US700671A - Reduction of azo compounds. - Google Patents
Reduction of azo compounds. Download PDFInfo
- Publication number
- US700671A US700671A US3096600A US1900030966A US700671A US 700671 A US700671 A US 700671A US 3096600 A US3096600 A US 3096600A US 1900030966 A US1900030966 A US 1900030966A US 700671 A US700671 A US 700671A
- Authority
- US
- United States
- Prior art keywords
- tin
- cathode
- azo compounds
- reduction
- electrolytic
- 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
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- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 22
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 9
- 239000012530 fluid Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000000203 mixture Substances 0.000 description 5
- 229960000443 hydrochloric acid Drugs 0.000 description 4
- 235000011167 hydrochloric acid Nutrition 0.000 description 4
- -1 azo compound Chemical class 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- CQPFMGBJSMSXLP-UHFFFAOYSA-M acid orange 7 Chemical compound [Na+].OC1=CC=C2C=CC=CC2=C1N=NC1=CC=C(S([O-])(=O)=O)C=C1 CQPFMGBJSMSXLP-UHFFFAOYSA-M 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 239000010405 anode material Substances 0.000 description 1
- 229950011260 betanaphthol Drugs 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000002101 lytic effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000002828 nitro derivatives Chemical class 0.000 description 1
- 125000000449 nitro group Chemical group [O-][N+](*)=O 0.000 description 1
- 238000009738 saturating Methods 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
- C25B3/00—Electrolytic production of organic compounds
- C25B3/20—Processes
- C25B3/25—Reduction
Definitions
- LMAX B UCHNER a citizen of the Empire of Germany, residing at Mannheim, in the Empire of Germany, have inventprocess of reducing nitro compounds to the corresponding amines by means of electro lytic action used in connection with a tin cathode or of an indifferent cathode and anelectrolytic fluid containing tin, the process consisting, more specifically, in introducing the nitro bodies dissolved or suspended in hydrochloric acid into the cathode-space of an electrolytic cell and submitting the same to action of the current. I have found in the course of subsequent experiments that this treatment may be applied also forthe purpose of reducing azo compounds.
- tin or indifferent cathode it is desirable to first coat the tin or indifferent cathode with a layer of tin sponge to maintain an elevated temperature, preferably about 60 centigrade, in the cathodespace and to operate with lower current densities than indicated in the aforesaid application.
- the preparation of the cathode may be dispensed with if at the beginning of electrolysis a relatively small quantity of electrolytically-precipitated powdered tin is added to the electrolytic fiuid.
- My invention therefore, broadly considered, consists in passing an electrolytic current through an azo body dissolved or suspended in an electrolytic fluid in the presence of tin, and more specifically in the use in connection therewith of an addition of tin to the tin or indifferent cathode and of an elevated temperature.
- cathodecompartment I Into the cathodecompartment I pour a mixture consisting of 48.7 parts,by weight,of chlorid of para-amidoazo-benzol, five grams of powdered electrolytically -precipitated tin dissolved or suspended in one hundred parts, by volume, of Water and two hundred and fifty parts, by volume, of fuming hydrochloric acid. An electric current is then passed through a tin or indifferent cathode. The liquid mixture is vigorously agitated or stirred during the course of the electrolysis,whose completion is indicated by the commencement of an active evolution of hydrogen.
- the current employed is preferably of a density of three hundred to four hundred amperes per square meter, and the temperature employed in the cathode-space is advantageously 60 centigrade.
- Theresultingparaphenylene-diamine is precipitated in the form of a chlorid by saturating the cathode electrolyte with hydrochloric-acid gas in the cold, the anilin, which is produced at the sametime, remaining in solution.
- Example 2 Re(luction of orange II to amz'do-beta-naphthoL-The same arrangement of electrolytic cell and the same materials for the anode-space as in Example 1 are-employed in this case.
- I charge the oathode compartment with a mixture of thirtythree parts, by weight, of orange II, two hundred and fifty parts, by weight, of water and two hundred and fifty parts, by weight, of fuming hydrochloric acid.
- I also add a quantity of powdered tin, as in the first example, if an indifferent cathode is employed, and, in general, conduct the operation as in said example. Even if a tin cathode is employed dispensable.
- the amido-beta-naphthol produced under these conditions is isolated and purified. according to well-known methods.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Electrolytic Production Of Metals (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Description
UNITED STATES PATENT FFICE;
MAX BUCHNERyOF MANNI-IEIM, GERMANY.
REDUCTION OF AZO COMPOUNDS.
SPECIFICATION forming part of Letters Patent No. 700,671, dated May 20, 1902.
Application filed September 24,1900. Serial No. 30,966- (No specimens.)
