US3007857A - Preparation of organic lead compounds - Google Patents

Preparation of organic lead compounds Download PDF

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Publication number
US3007857A
US3007857A US675260A US67526057A US3007857A US 3007857 A US3007857 A US 3007857A US 675260 A US675260 A US 675260A US 67526057 A US67526057 A US 67526057A US 3007857 A US3007857 A US 3007857A
Authority
US
United States
Prior art keywords
lead
anode
grignard reagent
organic
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
Application number
US675260A
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English (en)
Inventor
David G Braithwaite
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ChampionX LLC
Original Assignee
Nalco Chemical Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority to BE569921D priority Critical patent/BE569921A/xx
Application filed by Nalco Chemical Co filed Critical Nalco Chemical Co
Priority to US675260A priority patent/US3007857A/en
Priority to GB24186/58A priority patent/GB839172A/en
Priority to DEN15419A priority patent/DE1164406B/de
Priority to FR1201049D priority patent/FR1201049A/fr
Application granted granted Critical
Publication of US3007857A publication Critical patent/US3007857A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B3/00Electrolytic production of organic compounds
    • C25B3/01Products
    • C25B3/13Organo-metallic compounds

Definitions

  • This invention relates to the preparation of organic lead compounds, and more particularly to a. new and improved process for making tetraethyl lead.
  • Equation A represents one of the early synthesis processes which is no longer being used commercially.
  • Equation B represents a current commercial process.
  • One of the objects of the present invention is to provide a new and improved process for producing organic lead compounds and especially tetraethyl'lead.
  • Another object of the invention is to provide a process for producing organic lead compounds in relatively high yields. Other objects will appear hereinafter.
  • organic lead compounds can be produced by electrolyzing a Grignard reagent in an organic solvent for the Grignard reagent using a lead anode and a cathode which may be either lead, platinum or another conducting material.
  • a lead anode and a cathode which may be either lead, platinum or another conducting material.
  • the free hydrocarbon radicals derived from the Grignard reagent combine with the lead of the anode to form the corresponding organic metallo compound.
  • the process may be described, therefore, as a sacrificial anode process.
  • tetraethyl lead is produced by electrolyzing ethyl magnesium bromide dissolved in diethylether between two lead electrodes, the one forming the anode and the other the cathode.
  • the cathode may be formed of platinum or another conducting material of the type usually used as an electrode.
  • magnesium is deposited at the cathode and the free ethyl radicals which are liberated at the anode combine with the lead of the anode forming tetraethyl lead which dissolves in the diethylether and can be separated therefrom by distillation.
  • spacers between the anode and the cathode are used in order to segregate the magnesium at the cathode from the organic lead compounds formed at the anode. If no spacers are used the electrodes should be far enough apart so that the magnesium formed at the cathode does not bridge over to the anode.
  • circulation of the solvent medium at the cathode is used to remove the magnesium which is filtered and reutilized for the formation of additional quantities of Grignard reagent.
  • the invention has been operated over a wide range of current densities and at varying voltages.
  • the spacing and size of the electrodes will determine the current density.
  • the temperature used during the process is normally the boiling temperature of the sol- 2; vent.
  • the process can be carried out at varying temperatures and higher boiling solvents such as tetrahydrofuran have been successfully used.
  • the invention is not limited to any particular solvent except that the solvent must be relatively inert under the conditions of the process.
  • the solvents used are normally organic liquids which have dielectric properties but have sufficient conductivity to permit passage of'the current between the anode and the cathode.
  • organic lead compounds such as tetraethyl lead are soluble therein.
  • the process can be carried out with solvents for the Grignard reagent in which the organic lead compound is insoluble
  • solvents for the Grignard reagent in which the organic lead compound is insoluble
  • Other liquidalkyl' ethers such as dimethylether, diisopropylether and homologues thereof, including the polyoxyalkylene diethers can be employed as solvents ('e.g'., diethers of polyoxyethylene glycol's and diethers of poly oxypropylene glycols).
