Academic literature on the topic 'Biochemical engineering'
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Journal articles on the topic "Biochemical engineering"
Miot, Sylvie, and Jean-Louis Boulay. "Biochemical engineering." Current Opinion in Biotechnology 13, no. 2 (April 2002): 83. http://dx.doi.org/10.1016/s0958-1669(02)00290-2.
Full textLee, Kelvin H., and Vassily Hatzimanikatis. "Biochemical engineering." Current Opinion in Biotechnology 13, no. 2 (April 2002): 85–86. http://dx.doi.org/10.1016/s0958-1669(02)00306-3.
Full textZabriskie, DaneW. "Biochemical engineering." Current Opinion in Biotechnology 7, no. 2 (April 1996): 187–89. http://dx.doi.org/10.1016/s0958-1669(96)80011-5.
Full textMay, Sheldon W., and Robert D. Schwartz. "Biochemical engineering." Current Opinion in Biotechnology 8, no. 2 (April 1997): 145–47. http://dx.doi.org/10.1016/s0958-1669(97)80092-4.
Full textMittal, G. S. "Biochemical Engineering." Canadian Institute of Food Science and Technology Journal 22, no. 4 (October 1989): 338. http://dx.doi.org/10.1016/s0315-5463(89)70422-3.
Full textCarrondo, Manuel JT, and John G. Aunins. "Biochemical engineering." Current Opinion in Biotechnology 15, no. 5 (October 2004): 441–43. http://dx.doi.org/10.1016/j.copbio.2004.08.014.
Full textYarmush, Martin, and Henrik Pedersen. "Biochemical engineering." Current Opinion in Biotechnology 6, no. 2 (January 1995): 189–91. http://dx.doi.org/10.1016/0958-1669(95)80030-1.
Full textLarsson, G., S. B. Jørgensen, M. N. Pons, B. Sonnleitner, A. Tijsterman, and N. Titchener-Hooker. "Biochemical engineering science." Journal of Biotechnology 59, no. 1-2 (December 1997): 3–9. http://dx.doi.org/10.1016/s0168-1656(97)00158-2.
Full textLyddiatt, Andrew. "Advanced biochemical engineering." Chemical Engineering Science 43, no. 2 (1988): 403–4. http://dx.doi.org/10.1016/0009-2509(88)85060-7.
Full textWinkler, M. A. "Advance biochemical engineering." Chemical Engineering Journal 38, no. 1 (May 1988): B14—B15. http://dx.doi.org/10.1016/0300-9467(88)80063-7.
Full textDissertations / Theses on the topic "Biochemical engineering"
Conejeros, Raul. "Optimisation of biochemical engineering systems." Thesis, University of Cambridge, 2000. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.621770.
Full textWong, Kelvin Wai Wah. "Fundamentals and application of metabolic engineering /." View abstract or full-text, 2006. http://library.ust.hk/cgi/db/thesis.pl?CENG%202006%20WONG.
Full textHutchinson, Ucrecia Faith. "Biochemical processes for Balsamic-styled vinegar engineering." Thesis, Cape Peninsula University of Technology, 2019. http://hdl.handle.net/20.500.11838/3048.
