US1539297A - Method for producing lead compounds - Google Patents
Method for producing lead compounds Download PDFInfo
- Publication number
- US1539297A US1539297A US648872A US64887223A US1539297A US 1539297 A US1539297 A US 1539297A US 648872 A US648872 A US 648872A US 64887223 A US64887223 A US 64887223A US 1539297 A US1539297 A US 1539297A
- Authority
- US
- United States
- Prior art keywords
- lead
- catholyte
- set forth
- ethyl
- alkyl
- 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
- 150000002611 lead compounds Chemical class 0.000 title description 6
- 238000004519 manufacturing process Methods 0.000 title description 2
- 238000000034 method Methods 0.000 description 21
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 15
- 150000001350 alkyl halides Chemical class 0.000 description 14
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 10
- MRMOZBOQVYRSEM-UHFFFAOYSA-N tetraethyllead Chemical group CC[Pb](CC)(CC)CC MRMOZBOQVYRSEM-UHFFFAOYSA-N 0.000 description 9
- HVTICUPFWKNHNG-UHFFFAOYSA-N iodoethane Chemical compound CCI HVTICUPFWKNHNG-UHFFFAOYSA-N 0.000 description 7
- 235000019441 ethanol Nutrition 0.000 description 6
- 125000000217 alkyl group Chemical group 0.000 description 5
- -1 lead acetate Chemical class 0.000 description 5
- 229940046892 lead acetate Drugs 0.000 description 5
- 238000009835 boiling Methods 0.000 description 4
- 239000003792 electrolyte Substances 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 150000001351 alkyl iodides Chemical class 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- BLXSFCHWMBESKV-UHFFFAOYSA-N 1-iodopentane Chemical compound CCCCCI BLXSFCHWMBESKV-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical class [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- RDHPKYGYEGBMSE-UHFFFAOYSA-N bromoethane Chemical compound CCBr RDHPKYGYEGBMSE-UHFFFAOYSA-N 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 108010057108 condensin complexes Proteins 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- INQOMBQAUSQDDS-UHFFFAOYSA-N iodomethane Chemical compound IC INQOMBQAUSQDDS-UHFFFAOYSA-N 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 125000000740 n-pentyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F7/00—Compounds containing elements of Groups 4 or 14 of the Periodic Table
- C07F7/24—Lead compounds
Definitions
- This invention relates to modes of producing lead tetra alkyls, and, more particu- -larly, lead tetraethyl, and its principal objects are to promote an intimate relation between the substances employed and to electrically reduce the reaction mass.
- Fig. 1 is a plan View of an apparatus adapted to carry out my process
- Fig. 2 is a sectional View thereof, taken substantially on the line 2 2 of Fig. 1.
- FIG. 10 is a tank containing a porous cup 11 made of clay or other material, which divides the interior of the tank into an inner chamber 12 Within the cup and an outer chamberl between the cup and the tank walls.
- a series of graphite anodes 14, (shown herein as six in number) are held in vertical positions in. the outer chamber 13 by a tank cover 15 through which the anodes project.
- the outer ends of the anodes are connected in an electrical circuit by a wire 16.u
- the porous cup 11 has a cover 17 of nonconducting material, for example, hard rubits periphery by asphalt 18.
- the cathode may be formed of spongy lead to promote'a reaction between the llead andthe catholyte.
- V23 is a thermometer, and 24 a reflux condenser having a condensin chamber 25 communicating with the insi e of cup 11, and a cooling chamber26 having connections for circulating a cooling medium about the condensing chamber 25.
- the cell may be placed in a cooling bath 32 for maintainin the temperature of the catholyte vbelow t e boiling pointof the alkyl halide.
- the chamber 12 within thecup is partially filled with a catholyte comprising, b Weight, 90 parts of commercial ethyl alcoho 10 partsof NaOH and 10 parts of ethyl iodide, and the chamber 18 around the cup is partially filled with an anolyte comprising l() parts of NaOH and 90 parts of alcohol.
- a lead compound such as lead acetate, may be dissolved in the catholyte to promote a reaction with the lead, preferably by the formation of spongy lead at the cathode.