  • the solvents used are'preferably anhydrous or substantially anhydrous.
  • Example I Ethyl magnesium bromide was dissolved, in diethyle ether to produce a .67 N solution. Leadelectrodes which were 2 inches in diameter were placed in said solution spaced 1% inches apart and a direct current 05 300volts was applied at a current of 100 milliarnperes. The app a u s q ipped with a re l x ondenser to turn to thesolution any solvent which evaporated as a result of the boiling of the reaction mixture. Tetraethyllead was formed and the anode was completely used upl in the reaction. The normality of the solution was. reduced to 3 N-q i Example II 1400 cc.
  • Example II Since the procedure of Example II was carried out at a conductance of approximately 0.5 of an ampere employing 100 volts and the procedure of Example I was carried out at a higher voltage and a lower amperage, it can be concluded that the current density can be varied rather widely.
  • the pressures used can also be varied and may be subatmospheric, atmospheric, or superatmospheric.
  • the pressures used are normally sufficient to maintain the liquid phase with the particular solvent and temperature conditions employed.
  • phenyl magnesium bromide or mixtures of phenyl and ethyl magnesium bromide can be electrolyzed to produce organic lead compounds containing the phenyl radical or both phenyl and organic radicals or both phenyl and other alkyl radicals in case a higher alkyl magnesium bromide issubstituted for ethyl magnesium bromide.
  • the invention makes it possible to prepare organic lead compounds and especially substances such as tetraethyl lead by a very simple procedure in which free lead is not a by-product of the reaction.
  • the process of the invention also makes it possible to produce organic lead compounds including tetraethyl lead in relatively high yields.
  • a process for preparing organic lead compounds which comprises electrolyzing, using a lead anode, a substantially anhydrous solution of a Grignard reagent in a substantially inert organic solvent for said Grignard reagent employing an electrolyzing current effective to cause said lead anode to dissolve in said solution of said Grignard reagent in said organic solvent, said current being a minimum of 100 milliamperes, and recovering from the resultant product an organic lead compound consisting. of hydrocarbon radicals linked directly to metallic lead.
  • a process for preparing tetraethyl lead which comprises electrolyzing, usinga lead anode, a substantially anhydrous solution of ethyl magnesium bromide in a substantially inert organic solvent for said ethyl magnesium bromide employing an electrolyzing current effective to cause said lead anode to dissolve in said solution of said Grignard reagent in said organic solvent, said current being a minimum of 100 milliamperes, and recovering tetraethyl lead from the resultant solution.
  • Aprocess for preparing tetraethyl lead which comprises electrolyzing, using a lead anode, a substantially anhydrous solution of ethyl magnesium bromide in diethylether employing an electrolyzing current efiective to cause said leadanode to dissolve in said solution of said Grignard reagent in said organic solvent, said current being a minimum of 100 milliamperes, and recovering tetraethyl lead from the resultant solution.
  • a process for preparing tetraethyl lead which cornpnises electrolyzing, using a lead anode, a substantially anhydrous solution of ethyl magnesium bromide in tetrahydrofuran employing an electrolyzing current elfective to cause said lead anode to dissolve in said solution of said Grignard reagent in said organic solvent, said current being a minimum of milliamperes, and recovering tetraethyl lead from the resultant solution.
  • a process for preparing organic lead compounds which comprises electrolyzing between electrodes, one of which is a lead anode, a substantially anhydrous solution of a Grignard reagent in a substantially inert organic solvent for said Grignard reagent employing an electrolyzing current effective to cause said lead anode to dissolve in said solution of said Grignard reagent in said organic solvent, said current being a minimum of 100 milliamperes, the said electrodes being separated from each other in such a manner that the magnesium formed at the cathode does not bridge over to the anode, and recovering from the resultant product an organic lead compound consisting of hydrocarbon radicals linked directly to metallic lead.
  • a process .for preparing organic lead compounds which comprises electrolyzing, using a lead anode, an anhydrous solution of a Grignard reagent in tetrahydrofuran employing an electrolyzing current eifectiveto cause said lead anode to dissolve in said solution of said Grignard reagent in tetrahydrofuran, said current being a minimum of 100 milliamperes, said Grignard reagent being an ethyl magnesium halide, and recovering tetraethyl lead from the resultant solution.

