytic impurities and the like which detrimentally afiect reoxidation and thereafter reoxidized in one or more simple diaphragmless cells to obtain for redistillation a solution containing the desired amount of persulfuric acid orpersulfate.
- the cathodic potential most suitable for purification is obtained by a careful selection of cathode material, current density, cell resistance and speed of flow of the solution.
- the most suitable potential is preferably such that the impurities are reduced without appreciable reduction of the persulfate.
- the reduction itself is, therefore, carried out without any substantial change of concentration of persulfate with the result that the subsequent loss of oxygen during'distillation is minimized.
- this reoxidation may be omitted if desired, in which case 'the purified' solution leaving the cathod chamber is directly passed into theldiapliragmless cells for oxidation therein.
- the solution may be purified by passing it through th cathode chambers of a number of cells in series, and then if desired through the anode chambers of the cells.
- the cathode chamber of the diaphragm cell in v which the purification takes place may be of any desired construction or design.
- a diaphragm in the form of plates or the like may be built into the cell container to separate the two chambers.
- a cell particularly adaptable for use is shown in cross section in the accompanying drawing wherein casing 'I made of any suitable material contains a separated concentric cylindrical diaphragm 2, the outlet pipe 3 of which passes through an opening in the container to v which it is sealed at point 4.
- the cylindrical diaphragm 2 forms the enclosure for the cylinas theoperating time increases.
- drical anode chamber a which is connected with annular cathode chamber b by a series of holes 5 near its bottom.
- the cathode 5 surrounds the diaphragm 2 inside of which there is an anode I also of cylindrical shape.
- the electrolyte is introduced into the cathode chamber b at point c As a direct result of the present invention, it
- the diluted residue is uniformly passed through the cathode chambers of four cells in parallel and electrolyzed in each cell with a current of 2 amperes using a cathode current density of 0.01-0.02 ampere per square centimeter and an anode current density of 1.0 ampere per square centimeter at a temperature not above 20 (3'.
- persulfate as used herein includes persulfuric acid as well asthe persulfates such as the ammonium, potassium and sodium salts.
- the reoxidation in the diaphragmless cell may be defined as exposing the solution to simultaneous anodic oxidation and cathodic reduction to oxidize the solution to obtain the desired concentration of persulfate.”
- a continuous cyclic process for electrolytically producing hydrogen peroxide by distillation from a persulfate solution comprising distilling off the hydrogen peroxide therefrom, diluting the residual liquid, purifying the diluted liquid by subjecting it to cathodic reduction in the cathode chamber of at least one diaphragm cell in which the cathode potential is maintained suflicient to reduce the impurities in the solution without appreciably reducing the persulfate present-and subsequently reoxidizing the'so purified liquid by passingit through at least one diaphragmless cell wherein it is exposed to current conditions efiective for auodic oxidation to persulfates of high concentration.
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)
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DESCH112060D DE753434C (de) | 1937-02-13 | 1937-02-13 | Verfahren zur Reinigung von Loesungen, die zur Erzeugung von Perverbindungen dienen |
CH204843D CH204843A (de) | 1937-02-13 | 1938-04-01 | Verfahren und Vorrichtung zur Reinigung von Lösungen, die zur Erzeugung von Perverbindungen dienen. |
GB10544/38A GB509175A (en) | 1937-02-13 | 1938-04-06 | Improvements in or relating to the purification of solutions in a circulation process for the electrolytic production of hydrogen peroxide |
FR836493D FR836493A (fr) | 1937-02-13 | 1938-04-11 | Procédé et dispositif pour la purification de solutions qui servent à la production de percomposés |
NL88182A NL49589C (enrdf_load_stackoverflow) | 1937-02-13 | 1938-06-04 | |
US214245A US2297252A (en) | 1937-02-13 | 1938-06-17 | Process for the purification of solutions that serve as generators for percompounds |
Applications Claiming Priority (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DESCH112060D DE753434C (de) | 1937-02-13 | 1937-02-13 | Verfahren zur Reinigung von Loesungen, die zur Erzeugung von Perverbindungen dienen |
