Source: KANSAS STATE UNIV submitted to
PROCESS TECHNOLOGY FOR SCALEUP OF ENZYMATIC CATALYSIS IN ORGANIC MEDIA
Sponsoring Institution
National Institute of Food and Agriculture
Project Status
COMPLETE
Funding Source
Reporting Frequency
Annual
Accession No.
0194611
Grant No.
2001-35504-12970
Cumulative Award Amt.
(N/A)
Proposal No.
2003-01024
Multistate No.
(N/A)
Project Start Date
Jul 1, 2002
Project End Date
Sep 30, 2004
Grant Year
2003
Program Code
[71.2]- (N/A)
Recipient Organization
KANSAS STATE UNIV
(N/A)
MANHATTAN,KS 66506
Performing Department
CHEMICAL ENGINEERING
Non Technical Summary
The use of enzymes as catalysts for organic phase reactions offers the potential for the transformation of agricultural feedstocks into high value-added products. Unfortunately, in organic media, the activity and stability of enzymes has been shown to be a strong function of the amount of water present.
Animal Health Component
50%
Research Effort Categories
Basic
50%
Applied
50%
Developmental
(N/A)
Classification

Knowledge Area (KA)Subject of Investigation (SOI)Field of Science (FOS)Percent
1110210105050%
1110210106050%
Goals / Objectives
1. Develop an on-line sensor for the water content of micro-aqueous organic fluids and fluid mixtures as they occur for example in enzymatically catalyzed esterifications. 2. Based on previous results, develop a thin film composite pervaporation membrane based on cellulose acetate as selective layer, with a polymeric support structure and technically useful productivity and stability. 3. Test the performance of the combination of the new sensor and the continuous water removal by membrane pervaporation for a model reaction on the laboratory scale (production of geranyl acetate using a commercial lipase in hexane as the solvent).
Project Methods
Although the optical, mechanical, and electronic components for the sensor are already developed, experiments to determine the specific chemistry for sensing of water in organic solvents will be performed. In particular a number of polymer films will be tested for specific and sensitive detection and particular properties relevant to commercialization and engineering will be explored. We will screen thin film coatings to be used in hexane with the reactants and reaction products of our model reaction present at realistic levels. We will be testing sensing films based on organic, inorganic, and biological polymers. In order for a sensor to be operative and useful for real-time process control, a number of properties will need to be examined. For each sensing chemistry to be tested as described above, experiments are planned to address these issues. Sensitivity: The phase shift response in p radians as a function of change in water content will be determined. Water content in hexane will be controlled by mixing of rigorously dried hexane and water saturated hexane in defined amounts. Response time: Experiments will determine the speed with which the sensor reaches equilibrium upon a change in water content. Reproducibility: We will insure that consistent results are achieved for the same sample over the course of several repetitive experiments. Additionally, several waveguide sensors prepared with the same sensing chemistry will be checked to determine the sample to sample variation in response. Interferrents (specificity): All properties will be examined in both pure water:hexane solutions and with the addition of the other reaction components for the enzymatic esterification of geraniol. These components include lipase, acetic acid, geraniol, and geranyl acetate. Long-term stability: The response of a waveguide sensor as a function of exposure time to the reaction conditions will be examined in order to determine the long-term stability of our sensors. In this project, we will determine the optimum conditions for producing asymmetric membranes from cellulose acetate for application in enzymatic reactors. These integrally-skinned asymmetric cellulose acetate membranes will be produced according to known procedures by phase inversion from solutions in acetone and by our prior experience in membrane production. The membranes will be tested for integrity and characterized for the thickness of their selective layer using gas permeation by non-condensible gases. A steady state fed batch reaction will be set up for enzymatic esterification of geraniol to geranyl acetate by a commercially available immobilized enzyme preparation from Candida Antarctica. Adjustable water removal will be made possible by having two or three membrane separation cells available in parallel, and by adjusting the flow to each cell. Initially, the continuous water control by pervaporation will be tested by injecting via syringe pump water or water saturated solvent into the reactor at water addition rates expected from the esterification reaction and removing this water continuously by pervaporation.

Progress 07/01/02 to 09/30/04

Outputs
Enzymes are fundamental to all life on earth. They facilitate all biologically important chemical reactions and are for example essential to handling information and energy in all living organisms. Products derived from inexpensive agricultural byproducts by enzymatic catalysis can be labeled as "natural" which is a significant incentive for the consumer. These products command a much higher price than identical chemicals made using conventional chemical catalysis. However, such new natural products can often only be made in organic solvents where the reactants and products are both soluble. The dissolved water content is crucial for enzymatic reactions in solvents. The technical feasibility of sensing and simultaneously controlling dissolved water in an organic solvent was conclusively shown in laboratory experiments. Commercial enzyme preparations were used to produce a fragrance in the solvent hexane from a byproduct of wood pulping. The optimum reaction conditions were determined. These results will aid in the use of enzymatic reactions to produce high-value natural flavors and fragrances from inexpensive agricultural feedstocks. Our new technology also allows to investigate the fundamentals of enzymatic catalysis in solvents at controlled water contents, which may lead to new information regarding the function of enzymes.

