S. Nagashima et al. / Applied Catalysis A: General 464–465 (2013) 332–338
333
practical method for the acylation of both aliphatic and aromatic
100
80
60
40
20
0
thiols with carboxylic acids or their esters over various solid acid
catalysts that are stable above 200 ◦C (Eq. (2)).
C6H5SH + CH3COOR
→ C6H5SR + C6H5SCOCH3 (R = CH3, C2H5, C3H7)
(1)
R1SH + R2COOR3 → R1SCOR2 + HOR3
(R1 = C5–C8alkyl, C6H5;R2 = C1–C4alkyl, C6H5;
R3 = H, C1–C3alkyl)
(2)
0
2
4
6
8
2. Experimental
t / h
Fig. 1. A typical reaction profile for the S-acetylation of benzenethiol with acetic
acid over (H3O)2[(Mo6Cl8)Cl6]·6H2O (2)/SiO2. Following the pretreatment of 2/SiO2
(30 mg) in a hydrogen stream (300 mL/h) at 300 ◦C for 1 h, reaction was initiated
by the introduction of a mixture of benzenethiol (102 L/h, 1.0 mmol/h) and acetic
acid (114 L/h, 2.0 mmol/h) to the hydrogen stream without changing the temper-
ature. Conversion (᭹), S-phenyl thioacetate (ꢀ), diphenyl sulfide (ꢁ), and diphenyl
disulfide (ꢀ).
Crystals
of
the
molecular
cluster
complexes
of
[(Nb6Cl12)Cl2(H2O)4]·4H2O (1) [7], (H3O)2[(Mo6Cl8)Cl6]·6H2O (2)
[8], [(Ta6Cl12)Cl2(H2O)4]·4H2O [7], and (H3O)2[(W6Cl8)Cl6]·6H2O
[9] were synthesized using the published procedures. The general
procedure for the preparation of a silica-supported catalyst is
described for 1. Methanol (330 mL) was added to a 1 L flask
containing 1 (1.0 g). After dissolution of the clusters, silica gel
(Nippon Aerosil, Tokyo; Aerosil 380 m2/g, 19.0 g) was added and
allowed to stand for 1 h with occasional shaking. Then, the solvent
was evaporated to dryness under reduced pressure at ambient
temperature. Samples of the dried silica gel were crushed and
screened to 166−200 mesh. All of the clusters were supported
on the silica gel in the same way at 5.0% by weight. No peaks
attributable to the cluster complexes were observed in XRD
pattern of the silica gel supported catalysts. The clusters were sup-
ported in well dispersed form. Crystalline heteropoly acids were
gifted from Nippon Inorganic Colour & Chemical Co., Ltd. (Tokyo):
phosphomolybdic acid H3[PMo12O40]·nH2O (n ≈ 30), phospho-
tungstic acid H3[PW12O40]·nH2O (n ≈ 30), and silicotungstic acid
H4[SiW12O40]·nH2O (n ≈ 24). They were crushed and screened to
166−200 mesh. The other chemicals were commercial products
and used as received: silica–alumina (high alumina), Catalysts &
Chemicals Ind. Co., Ltd. (JRC-SHA-1, Catalysis Society of Japan);
H-Y zeolite, Tosoh Corporation (JRC-Z-HY5.5, Catalysis Society of
Japan), H-beta, Sud-Chemie Catalysts Japan, Inc. (JRC-Z-HB25(1),
Catalysis Society of Japan); H-mordenite, Tosoh Corporation
(JRC-Z-HM20(4), Catalysis Society of Japan); active alumina, GL
Sciences Inc. (Tokyo).
six-way valve kept at 150 ◦C followed by analysis using an online
gas–liquid chromatograph (GLC) with a methyl silicone column.
The reactor effluent was collected in an ice trap containing tetrahy-
drofuran for subsequent analyses by GLC with a poly(ethylene
glycol) capillary column or a dimethylpolysiloxane capillary col-
umn and gas chromatography–mass spectrometry (GC–MS) with
a dimethylpolysiloxane capillary column. Catalytic reactions using
the other thiols, alkylating reagents, and catalysts were performed
in the same way. In this paper, conversion and selectivity are
defined as follows: conversion = products/(products + recovered
thiol) × 100 (%), and selectivity = product/(total amount of prod-
ucts) × 100 (%) based on thiol.
3. Results and discussion
3.1. S-Acetylation of benzenethiol with acetic acid
Some acetylating reagents were reacted with benzenethiol.
When a mixture of two equivalents of acetyl chloride with ben-
zenethiol was allowed to stand for 3 h under neat conditions at
ambient temperature in the absence of any catalyst, S-acetylation
proceeded almost quantitatively to yield S-phenyl thioacetate.
Under the same reaction conditions, acetic anhydride yielded S-
phenyl thioacetate exclusively with about 50% conversion. Similar
results have been reported [11]. However, acetic acid and methyl
acetate did not afford even a trace amount of the thioacetate
under the same reaction conditions. Harsh reaction conditions are
required for the S-acetylation with carboxylic acids and their esters.
We have reported that S-acetylation of benzenethiol with acetic
esters proceeded at 400 ◦C over halide cluster catalysts [6]. Then,
S-acetylation of benzenethiol with acetic acid was attempted at
elevated temperatures in the gas phase in the presence of halide
2.2. Catalytic measurements
The general procedure for the catalytic reaction is described
for the benzenethiol/acetic acid/1 system. A conventional ver-
tical glass fixed-bed microreactor with a continuous gas-flow
system was operated at atmospheric pressure [10]. In each exper-
iment, a weighed supported sample of 1/SiO2 (30.0 mg) was
packed in a borosilicate glass tube (3 mm i.d.) with the aid of
quartz glass and placed in the center of an electric furnace.
The supported cluster sample was initially heated from room
temperature to a fixed temperature between 50 and 500 ◦C in
15 min in a hydrogen stream (300 mL/h), and then it was held
at that temperature for 45 min for activation. Then, the reaction
was initiated by feeding a mixture of benzenethiol (102 L/h,
1.0 mmol/h) and acetic acid (114 L/h, 2.0 mmol/h) into the hydro-
gen stream without changing the temperature. The reaction was
monitored every 30 min by sampling the reaction gas (1 mL) with a
A
typical reaction profile of benzenethiol with acetic
acid in
a
hydrogen stream at 300 ◦C in the presence of
(H3O)2[(Mo6Cl8)Cl6]·6H2O (2)/SiO2 as catalyst is shown in
Fig. 1. The activity decreased with time, probably because of
fouling by carbonaceous compounds or coke. When 1/SiO2 was
reduced in the hydrogen stream for 1 h by stopping the sup-
ply of the reactants at 3 h after the start of the reaction, the