Full textThe South African wine industry is constantly facing several challenges which affect the quality of wine, the local/global demand and consequently the revenue generated. These challenges include the ongoing drought, bush fires, climate change and several liquor amendment bills aimed at reducing alcohol consumption and alcohol outlets in South Africa. It is therefore critical for the wine industry to expand and find alternative ways in which sub-standard or surplus wine grapes can be used to prevent income losses and increase employment opportunities. Traditional Balsamic Vinegar (TBV) is a geographically and legislative protected product produced only in a small region in Italy. However, the methodology can be used to produce similar vinegars in other regions. Balsamic-styled vinegar (BSV), as defined in this thesis, is a vinegar produced by partially following the methods of TBV while applying process augmentation techniques. Balsamic-styled vinegar is proposed to be a suitable product of sub-standard quality or surplus wine grapes in South Africa. However, the production of BSV necessitates the use of cooked (high sugar) grape must which is a less favourable environment to the microorganisms used during fermentation. Factors that negatively affect the survival of the microorganisms include low water activity due to the cooking, high osmotic pressure and high acidity. To counteract these effects, methods to improve the survival of the non-Saccharomyces yeasts and acetic acid bacteria used are essential. The primary aim of this study was to investigate several BSV process augmentation techniques such as, aeration, agitation, cell immobilization, immobilized cell reusability and oxygen mass transfer kinetics in order to improve the performance of the microbial consortium used during BSV production. The work for this study was divided into four (4) phases. For all the phases a microbial consortium consisting of non-Saccharomyces yeasts (n=5) and acetic acid bacteria (n=5) was used. Inoculation of the yeast and bacteria occurred simultaneously. The 1st phase of the study entailed evaluating the effect of cells immobilized by gel entrapment in Ca-alginate beads alongside with free-floating cells (FFC) during the production of BSV. Two Ca-alginate bead sizes were tested i.e. small (4.5 mm) and large (8.5 mm) beads to evaluate the effects of surface area or bead size on the overall acetification rates. Ca-alginate beads and FFC fermentations were also evaluated under static and agitated (135 rpm) conditions. The 2nd phase of the study involved studying the cell adsorption technique for cell immobilization which was carried-out using corncobs (CC) and oak wood chips (OWC), while comparing to FFC fermentations. At this phase of the study, other vinegar bioreactor parameters such as agitation and aeration were studied in contrast to static fermentations. One agitation setting (135 rpm) and two aeration settings were tested i.e. high (0.3 vvm min−1) and low (0.15 vvm min−1) aeration conditions. Furthermore, to assess the variations in cell adsorption capabilities among individual yeast and AAB cells, the quantification of cells adsorbed on CC and OWC prior- and post-fermentation was conducted using the dry cell weight method. The 3rd phase of the study entailed evaluating the reusability abilities of all the matrices (small Ca-alginate beads, CC and OWC) for successive fermentations. The immobilized cells were evaluated for reusability on two cycles of fermentation under static conditions. Furthermore, the matrices used for cell immobilization were further analysed for structure integrity by scanning electron microscopy (SEM) before and after the 1st cycle of fermentations. The 3rd phase of the study also involved the sensorial (aroma and taste) evaluations of the BSV’s obtained from the 1st cycle of fermentation in order to understand the sensorial effects of the Ca-alginate beads, CC and OWC on the final BSV. The 4th phase of the study investigated oxygen mass transfer kinetics during non-aerated and aerated BSV fermentation. The dynamic method was used to generate several dissolved oxygen profiles at different stages of the fermentation. Consequently, the data obtained from the dynamic method was used to compute several oxygen mass transfer parameters, these include oxygen uptake rate ( 𝑟𝑟𝑂𝑂2 ), the stoichiometric coefficient of oxygen consumption vs acid yield (𝑌𝑌𝑂𝑂/𝐴𝐴), the oxygen transfer rate (𝑁𝑁𝑂𝑂2 ), and the volumetric mass transfer coefficients (𝐾𝐾𝐿𝐿𝑎𝑎). During all the phases of the study samples were extracted on weekly intervals to evaluate pH, sugar, salinity, alcohol and total acidity using several analytical instruments. The 4th phase of the study involved additional analytical tools, i.e. an oxygen µsensor to evaluate dissolved oxygen and the ‘Speedy breedy’ to measure the respiratory activity of the microbial consortium used during fermentation. The data obtained from the 1st phase of the