Grants and Contracts Details
Description
Alkali-catalyzed transesterification of triglycerides is the preferred commercial
method for making biodiesel fuels in the United States. The economics of this process
are sensitive mainly to feedstock price and conversion costs. The conversion costs relate
to the feedstock purity, the reaction rate, the yield of alkyl esters, the efficiency of
separating the esters from the glycerol, and the glycerol purity. Recent studies of
biodiesel reactions, and a study of another two-phase natural oil reaction, have
demonstrated that novel mixing technologies can make significant reductions in batch
reaction times and product purities.
This project will study the effects of ultrasound micromixing on the
transesterification of soybean oil (SBO) with methanol under base catalysis. The primary
hypothesis is that the increase in methyl ester formation rates is primarily dependent on
the particle size distributions developed as a result of the ultrasonication. Measurements
of the actual particle size distributions will be related to the ultrasonication power per unit
volume. The transesterification kinetics will be interpreted in models that include the
interfacial area between the oil-rich and alcohol-rich phases, and the partition coefficients
for the various constituents. This model will be used, in part, to optimize product purities
and yields for various feed compositions and conditions. Existing process design
simulations of a biodiesel process will be updated based on our research to develop
economic models comparing the new process to conventional technology.
The work plan will generate the following deliverables: I) correlations of particle
size distributions and interfacial area with energy per unit volume for ultrasound
micromixing, 2) a kinetic model that includes interfacial area and predicts product
purities and methyl ester yield, 3) phase equilibria models that correlate the partitioning
of chemical components between the oil-rich and the alcohol-rich phases, and 4) a
process design simulation suitable for economic evaluation of an ultrasonication process
for biodiesel production from soybean oil.
A successful project could result in new, low-cost reactor designs for biodiesel
production and/or cost-saving modifications of existing reactors with appropriate
technology. Many existing plants use waste oils and greases as triglyceride sources since
the process feedstock is a major factor in the biodiesel price. While recycled
triglycerides can have high free fatty acid levels and water contamination that will limit
the improvements possible through improved mixing using sonication, it still is possible
to retrofit existing plants for better performance. Soybean oil is good model system for
this research as it has fairly uniform properties and is of interest to the co-sponsor.
Status | Finished |
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Effective start/end date | 1/1/05 → 12/31/06 |
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