To all whom it may concern:
Be it known that LMAX B UCHNER, a citizen of the Empire of Germany, residing at Mannheim, in the Empire of Germany, have inventprocess of reducing nitro compounds to the corresponding amines by means of electro lytic action used in connection with a tin cathode or of an indifferent cathode and anelectrolytic fluid containing tin, the process consisting, more specifically, in introducing the nitro bodies dissolved or suspended in hydrochloric acid into the cathode-space of an electrolytic cell and submitting the same to action of the current. I have found in the course of subsequent experiments that this treatment may be applied also forthe purpose of reducing azo compounds. In this case, however, it is desirable to first coat the tin or indifferent cathode with a layer of tin sponge to maintain an elevated temperature, preferably about 60 centigrade, in the cathodespace and to operate with lower current densities than indicated in the aforesaid application.
It is to be observed that the preparation of the cathode may be dispensed with if at the beginning of electrolysis a relatively small quantity of electrolytically-precipitated powdered tin is added to the electrolytic fiuid.
My invention therefore, broadly considered, consists in passing an electrolytic current through an azo body dissolved or suspended in an electrolytic fluid in the presence of tin, and more specifically in the use in connection therewith of an addition of tin to the tin or indifferent cathode and of an elevated temperature.
My invention, moreover, comprises such further features as will be hereinafter described and pointed out in the claims.
To enable those skilled in the art to carry out my invention, I will now describe the same in detailby reciting the following examples, which constitute what I consider the preferable embodiment of the same.
Example 1-Reduction ofpara-cm'zido-azobenzol to paraphenylene-(Z'iamine.-An electrolytic cell is divided into an anode and a cathode space by a suitable diaphragm, as will be readily understood. A ten-percent. solution of sulfuric acid is poured into the anodespace,and anode of indifferent anode material, such as lead, is introduced. Into the cathodecompartment I pour a mixture consisting of 48.7 parts,by weight,of chlorid of para-amidoazo-benzol, five grams of powdered electrolytically -precipitated tin dissolved or suspended in one hundred parts, by volume, of Water and two hundred and fifty parts, by volume, of fuming hydrochloric acid. An electric current is then passed through a tin or indifferent cathode. The liquid mixture is vigorously agitated or stirred during the course of the electrolysis,whose completion is indicated by the commencement of an active evolution of hydrogen. The current employed is preferably of a density of three hundred to four hundred amperes per square meter, and the temperature employed in the cathode-space is advantageously 60 centigrade. Theresultingparaphenylene-diamine is precipitated in the form of a chlorid by saturating the cathode electrolyte with hydrochloric-acid gas in the cold, the anilin, which is produced at the sametime, remaining in solution.
Example 2 Re(luction of orange II to amz'do-beta-naphthoL-The same arrangement of electrolytic cell and the same materials for the anode-space as in Example 1 are-employed in this case. I charge the oathode compartment with a mixture of thirtythree parts, by weight, of orange II, two hundred and fifty parts, by weight, of water and two hundred and fifty parts, by weight, of fuming hydrochloric acid. I also add a quantity of powdered tin, as in the first example, if an indifferent cathode is employed, and, in general, conduct the operation as in said example. Even if a tin cathode is employed dispensable. The amido-beta-naphthol produced under these conditions is isolated and purified. according to well-known methods.
What I claim, and desire to secure by Letters Patent of the United States, is
1. The process of reducing azo compounds which consists in passing an electric current through such azo compounds dissolved or suspended in an electrolytic fluid capable of dissolving tin in the presence of tin, the azo compound and tin being arranged in the cathode-compartment.
2. The process of reducing azo compounds which consists in passing an electric current through such azo compounds dissolved or suspended in an electrolytic fluid containing tin, the azo compound and tin being arranged in the cathode-compartment.
3. The process of reducing azo compounds which consists in passing an electric current through such 'azo compounds dissolved or suspended in an electrolytic fluid capable of dissolving tin in the presence of tin and at an elevated temperature, the electrolytic fluid being capable of dissolving tin and the tin 6. The process of reducing azo compounds which consists in charging the cathode-space of an electrolytic cell with a mixture of the azo compound and powdered tin with water and hydrochloric acid and then passing the electrolytic current through the mixture.
In testimony whereof I affix my signature in presence of two witnesses.
MAX BUCHNER.
l/Vitnesses:
JACOB ADRIAN, FRITZ A011.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US3096600A US700671A (en) | 1900-09-24 | 1900-09-24 | Reduction of azo compounds. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US3096600A US700671A (en) | 1900-09-24 | 1900-09-24 | Reduction of azo compounds. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US700671A true US700671A (en) | 1902-05-20 |
Family
ID=2769202
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US3096600A Expired - Lifetime US700671A (en) | 1900-09-24 | 1900-09-24 | Reduction of azo compounds. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US700671A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5496143A (en) * | 1994-04-11 | 1996-03-05 | Breyer; Stephen R. | Tree and shrub lifting system |
-
1900
- 1900-09-24 US US3096600A patent/US700671A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5496143A (en) * | 1994-04-11 | 1996-03-05 | Breyer; Stephen R. | Tree and shrub lifting system |
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