- f 2 parts of lead acetate may be used in the catholyte given above.
- the current is turned on, a current density of about 1.15 amperes per din2 being preerred.
- the current heats the reaction mass, and forms hydrogen.
- the temperature of the reaction mass given above is preferably maintained at about 55 C., which temperature is below the boiling point of ethyl iodide, but high enough to maintain a relatively high rate of reaction in the cell.
- vreflux apparatus condenses and returns to the cup the ethyl iodide which vaporizes during the reaction. Apparently the hydrogen formed at the cathode reduces the reaction mass, forming lead di-ethyl, which is unstable .at the temperature of the catholyte, and breaks up thermally into lead and lead tetraethyl. The lead tends to settle to the bottom of the cup.
- the alcohol and ethyl iodide are distilled overby heating the catholyte to a temperature below about 98 C., the heavier lead tetraethyl is then .steamed distilled out, preferably by passing steam into the lead tetraethyl, and collected in another vessel, and the caustic which remains in the cell may be recovered.
- composition of the reaction mass may be varied by using in place of ethyl iodide, other alkyl halides, for example, methyl iodide, amyl iodide, and methyl, amyl or ethyl bromide, and by employing other substances than ethyl alcohol as a solvent for the alkyl i v solved in ethyl alcohol.
- ethyl iodide other alkyl halides, for example, methyl iodide, amyl iodide, and methyl, amyl or ethyl bromide
- the process of producing a lead alkyl which comprises dissolving an alkyl halide in an alcoholic electrolyte, placing a lead cathode in the electrolyte, and passing' an electric current through the cathode and the electrolyte.
- alkyl halide is an ethyl halide and lead tetraethyl is formed.
- the process of producing lead tetraethyl, Wh-ich comprises forming a catholyte of NaOH, an ethyl halide and ethyl alcohol; and passing an electric current through a lead cathode in contact Withthe catholyte. 18.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Y May 26, 1925.
G. H. F. CALINGAERT METHOD FOR PRODUCING LEAD COMPOUNDS Flled JulV 2, 1925 ber, sealed alon Patented May 26, 1925.
UNITED STATES PATENT OFFICE.
l(1`r1lOlRGr1il4 H. F. CALINGAERT, 0F WATERTOWN, MASSACHUSETTS, ASSIGNOR, BY MESNE ASSIGNMENTS, TO GENERAL MOTORS CORPORATION, OF DETRO'IT, MICHIGAN, A
CORPORATION OF DELAWARE.
METHOD FOR PROD'UOING LEAD COMPOUNDS.
Application filed July 2,
To all whom i# may coa-cern:
Be it known that I, GEORGE H. F. GALIN- GAERT, asubject of the King of the Belgians, residing at Watertown, in the county of Middlesex, Massachusetts, have invented certain new and useful Improvements in Methods for Producing Lead Compounds, of which the following is a full, clear, and exact description.
This invention relates to modes of producing lead tetra alkyls, and, more particu- -larly, lead tetraethyl, and its principal objects are to promote an intimate relation between the substances employed and to electrically reduce the reaction mass.
In the accompanying drawings:
Fig. 1 is a plan View of an apparatus adapted to carry out my process; and
Fig. 2 is a sectional View thereof, taken substantially on the line 2 2 of Fig. 1.
In these drawings 10 is a tank containing a porous cup 11 made of clay or other material, which divides the interior of the tank into an inner chamber 12 Within the cup and an outer chamberl between the cup and the tank walls. A series of graphite anodes 14, (shown herein as six in number) are held in vertical positions in. the outer chamber 13 by a tank cover 15 through which the anodes project. lThe outer ends of the anodes are connected in an electrical circuit by a wire 16.u
The porous cup 11 has a cover 17 of nonconducting material, for example, hard rubits periphery by asphalt 18. Metal ferru es 19, with rubber attachments, seated in the cover 17 support leads 20` which are attachedat their inner ends outer ends'to a wire 22 connected in the electrical circuit with wire 16. The cathode may be formed of spongy lead to promote'a reaction between the llead andthe catholyte.
