IE38319L - Electrolytic hydrodimerization - Google Patents

Electrolytic hydrodimerization

Info

Publication number
IE38319L
IE38319L IE731563A IE156373A IE38319L IE 38319 L IE38319 L IE 38319L IE 731563 A IE731563 A IE 731563A IE 156373 A IE156373 A IE 156373A IE 38319 L IE38319 L IE 38319L
Authority
IE
Ireland
Prior art keywords
cathode
ammonium
coom
hydrogen
alkali metal
Prior art date
Application number
IE731563A
Other versions
IE38319B1 (en
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
Publication of IE38319L publication Critical patent/IE38319L/en
Publication of IE38319B1 publication Critical patent/IE38319B1/en

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

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 Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

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. [GB1419155A]
IE1563/73A 1972-09-05 1973-09-03 Electrolytic hydrodimerization process IE38319B1 (en)

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 (2)

Publication Number Publication Date
IE38319L true IE38319L (en) 1974-03-05
IE38319B1 IE38319B1 (en) 1978-02-15

Family

ID=27403578

Family Applications (1)

Application Number Title Priority Date Filing Date
IE1563/73A IE38319B1 (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
JPS5742710B2 (en) 1982-09-10
IE38319B1 (en) 1978-02-15
GB1419155A (en) 1975-12-24
DE2344294B2 (en) 1976-09-16
DE2344294A1 (en) 1974-03-21
NL7312112A (en) 1974-03-07
CA1039231A (en) 1978-09-26
FR2197841A1 (en) 1974-03-29
FR2197841B1 (en) 1980-01-18
JPS4992021A (en) 1974-09-03

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