PAPER
Enhancement of cyclic ether formation from polyalcohol compounds
in high temperature liquid water by high pressure carbon dioxide
Aritomo Yamaguchi, Norihito Hiyoshi, Osamu Sato, Kyoko K. Bando and Masayuki Shirai*
Received 24th July 2008, Accepted 10th October 2008
First published as an Advance Article on the web 7th November 2008
DOI: 10.1039/b812318g
Cyclic ethers were produced by a dehydration reaction of polyalcohol compounds in high
temperature liquid water, which was accelerated by the presence of carbon dioxide dissolved in the
water. 3-hydroxytetrahydrofuran was produced by the dehydration of 1,2,4-butanetriol. Both
tetrahydrofurfuryl alcohol and 3-hydroxytetrahydropyran were produced by the dehydration of
1,2,5-pentanetriol. Five-membered cyclic ethers were formed faster than six-membered cyclic
ethers and the formation rates of the cyclic ethers depended strongly on the structure of the
polyalcohol compounds. The position of the hydroxyl groups is crucial for the efficient
intramolecular dehydration.
this manuscript, we investigated the dehydration mechanism of
Introduction
polyalcohol compounds having two or three hydroxyl groups,
Biomass has a large amount of oxygen atoms because plants
as simple model compounds of biomass-derived carbohydrates,
combine carbon dioxide with water using solar energy to store
to corresponding five- or six-membered cyclic ethers in water
oxygen as sugar building blocks, (CH2O)n. The selective removal
under high pressure carbon dioxide at 573 K.
of oxygen atoms from biomass-derived carbohydrates, which
are polyalcohol compounds like fructose, sorbitol, and glycerol
in most cases, by dehydration or hydrogenolysis is important
Experimental
to obtain valuable products with desired boiling points, water
solubilities, octane numbers and viscosities.1 The chemistry of
intramolecular dehydration of polyalcohol compounds provides
a key technology for developing an efficient conversion process
of biomass derivatives to useful materials;2 however, biomass-
derived carbohydrates, such as fructose and sorbitol, have five
or six hydroxyl groups in a molecule and their intramolecular
dehydration mechanisms are complicated.
High temperature liquid water has attracted much attention
as an alternative to harmful organic solvents because of its
high proton concentration, which enhances the rates of acid-
catalyzed reactions, such as dehydration in water, without
adding any hazardous acid.3,4 Cyclic ethers are essential ma-
terials for the chemical industry and they are produced from
diols by intramolecular dehydration over strong mineral acids,
aluminium silicates, and ion-exchange resins.5 Savage’s group
reported that the addition of carbon dioxide to water (473–
623 K) enhanced the production of tetrahydrofuran (THF) from
1,4-butanediol (1,4-BDO).6–8 The added carbon dioxide was
dissolved in water to form carbonic acid, accelerating the acid
catalysis of high temperature water. An acid solvent composed
of water and carbon dioxide is environmentally-benign not
only because both water and carbon dioxide are non-toxic,
but also separation and recycling of these two components
are easily performed by depressurization after reaction. In
1,2,4-Butanetriol (1,2,4-BTO, Wako Pure Chemical Industries),
1,2,5-pentanetriol (1,2,5-PTO, Tokyo Chemical Industry), 1,4-
butanediol (1,4-BDO, Wako Pure Chemical Industries), 1,4-
pentanediol (1,4-PDO, Aldrich) and 1,5-pentanediol (1,5-PDO,
Wako Pure Chemical Industries) were purchased and used
without any further purification.
The dehydration of polyalcohol compounds was carried out
in a batch reactor (inner volume: 6 cm3) made of a SUS316
tube.9 After 3 cm3 of polyalcohol aqueous solution (1.0 and
0.3 mol dm-3) was loaded in the reactor, the gas phase was
purged with argon gas to remove air. Carbon dioxide (10 and
15 MPa) was then loaded in the reactor at 323 K.10 The reactor
was submerged into a molten-salt bath at 573 K for a given
reaction time and then submerged into a water bath for cooling
to ambient temperature quickly after the reaction. The water
in the reactor maintained vapor-liquid equilibrium at 573 K
under 8.6 MPa of partial pressure. The partial pressure of carbon
dioxide at 573 K was estimated to be 17.7 and 26.6 MPa, based
on the equation of Charles’s law, corresponding to the initial
pressure of 10 and 15 MPa at 323 K, respectively. A mixture of
a reactant and liquid products was taken out from the reactor
with distilled water.
The quantitative analysis of liquid products was conducted
by gas chromatography with a flame ionization detector (GC-
FID) equipped with a DB-WAX capillary column (Agilent Tech-
nologies) using 1-propanol (Wako Pure Chemical Industries)
as an internal standard material. The products were identified
by their retention times of the GC-FID analysis, compared
with those for known materials; 3-hydroxytetrahydrofuran
(3-HTHF, Wako Pure Chemical Industries), tetrahydrofur-
Research Center for Compact Chemical Process, National Institute of
Advanced Industrial Science and Technology (AIST), 4-2-1 Nigatake,
Miyagino, Sendai, 983-8551, Japan. E-mail: m.shirai@aist.go.jp;
Fax: +81 22 237 5224; Tel: +81 22 237 5219
48 | Green Chem., 2009, 11, 48–52
This journal is
The Royal Society of Chemistry 2009
©