V23 is a thermometer, and 24 a reflux condenser having a condensin chamber 25 communicating with the insi e of cup 11, and a cooling chamber26 having connections for circulating a cooling medium about the condensing chamber 25.
1923. serial No. 648,872.
The cell may be placed in a cooling bath 32 for maintainin the temperature of the catholyte vbelow t e boiling pointof the alkyl halide.
The chamber 12 within thecup is partially filled with a catholyte comprising, b Weight, 90 parts of commercial ethyl alcoho 10 partsof NaOH and 10 parts of ethyl iodide, and the chamber 18 around the cup is partially filled with an anolyte comprising l() parts of NaOH and 90 parts of alcohol. If desired, a lead compound, such as lead acetate, may be dissolved in the catholyte to promote a reaction with the lead, preferably by the formation of spongy lead at the cathode. f 2 parts of lead acetate may be used in the catholyte given above.
The current is turned on, a current density of about 1.15 amperes per din2 being preerred. The current heats the reaction mass, and forms hydrogen. The temperature of the reaction mass given above is preferably maintained at about 55 C., which temperature is below the boiling point of ethyl iodide, but high enough to maintain a relatively high rate of reaction in the cell. The
vreflux apparatus condenses and returns to the cup the ethyl iodide which vaporizes during the reaction. Apparently the hydrogen formed at the cathode reduces the reaction mass, forming lead di-ethyl, which is unstable .at the temperature of the catholyte, and breaks up thermally into lead and lead tetraethyl. The lead tends to settle to the bottom of the cup.
When the reaction is completed, the alcohol and ethyl iodide are distilled overby heating the catholyte to a temperature below about 98 C., the heavier lead tetraethyl is then .steamed distilled out, preferably by passing steam into the lead tetraethyl, and collected in another vessel, and the caustic which remains in the cell may be recovered.
The composition of the reaction mass. may be varied by using in place of ethyl iodide, other alkyl halides, for example, methyl iodide, amyl iodide, and methyl, amyl or ethyl bromide, and by employing other substances than ethyl alcohol as a solvent for the alkyl i v solved in ethyl alcohol.
halide and the NaOH or its equivalents, such as KOI-I.
Slight alkalinity of the electrolyte promotes the reaction and avoids acidity whichK is detrimental to the reaction.
I claim: Y
1. The process of producing a lead alkyl, which comprises forming a solution of an alkyl halide and an alkali, and reducing the reaction mass thus formed in contact With lead.
2. A process as set forth in claim l in Which the temperature of the reaction mass s maintained slightly below the boiling point of the alkyl halide.
3. A process' as set forth Vin claim 1 in which the alkyl halide is an ethyl halide and lead tetraethyl is formed.
4. A process as set forth in claim 1 in which the alkyl halide is an alkyl iodide.
5. A process as set forth in claiml in which the alkyl halide is ethyl iodide and lead tetraethyl is formed.
6. A process as set forth in claim 1, in which the alkyl halide and alkali are dis- 7. The process of producing a lead alkyl, which comprises dissolving an alkyl halide in an alcoholic electrolyte, placing a lead cathode in the electrolyte, and passing' an electric current through the cathode and the electrolyte.
8. A process as set forth in claim 7, in which the solution is alkaline.
9. A process as set forth in claim 7, in
which an `alkali and a lead compound are a' added to the solution.
10. A process as set forth in claim 7, in which NaOH and lead acetate are added to the solution.
11. The process of 'producingA a lead alkyl, which com rises forming a' catholyte comprising Na H and an alkyl halide dissolved in ethyl alcohol, placing a lead cathode in the catholyte, and passing an electric current throughthe cathode and catholyte.
^ 12. A process as set forth in claim 1l, in which the temperature of the catholyte is maintained below the boiling pointv of the alkyl halide.