CH204843T | 1938-04-01 | ||
GB10544/38A GB509175A (en) | 1937-02-13 | 1938-04-06 | Improvements in or relating to the purification of solutions in a circulation process for the electrolytic production of hydrogen peroxide |
FR836493T | 1938-04-11 | ||
NL88182A NL49589C (enrdf_load_stackoverflow) | 1937-02-13 | 1938-06-04 | |
US214245A US2297252A (en) | 1937-02-13 | 1938-06-17 | Process for the purification of solutions that serve as generators for percompounds |
Publications (1)
Publication Number | Publication Date |
---|---|
US2297252A true US2297252A (en) | 1942-09-29 |
Family
ID=25993738
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US214245A Expired - Lifetime US2297252A (en) | 1937-02-13 | 1938-06-17 | Process for the purification of solutions that serve as generators for percompounds |
Country Status (6)
Country | Link |
---|---|
US (1) | US2297252A (enrdf_load_stackoverflow) |
CH (1) | CH204843A (enrdf_load_stackoverflow) |
DE (1) | DE753434C (enrdf_load_stackoverflow) |
FR (1) | FR836493A (enrdf_load_stackoverflow) |
GB (1) | GB509175A (enrdf_load_stackoverflow) |
NL (1) | NL49589C (enrdf_load_stackoverflow) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2431948A (en) * | 1943-11-01 | 1947-12-02 | Gen Motors Corp | Apparatus for electrodepositing metal on bearing shells and the like |
US3462351A (en) * | 1967-01-30 | 1969-08-19 | Kimberly Clark Co | Process for alkaline peroxide solution production including alkali concentration control |
US3506560A (en) * | 1967-01-30 | 1970-04-14 | Kimberly Clark Co | Electrolytic cell having novel electrolyte flow path means |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL30269C (enrdf_load_stackoverflow) * | 1930-02-20 | |||
DE548366C (de) * | 1930-08-18 | 1932-04-11 | Oesterr Chem Werke | Vorrichtung zur elektrolytischen Behandlung von Fluessigkeiten |
-
1937
- 1937-02-13 DE DESCH112060D patent/DE753434C/de not_active Expired
-
1938
- 1938-04-01 CH CH204843D patent/CH204843A/de unknown
- 1938-04-06 GB GB10544/38A patent/GB509175A/en not_active Expired
- 1938-04-11 FR FR836493D patent/FR836493A/fr not_active Expired
- 1938-06-04 NL NL88182A patent/NL49589C/xx active
- 1938-06-17 US US214245A patent/US2297252A/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2431948A (en) * | 1943-11-01 | 1947-12-02 | Gen Motors Corp | Apparatus for electrodepositing metal on bearing shells and the like |
US3462351A (en) * | 1967-01-30 | 1969-08-19 | Kimberly Clark Co | Process for alkaline peroxide solution production including alkali concentration control |
US3506560A (en) * | 1967-01-30 | 1970-04-14 | Kimberly Clark Co | Electrolytic cell having novel electrolyte flow path means |
Also Published As
Publication number | Publication date |
---|---|
FR836493A (fr) | 1939-01-18 |
NL49589C (enrdf_load_stackoverflow) | 1940-11-15 |
GB509175A (en) | 1939-07-12 |
CH204843A (de) | 1939-05-31 |
DE753434C (de) | 1951-10-31 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Lewis et al. | Concentration of H2 isotope | |
US2819950A (en) | Conversion of hydrogen sulfide to sulfur with quinones | |
US2795541A (en) | Electrolytic production of percompounds | |
US4236983A (en) | Process and apparatus for electrolysis of hydrochloric acid | |
US2297252A (en) | Process for the purification of solutions that serve as generators for percompounds | |
US2044888A (en) | Process of purifying alkali metal hydroxide solutions | |
US3721615A (en) | Process for the production of hydroquinone | |
US2813825A (en) | Method of producing perchlorates | |
US1942208A (en) | Means for obtaining lead in metallic condition | |
US3509031A (en) | Electrochemical oxidation of phenol | |
US1414423A (en) | Electrolytic separation of metals | |
US4129481A (en) | Uranium isotopic enrichment | |
US2417259A (en) | Electrolytic process for preparing manganese and manganese dioxide simultaneously | |
US2333578A (en) | Electrolytic chromate production | |
US3382163A (en) | Method of electrolytic extraction of metals | |
US1837177A (en) | Electrolytic process and apparatus | |
US2224831A (en) | Electrolysis cell | |
US825057A (en) | Method of making sulfuric acid. | |
US1322580A (en) | Method and apparatus for producing quinone and quinol | |
US2234908A (en) | Manufacture of hydrogen peroxide | |
US1937621A (en) | Electrolytic apparatus | |
US3134729A (en) | Electrolysis of sodium sulfate | |
US3262871A (en) | Preparation of phosphine | |
SU51390A1 (ru) | Способ электролитического получени перманганата кали | |
SU141860A1 (ru) | Способ получени сернокислого олова |