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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

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