3
08
Can. J. Chem. Vol. 78, 2000
4
electrolysis (4, 5). Catalytic hydrogenation has also been
studied as a method for production of phenolic monomers
(
(which are soluble in aqueous alkali) on Raney nickel and
palladium-based electrodes. It has been recognized that the
β-O-4 linkage (see 4 in Fig. 1) is the most important type of
structural element in native lignins. We therefore studied the
following models (see Fig. 1 for structures): (i) three com-
pounds having one β-O-4 linkage and referred to as phenolic
monoethers: 1-(4-hydroxy-3-methoxyphenyl)-2-(methoxyphenoxy)-
1-ethanol (1), its hydroxymethyl derivative 2, and its keto
derivative 3; (ii) phenolic diether 4 with two β-O-4 linkages;
(iii) 1-(3,4-dimethoxyphenyl)-2-(methoxyphenoxy)-1-ethanol (5),
a non-phenolic monoether (β-O-4 linkage); and (iv) 4-
phenoxyphenol (6), a model of 4-O-5 linkages in which two
aryl groups are directly bound to an oxygen atom. Raney
nickel has proven to be a versatile hydrogenation electro-
catalyst (13), and supported palladium was chosen in view
of its well known activity in catalytic hydrogenolysis (17).
6). A variety of catalysts have been used, including Raney
nickel (7), copper chromite (8), supported rhodium (9, 10),
ruthenium or palladium (11), and nickel boride . Interesting
5
compounds such as 4-n-propylguaiacol and dihydroconiferyl
alcohol have been generated from aspen wood using Raney
nickel (7) or supported rhodium (9, 10). With a palladium
catalyst, a high selectivity has been reported for the forma-
tion of dihydroconiferyl alcohol (11). The use of nickel
boride has led to the production of 4-ethylguaiacol and
4
-ethylsyringol from wood.5
In a recent article (12), we prepared basic nonphenolic
models of α-O-4 and β-O-4 bonds in lignins to demonstrate
the potential of electrocatalytic hydrogenation (ECH) as an
alternative method for lignin depolymerization. ECH is an
advantageous combination of electrochemical and catalytic
methods (for a review on ECH, see ref. 13). In ECH, chemi-
sorbed hydrogen (H)M is generated in situ on the
electrocatalyst surface by electroreduction of water at a low
overpotential (rxn. [1]) and reacts with the adsorbed organic
substrate (rxns. [2]–[4]). However, hydrogenation (rxns.
2]–[4]) competes with hydrogen desorption (rxns. [5] and
or) [6]) and this may decrease the current efficiency (13).
This method of generating chemisorbed hydrogen allows
one to carry out reactions similar to catalytic hydrogenation
but at lower temperatures and pressures (13). Furthermore,
the concentration of chemisorbed hydrogen can be con-
trolled by adjustment of the current density.
Experimental
Organic substrates and products
Phenolic monoethers 1 (18), 2 (19), 3 (18), and 5 (5) are
known compounds and were synthesized according to
published procedures. Phenolic diether 4 is also a known
compound and was prepared from O-isopropyl-α -bromo-
acetovanillone (prepared according to ref. 20) by described
procedures (18, 21). The following compounds (Fig. 2) were
obtained from commercial sources: 4-phenoxyphenol (6),
guaiacol (9), ethylphenol (10a), acetovanillone (11b), and
4′-hydroxypropiophenone (11c) from Aldrich; cyclohexanol
[
(
(
7) and phenol (8) from BDH; 4-ethylguaiacol (10b), 4-n-
–
–
[
1]
2 H O + 2 e + M → 2 (H)M + 2 OH
2
propylphenol (10c), and 4-n-propylguaiacol (10d) from
Lancaster; 4′-hydroxyacetophenone (11a) from Eastman.
The alcohols 12a, b (Fig. 2) were prepared by catalytic hy-
drogenation of the corresponding ketone using nickel-
aluminum alloy in 10% sodium hydroxide at 15°C (in situ
generation of Raney nickel and chemisorbed hydrogen) (22).
[
[
2]
3]
R + M
º
(R)M
(R)M + 2 (H)M º (RH )M
2
[
[
4]
5]
(RH )M º RH + M
1
13
2
2
All compounds had H NMR, C NMR, IR, and mass spec-
tral data in accordance with their structure.
–
–
(H)M + H O + e → H + M + OH
2
2
Electrodes and electrolyses
Raney nickel electrodes were made by mixing and grind-
ing 45% of Raney alloy (Fluka), 45% of fractal nickel pow-
[
6]
(H)M + (H) M º H + 2 M
2
ECH at electrodes made of Raney-type materials has been
applied successfully to the selective hydrogenation of many
types of molecules (13). In principle, all catalytic powders
used in catalytic hydrogenation can also be used in ECH,
provided that the catalyst can be immobilized on (or sup-
ported by) a conductive material or cast into a solid conduc-
tive piece. The simplest electrode set up is to spread the
catalytic powder onto a conductive plate, but such a design
is not fully satisfactory from a practical point of view. Sev-
eral approaches have been developed to prepare electrodes
from catalytic powders, including electromagnetic deposi-
tion (14), electrocodeposition (15), lanthanum phosphate
6
der (Inco Type 250), and 10% of lanthanum phosphate .
About 40 g of this powder was pressed into a plate 3mm
2
2
thick at about 1000 kg/cm into a 5 × 71/2 cm mould from
2
which 2 × 21/2 cm plates were cut. These plates were
heated at 800°C for 4 h under an argon atmosphere. The
electrical contact was made with a nickel stripe. The plates
were leached in NaOH 30% at 75°C for 24 h to remove alu-
minum. In order to eliminate the chemisorbed hydrogen
formed in the leaching process (reduction of water by alumi-
num), the Raney nickel plate was treated with a solution of
trans-cinnamic acid (5 g in 200 mL of 1 M NaOH) at room
temperature for at least 18 h (hydrogenation to phenyl-
propionic acid) prior to electrolysis.
6
polymerization, and embodiment in a reticulated vitreous
carbon support (16). The latter two methods have been used
in this work.
The palladium-based electrode consisted of a 2 × 2.5 ×
3
As an extension of our previous work (12), we report in
0.6 cm piece of 100 ppi reticulated vitreous carbon
this paper the results of the ECH of phenolic lignin models
(Electrosynthesis Co.) into which 0.20 g of catalyst
4
J.H.P. Utley and C.Z. Smith. U.S. Patent 4,786,382 (1988).
B. Loubinoux. French Patent 80 15272 (1980).
J.-M. Lalancette, E. Potvin, and H. Ménard. U.S. Patent 4,886,591 (1989).
5
6
©
2000 NRC Canada