Impacts
The impact of the proposed work is to develop processing tools for efficient technical scale bioprocessing of agricultural feedstocks to high value added natural products using enzymatic catalysis. This work will remove technical barriers to producing natural high value-added products such as flavors, fragrances, and pharmaceuticals from agricultural feedstocks.

Publications

  • Kang, I.-J., Rezac, M. E., Pfromm, P. H., "Membrane permeation based sensing for dissolved water in organic micro-aqueous media", Journal of Membrane Science, 239/2, 213-217, 2004


Progress 01/01/03 to 12/31/03

Outputs
Nevertheless, we are on-schedule with significant achievements on all of the original objectives. To summarize the results to date that are detailed below, the laser interferometric sensor for dissolved water in organics shows promise and we continue development as proposed. In addition, a membrane permeation based water sensor has been developed and tested in batch reactor runs for gram-scale enzymatic production of geranyl acetate while actively controlling the water concentration via membrane pervaporation. Initial kinetic data with water concentration control and continuous sensing of the thermodynamic water activity by our membrane sensor is shown below. 1. Develop an on-line sensor for the water content of micro-aqueous organic fluids and fluid mixtures. We evaluated two separate approaches for measuring the concentration of dissolved water in n-hexane. The first was based on a laser interferometric principle. The second was based on a selective membrane permeation process. Both showed good results. The membrane sensor proved to require less instrumentation and up to now provided more stable results over the entire range of water concentrations of interest. Sensor response times are on the order of seconds. To date, we have detected no problems with interference from other solution components. We have worked extensively with water/organic systems. 2. Develop a thin film composite pervaporation membrane. We have used cellulose acetate/ceramic composite membranes made by kiss-coating of cellulose acetate solutions in acetone on a commercial ceramic substrate up to now Defect-free cellulose acetate films on the order of 1 micrometer thickness or less have been produced. 3. Test the performance of the combination of the new sensor and the continuous water removal for a model reaction on the laboratory scale. In this work, we demonstrated that the membrane permeation system could be used to rapidly and accurately increase or decrease the concentration of water in the system. The rate of reaction for enzymatically catalyzed geraniol conversion to geranyl acetate was measured at water concentrations of 13 and 16 ppm. Even the minor change in water activity in n-hexane (3ppm) had an impact on the initial rate of reaction. We can now explore the exact influence of the water thermodynamic activity (constant throughout the reaction) on the reaction kinetics. Issues such as enzyme lifetime and reversibility (cycling) of the water activity will be investigated.

Impacts
Process technology for the rapid and facile control of the water activity in organic liquids has been developed. The technology is being employed to demonstrate the importance of water content on the kinetic activity of enzymes in organic media.

Publications

  • Kang, I.-J., Rezac, M. E. and Pfromm, P. H. "Membrane permeation based sensing for dissolved water in organic micro-aqueous media", Journal of Membrane Science (submitted June 2003, accepted January 2004).
  • Kang, I.-J., Rezac, M. E. and Pfromm, P. H., "Sensing of Water in Microaqueous Solvents by Highly Selective Membrane Permeation", AIChE National Meeting, San Francisco, CA, paper 334b, November 18, 2003.
  • Bartling, K., Thompson, J., Pfromm, P, Rezac, M., Czermak, P., "Membrane-reactor systems for the selective control of water activity in lipase-catalyzed esterifications", Grenada, Spain, 2001.
  • Bartling, K., Thompson, J., Pfromm, P. H., Rezac, M. E., Czermak, P., "Biocatalytic membrane reactor – application of pervaporation for improved enzyme-catalyzed esterification of geraniol in the organic phase", Dechema Section Membrane Technology, Frankfurt, Germany, 2001.
  • Bartling, K., Thompson, J. U. S., Pfromm, P. H., Rezac, M.E. and Czermak, P., "Einsatz der Pervaporation zur Verbesserung der enzymkatalysierten Esterifikation von Geraniol in der organischen Phase," Aachener Membran Kolloquium, Preprints 8, pg. II93-II96, Verlag Mainz, Aachen 2001, ISBN 3-89653-834-9, 2001.