A green alternative to THF - Romil
A green alternative to THF - Romil
A green alternative to THF - Romil
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The solvent 2-methyl tetrahydrofuran<br />
(2-Me<strong>THF</strong>) can provide<br />
a cost-effective, <strong>green</strong><br />
<strong>alternative</strong> <strong>to</strong> tetrahydrofuran<br />
(<strong>THF</strong>) chemistry. 2-Me<strong>THF</strong>’s<br />
advantages include its origin from<br />
renewable and price stable resources as<br />
well as beneficial physical and chemical<br />
properties that can provide increased<br />
yields at reduced costs. The major benefits<br />
are summarised in table 1.<br />
The solvent 2-Me<strong>THF</strong> is obtained<br />
from furfural through hydrogenation.<br />
In turn, furfural is obtained from<br />
renewable resources, such as corn cobs<br />
and sugar cane, through the intramolecular<br />
cyclisation of the naturally-occurring<br />
pen<strong>to</strong>ses. In contrast, <strong>THF</strong> is<br />
obtained from 1,4-butanediol, an oilderived<br />
substance.<br />
The incineration of solvents is the<br />
main fine chemicals industry contribu<strong>to</strong>r<br />
<strong>to</strong> the <strong>green</strong>house effect. The recent<br />
political and legislative drive for reduction<br />
of CO 2 emissions should make solvents<br />
derived from renewable<br />
resources highly desirable due <strong>to</strong> their<br />
reduced CO 2 emissions impact. Incineration<br />
of 2-Me<strong>THF</strong> does not increase<br />
the CO 2 concentration in the atmosphere<br />
as it simply returns the CO 2 captured<br />
by the previous year’s crop from<br />
the air.<br />
2-Me<strong>THF</strong> is currently the only aprotic<br />
solvent similar <strong>to</strong> <strong>THF</strong> that is<br />
derived from renewable resources and<br />
industrially available 1 . The market<br />
share for 2-Me<strong>THF</strong> is growing rapidly<br />
driving the price of the compound<br />
lower. This is in sharp contrast <strong>to</strong> the<br />
long term trend for oil-derived <strong>THF</strong>,<br />
where prices have increased over the<br />
past decade by approximately 50%.<br />
innovation opportunities<br />
The methyl substituted version of <strong>THF</strong><br />
is not miscible with water. It is comparable<br />
or even better than <strong>THF</strong> in terms<br />
of its chemical properties. However, 2-<br />
Me<strong>THF</strong> resembles <strong>to</strong>luene in terms of<br />
physical properties and this creates<br />
huge innovation opportunities for cutting<br />
costs both in existing and new<br />
processes.<br />
The work-up for the <strong>THF</strong>-based reaction<br />
is complicated by <strong>THF</strong>’s miscibility<br />
with water. For oily products, <strong>THF</strong><br />
is distilled first and then the oily crude<br />
is extracted with a saturated saline<br />
solution. For solid products, a nonpolar<br />
solvent such as <strong>to</strong>luene needs <strong>to</strong> be<br />
added <strong>to</strong> achieve phase separation and<br />
avoid precipitation. In both cases emulsions,<br />
rag layers at the phase interfaceand<br />
poor extraction yields are frequent<br />
complications.<br />
2-Me<strong>THF</strong> is not water miscible and<br />
provides easy and clean phase separation<br />
during work-up. These advantages<br />
make the process simpler and more<br />
robust, translating in<strong>to</strong> higher throughput<br />
and reduced cost of quality.<br />
organic synthesis<br />
A <strong>green</strong><br />
<strong>alternative</strong> <strong>to</strong> <strong>THF</strong><br />
Table 1: Me<strong>THF</strong> vs <strong>THF</strong><br />
Dr Rainer Aul, of Chemetall GmbH, and Dr<br />
Bogdan Comanita, of Penn Specialty<br />
Chemicals propose 2-methyl tetrahydrofuran<br />
as a cost-effective <strong>alternative</strong> <strong>to</strong> widely used<br />
tetrahydrofuran chemistry<br />
Advantages Source of savings<br />
Renewable resource CO2 emissions credits; solvent from renewable resources<br />
Decreasing price trend; supply risk decoupled from oil<br />
Physical properties Increased throughput; easy aqueous phase separation<br />
Less solvent; more efficient extraction<br />
