GB1419155A - Electrolytic hydrodimerization process - Google Patents

Electrolytic hydrodimerization process

Info

Publication number
GB1419155A
GB1419155A GB4139073A GB4139073A GB1419155A GB 1419155 A GB1419155 A GB 1419155A GB 4139073 A GB4139073 A GB 4139073A GB 4139073 A GB4139073 A GB 4139073A GB 1419155 A GB1419155 A GB 1419155A
Authority
GB
United Kingdom
Prior art keywords
cathode
ammonium
coom
hydrogen
alkali metal
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
Application number
GB4139073A
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.)
Monsanto Co
Original Assignee
Monsanto 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
Application filed by Monsanto Co filed Critical Monsanto Co
Priority to US497808A priority Critical patent/US3898140A/en
Publication of GB1419155A publication Critical patent/GB1419155A/en
Expired legal-status Critical Current

Links

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
    • C25B3/20Processes
    • C25B3/29Coupling reactions
    • C25B3/295Coupling reactions hydrodimerisation

Abstract

1419155 Electrohydrodimerization process MONSANTO CO 3 Sept 1973 [5 Sept 1972 4 April 1973 6 Aug 1973] 41390/73 Heading C2C [Also in Division C7] A process for hydrodimerizing an olefinic compound (such as acrylonitrile) having the formula R 2 C = CRX wherein -X is -CN, -CONR 2 or -COOR<SP>1</SP>, R is H or R<SP>1</SP>, and R<SP>1</SP> is C 1 -C 4 alkyl, comprises electrolysing an aqueous solution having dissolved therein (a) at least 0À1% by weight of the olefinic compound, (b) at least 10<SP>-5</SP> g. mol./l. of quaternary ammonium cations and (c) at least 0À1% by weight of conductive salt in contact with a cathodic surface, there being included in the solution in a concentration sufficient to inhibit (i.e. lower) formation of hydrogen at the cathodic surface, (d) at least one nitrilocarboxylic acid compound having the formula Y 2 N(ZÀYNÀ) n (CH 2 ) m COOM wherein Y is hydrogen, -(CH 2 ) m COOM, -(CH 2 ) m+1 OH or C 1 -C 20 alkyl, Z is a divalent C 2 -C 6 hydrocarbon radical, M is hydrogen, alkali metal or ammonium, m is 1 or 2, n is 0, 1, 2, 3 or 4 and at least one Y is -(CH 2 ) m COOM or -(CH 2 ) m+1 OH, "Quaternary ammonium" includes piperidiniums, pyrrolidiniums and morpholiniums. The conductive salt may itself be a quarternary ammonium salt or may be an alkali metal salt. Specified salts are phosphates, borates, perchlorates, carbonates and sulphates; particularly incompletely substituted salts such as Na 2 HPO 4 and K 2 HBO 3 , and alkali metal and ammonium salts of condensed acids of P and B. Electrolysis may be in a single compartment or diaphragm cell. Specified conditions are: a pH of 2-12; a temperature from the freezing point to 75‹ C. and above; pressures at or above atmospheric; solution flow adjacent the cathode of at least 1 ft./sec.; an anode cathode gap of 40 mils or less to ¢ inch or more; a cathode comprising Cd, Hg, Tl, Pb, Zn, Mn, Sn or graphite; an anode comprising Pt, Ru, Ni, Pb, PbO 2 , C steel, alloy steel Fe or magnetite; and the aqueous solution of the electrolysis medium may also contain a dispersed but undissolved organic phase. In all the examples, acrylonitrile is electrolytically hydrodimerized in undivided cells to form adiponitrile. The aqueous solution contains ethyl tributyl ammonium cations, incompletely substituted sodium orthophosphates, (borates in Examples IV, VII and VIII), and tetrasodium ethylenediamine tetracetate. The anodes are of carbon steel and the cathodes are of Cd except for Example VI where the cathode is Pb.
GB4139073A 1972-09-05 1973-09-03 Electrolytic hydrodimerization process Expired GB1419155A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US497808A US3898140A (en) 1973-08-06 1974-08-15 Electrolytic hydrodimerization process improvement

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US28597572A 1972-09-05 1972-09-05
US34794873A 1973-04-04 1973-04-04
US38576773A 1973-08-06 1973-08-06

Publications (1)

Publication Number Publication Date
GB1419155A true GB1419155A (en) 1975-12-24

Family

ID=27403578

Family Applications (1)

Application Number Title Priority Date Filing Date
GB4139073A Expired GB1419155A (en) 1972-09-05 1973-09-03 Electrolytic hydrodimerization process

Country Status (7)

Country Link
JP (1) JPS5742710B2 (en)
CA (1) CA1039231A (en)
FR (1) FR2197841B1 (en)
GB (1) GB1419155A (en)
IE (1) IE38319B1 (en)
IT (1) IT998529B (en)
NL (1) NL7312112A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4046651A (en) * 1975-07-28 1977-09-06 Monsanto Company Electrolytic hydrodimerization process improvement

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2424587C3 (en) * 1974-05-21 1980-03-20 Eisenwerk-Gesellschaft Maximilianshuette Mbh, 8458 Sulzbach-Rosenberg Rolling device

Also Published As

Publication number Publication date
IT998529B (en) 1976-02-20
NL7312112A (en) 1974-03-07
FR2197841A1 (en) 1974-03-29
IE38319L (en) 1974-03-05
DE2344294A1 (en) 1974-03-21
FR2197841B1 (en) 1980-01-18
JPS4992021A (en) 1974-09-03
DE2344294B2 (en) 1976-09-16
CA1039231A (en) 1978-09-26
IE38319B1 (en) 1978-02-15
JPS5742710B2 (en) 1982-09-10

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PE20 Patent expired after termination of 20 years

Effective date: 19930902