13. A process as set forth in claim 11, in which the alkyl halide is an ethyl halide and lead tetraethyl is formed.
14. A process as set forth in claim 11, in Which the alkyl halide is an alkyl iodide.
15. A process as set forth in claim 11, in -f which the alkyl halide is ethyl iodide and lead tetraethyl is formed.
16. A process as set forth in claim 11, in Which lead acetate is added to the catholyte.
17. The process of producing lead tetraethyl, Wh-ich comprises forming a catholyte of NaOH, an ethyl halide and ethyl alcohol; and passing an electric current through a lead cathode in contact Withthe catholyte. 18. A process as set forth in claim 17, in which lead acetate is added to the catholyte. In testimony whereof4 I hereto allix my signature.
GEORGE I-I. F. CALINGAERT.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US648872A US1539297A (en) | 1923-07-02 | 1923-07-02 | Method for producing lead compounds |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US648872A US1539297A (en) | 1923-07-02 | 1923-07-02 | Method for producing lead compounds |
Publications (1)
Publication Number | Publication Date |
---|---|
US1539297A true US1539297A (en) | 1925-05-26 |
Family
ID=24602570
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US648872A Expired - Lifetime US1539297A (en) | 1923-07-02 | 1923-07-02 | Method for producing lead compounds |
Country Status (1)
Country | Link |
---|---|
US (1) | US1539297A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2535395A (en) * | 1947-11-04 | 1950-12-26 | Dinsley Alfred | Electrophoretic apparatus for research |
US3197392A (en) * | 1961-11-30 | 1965-07-27 | Du Pont | Process for preparing organometal compounds |
US3392093A (en) * | 1964-06-23 | 1968-07-09 | Du Pont | Electrolytic process for producing tetraalkyl lead compounds |
US4077862A (en) * | 1976-01-23 | 1978-03-07 | Okazaki Manufacturing Company Limited | Device for regulating drinking water |
-
1923
- 1923-07-02 US US648872A patent/US1539297A/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2535395A (en) * | 1947-11-04 | 1950-12-26 | Dinsley Alfred | Electrophoretic apparatus for research |
US3197392A (en) * | 1961-11-30 | 1965-07-27 | Du Pont | Process for preparing organometal compounds |
US3392093A (en) * | 1964-06-23 | 1968-07-09 | Du Pont | Electrolytic process for producing tetraalkyl lead compounds |
US4077862A (en) * | 1976-01-23 | 1978-03-07 | Okazaki Manufacturing Company Limited | Device for regulating drinking water |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3155602A (en) | Preparation of organic lead compounds | |
US1539297A (en) | Method for producing lead compounds | |
US2363386A (en) | Electrolytic preparation of capillary-active quaternary ammonium hydroxides | |
US3193477A (en) | Electrolytic hydrodimerization process and extraction procedure | |
US3853735A (en) | Electrolytic apparatus for preparation of organometallic compounds | |
US1567159A (en) | Method for producing lead compounds | |
US1992310A (en) | Process for treating hydrocarbons | |
US1538390A (en) | Treatment of alkali-metal amalgams, especially for the production of alkali metals | |
US3254009A (en) | Production of metal alkyls | |
US1384499A (en) | Method of and apparatus for refining metals | |
US1882525A (en) | Process for the electrolytic production of metals of the alkalis or alkaline earths | |
US1225052A (en) | Process of treating organic compounds by electrolysis. | |
US801199A (en) | Process for the production of metals of the alkali group by electrolysis. | |
US959730A (en) | Process of treating electrolytic and similar solutions. | |
SU1235456A3 (en) | Method of producing cebacic acid | |
US2289189A (en) | Process of reducing sugars | |
US3335143A (en) | Perfluorotriethylenediamine | |
US3306836A (en) | Process for the electrolytic production of magnesium dialkyls and aluminium trialkyls | |
US2024242A (en) | Apparatus for producing anhydrous magnesium chloride | |
US777669A (en) | Process of producing salts of hydrosulfurous acid. | |
US1570212A (en) | Apparatus for the production of electrolytic iron | |
US3432409A (en) | Electrolytic process for making tetraalkylammonium polybromides | |
US2786022A (en) | Electrolytic production of acetylene carboxylic acid | |
US1275161A (en) | Process or electrolytically producing iron. | |
US3169913A (en) | Preparation of gem-dinitroparaffins by electrolysis |