Less solvent; solvent reuse & recycling: azeotrope with water<br />
Chemical properties Less impurities; better solvent stability <strong>to</strong> acids and base<br />
Increased throughput; higher reaction yields<br />
Less solvent; higher saturation concentrations<br />
Improved safety; lower volatility, higher flash point<br />
Figure 1: Degradation<br />
of <strong>THF</strong> and Me<strong>THF</strong>,<br />
using homogenous<br />
50:50 % solutions<br />
<strong>THF</strong>/Me<strong>THF</strong> with 2 N<br />
HCl at 60°C.<br />
The methyl-substituted<br />
<strong>THF</strong> reduces<br />
the solvent and<br />
energy variable costs.<br />
Thus 2-Me<strong>THF</strong> has<br />
better extractive properties<br />
than the classic<br />
<strong>THF</strong>/ <strong>to</strong>luene mixture<br />
2 . This means the<br />
number of extraction<br />
steps can be reduced<br />
while the recovery of<br />
the product is simultaneously<br />
increased.<br />
The 2-Me<strong>THF</strong> solution<br />
of crude product can be dried<br />
through a simple distillation at atmospheric<br />
pressure. The water-rich Me<strong>THF</strong><br />
azeotrope will create rapidly an anhydrous<br />
solution providing the option <strong>to</strong><br />
add a new reagent without product isolation.<br />
For example, the classic reaction<br />
sequence carbonyl <strong>to</strong> alcohol followed<br />
by alcohol <strong>to</strong> ester is particularly<br />
adequate for Me<strong>THF</strong>. The solvent consumption<br />
is cut by 50% and the<br />
throughput is vastly improved by<br />
avoiding isolation of the intermediate<br />
alcohol.<br />
Last but not least, 2-Me<strong>THF</strong> is much<br />
easier <strong>to</strong> recycle and dry than <strong>THF</strong>.<br />
This has important advantages for <br />
www.manufacturing-chemist.info May 2007 manufacturing chemist 33
dedicated production capacities consuming<br />
hundreds of metric <strong>to</strong>ns of solvent<br />
per year. In these capacities <strong>THF</strong> is<br />
recycled and dried using ‘swing distillation’.<br />
In contrast 2-Me<strong>THF</strong> needs<br />
only a simple distillation at atmospheric<br />
pressure. The recycling and drying<br />
process is much more cost efficient<br />
for 2-Me<strong>THF</strong> because the energy cost of<br />
distillation is reduced by an estimated<br />
70% 3 . The need for an upfront capital<br />
investment for a specialised distillation<br />
unit for <strong>THF</strong> recycling is also eliminated.<br />
<br />
chemical advantages<br />
2-Me<strong>THF</strong> is a versatile reaction solvent<br />
covering a range of applications including<br />
Grignard, organopalladium,<br />
organozinc, lithium hydride reductions<br />
and biphasic reactions 4 . It shows<br />
increased stability <strong>to</strong> strong bases compared<br />
with <strong>THF</strong>, a fact that is well documented<br />
and explains its use in<br />
organolithium chemistry applications 5 .<br />
Me<strong>THF</strong> is also more stable than <strong>THF</strong><br />
in acidic conditions. Figure 1 shows<br />
the intrinsic difference of stability<br />
between <strong>THF</strong> and Me<strong>THF</strong> under acidic<br />
conditions in a homogenous solution 6 .<br />
In a real life situation, the hydrolysis of<br />
2-Me<strong>THF</strong> will be much slower due <strong>to</strong><br />
its immiscibility with water. This has<br />
important implications relative <strong>to</strong> the<br />
impurity profile and cost of quality<br />
associated <strong>to</strong> a given process.<br />
<strong>THF</strong> is currently the most common<br />
solvent used in Grignard reactions. 2-<br />
Me<strong>THF</strong> is challenging this position<br />
based on its very limited water solubility<br />
and better pH stability allowing for<br />
phase separation and improved yields.<br />
Additional washing steps are eliminated<br />
and a dry solution can be obtained by<br />
simple azeotropic distillation.<br />
34<br />
organic synthesis<br />
Table 2: Grignard bromides solubility in 2-Me<strong>THF</strong><br />
RMgBr Solution in Me<strong>THF</strong> Solution in <strong>THF</strong><br />
w/w % Mol/l Cryst. Temp. w/w% Mol/l Cryst. Temp.<br />
MethylMgBr 35 3.2