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  • 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 Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
US675260A 1957-07-31 1957-07-31 Preparation of organic lead compounds Expired - Lifetime US3007857A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
BE569921D BE569921A (US07176317-20070213-C00004.png) 1957-07-31
US675260A US3007857A (en) 1957-07-31 1957-07-31 Preparation of organic lead compounds
GB24186/58A GB839172A (en) 1957-07-31 1958-07-28 Preparation of organic lead compounds
DEN15419A DE1164406B (de) 1957-07-31 1958-07-30 Verfahren zur elektrolytischen Herstellung von Alkyl- oder Arylbleiverbindungen
FR1201049D FR1201049A (fr) 1957-07-31 1958-07-31 Procédé de préparation de composés organiques du plomb

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US675260A US3007857A (en) 1957-07-31 1957-07-31 Preparation of organic lead compounds

Publications (1)

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US3007857A true US3007857A (en) 1961-11-07

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US675260A Expired - Lifetime US3007857A (en) 1957-07-31 1957-07-31 Preparation of organic lead compounds

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US (1) US3007857A (US07176317-20070213-C00004.png)
BE (1) BE569921A (US07176317-20070213-C00004.png)
DE (1) DE1164406B (US07176317-20070213-C00004.png)
FR (1) FR1201049A (US07176317-20070213-C00004.png)
GB (1) GB839172A (US07176317-20070213-C00004.png)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3155602A (en) * 1960-03-15 1964-11-03 Standard Oil Co Preparation of organic lead compounds
US3180810A (en) * 1961-07-31 1965-04-27 Standard Oil Co Electrolytic cell and method of operation
US3197392A (en) * 1961-11-30 1965-07-27 Du Pont Process for preparing organometal compounds
US3234112A (en) * 1961-03-21 1966-02-08 Nalco Chemical Co Process of producing organic lead compounds
US3391066A (en) * 1959-05-06 1968-07-02 Nalco Chemical Co Preparation of organic compounds of metals
US3391067A (en) * 1959-05-06 1968-07-02 Nalco Chemical Co Electrolytic process for the preparation of mixed organic lead compounds and electrolyte therefor

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3100181A (en) * 1961-02-16 1963-08-06 Nalco Chemical Co Preparation of organoboranes
US3079311A (en) * 1961-02-20 1963-02-26 Nalco Chemical Co Method of preparing tertiary phosphines
DE1216303B (de) * 1963-09-24 1966-05-12 Nalco Chemical Co Elektrolyt fuer die Herstellung von Bleialkylverbindungen
DE1226100B (de) * 1963-09-24 1966-10-06 Halco Chem Co Verfahren zur Herstellung von Bleitetraalkylen

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE534128A (US07176317-20070213-C00004.png) * 1954-12-15
US2849349A (en) * 1955-06-13 1958-08-26 Ziegler Process for the electrolytic deposition of aluminium

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL101542C (US07176317-20070213-C00004.png) * 1954-11-26
US2944948A (en) * 1956-02-06 1960-07-12 Ethyl Corp Method of purifying organometallic complexes and their use in the preparation of organolead compounds

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE534128A (US07176317-20070213-C00004.png) * 1954-12-15
US2849349A (en) * 1955-06-13 1958-08-26 Ziegler Process for the electrolytic deposition of aluminium

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3391066A (en) * 1959-05-06 1968-07-02 Nalco Chemical Co Preparation of organic compounds of metals
US3391067A (en) * 1959-05-06 1968-07-02 Nalco Chemical Co Electrolytic process for the preparation of mixed organic lead compounds and electrolyte therefor
US3155602A (en) * 1960-03-15 1964-11-03 Standard Oil Co Preparation of organic lead compounds
US3298939A (en) * 1960-03-15 1967-01-17 Standard Oil Co Electrolytic preparation of organolead compounds
US3234112A (en) * 1961-03-21 1966-02-08 Nalco Chemical Co Process of producing organic lead compounds
US3180810A (en) * 1961-07-31 1965-04-27 Standard Oil Co Electrolytic cell and method of operation
US3197392A (en) * 1961-11-30 1965-07-27 Du Pont Process for preparing organometal compounds

Also Published As

Publication number Publication date
BE569921A (US07176317-20070213-C00004.png)
GB839172A (en) 1960-06-29
DE1164406B (de) 1964-03-05
FR1201049A (fr) 1959-12-28

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