study demonstrated that smaller Ca-alginate beads resulted in higher (4.0 g L-1 day−1) acetification rates compared to larger (3.0 g L-1 day−1) beads, while freely suspended cells resulted in the lowest (0.6 g L-1 day−1) acetification rates. The results showed that the surface area of the beads had a substantial impact on the acetification rates when gel entrapped cells were used for BSV fermentation. The 2nd phase results showed high acetification rates (2.7 g L-1 day−1) for cells immobilized on CC in contrast to cells immobilized on OWC and FFC, which resulted in similar and lower acetification rates. Agitated fermentations were unsuccessful for all the treatments (CC, OWC and FFC) studied. Agitation was therefore assumed to have promoted cell shear stress causing insufficient acetification during fermentations. Low aerated fermentations resulted in better acetification rates between 1.45–1.56 g L-1 day−1 for CC, OWC and FFC. At a higher aeration setting, only free-floating cells were able to complete fermentations with an acetification rate of 1.2 g L-1 day−1. Furthermore, the adsorption competence data showed successful adsorption on CC and OWC for both yeasts and AAB with variations in adsorption efficiencies, whereby OWC displayed a lower cell adsorption capability compared to CC. On the other hand, OWC were less efficient adsorbents due to their smooth surface, while the rough surface and porosity of CC led to improved adsorption and, therefore, enhanced acetification rates. The 3rd phase results showed a substantial decline in acetification rates on the 2nd cycle of fermentations when cells immobilized on CC and OWC were reused. While cells entrapped in Ca-alginate beads were able to complete the 2nd cycle of fermentations at reduced acetification rates compared to the 1st cycle of fermentations. The sensory results showed positive ratings for BSV’s produced using cells immobilized in Ca-alginate beads and CC. However, BSV’s produced using OWC treatments were neither ‘liked nor disliked’ by the judges. The SEM imaging results further showed a substantial loss of structural integrity for Ca-alginate beads after the 1st cycle fermentations, with minor changes in structural integrity of CC being observed after the 1st cycle fermentations. OWC displayed the same morphological structure before and after the 1st cycle fermentations which was attributed to their robustness. Although Ca-alginate beads showed a loss in structural integrity, it was still assumed that Ca-alginate beads provided better protection against the harsh environmental conditions in contrast to CC and OWC adsorbents due to the acetification rates obtained on both cycles. The 4th phase data obtained from the computations showed that non-aerated fermentations had a higher 𝑌𝑌𝑂𝑂/𝐴𝐴, 𝑟𝑟𝑂𝑂2 , 𝑁𝑁𝑂𝑂2 and a higher 𝐾𝐾𝐿𝐿𝑎𝑎 . It was clear that aerated fermentations had a lower aeration capacity due to an inappropriate aeration system design and an inappropriate fermentor. Consequently, aeration led to several detrimental biochemical changes in the fermentation medium thus affecting 𝐾𝐾𝐿𝐿𝑎𝑎 and several oxygen mass transfer parameters which serve as a driving force. Overall, it was concluded that the best method for BSV production is the use of cells entrapped in small alginate beads or cells adsorbed on CC under static and non-aerated fermentations. This conclusion was based on several factors such as cell affinity/cell protection, acetification rates, fermentation period and sensorial contributions. However, cells entrapped in Ca-alginate beads had the highest acetification rates. The oxygen mass transfer computations demonstrated a high 𝐾𝐾𝐿𝐿𝑎𝑎 when Ca-alginate beads were used under static-non-aerated conditions compared to fermentations treated with CC. Therefore, a fermentor with a high aeration capacity needs to be designed to best suit the two BSV production systems (Ca-alginate beads and CC). It is also crucial to develop methods which can increase the robustness of Ca-alginate beads in order to improve cell retention and reduce the loss of structural integrity for subsequent cycles of fermentation. Studies to define parameters used for upscaling the BSV production process for large scale productions are also crucial.
Guise, Andrew David. "A biochemical engineering study of lysozyme refolding." Thesis, University of Bath, 1996. https://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.337816.
Full textCampbell, Sean Thomas. "Protein Engineering for Biochemical Interrogation and System Design." Diss., The University of Arizona, 2015. http://hdl.handle.net/10150/560940.
Full textMandel, Johannes Julius. "Graph-Based Modelling and Reverse-Engineering of Biochemical Networks." Thesis, Ulster University, 2007. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.487658.
Full textRocha, Andrea M. "Computational Discovery of Phenotype Related Biochemical Processes for Engineering." Scholar Commons, 2011. http://scholarcommons.usf.edu/etd/3315.
Full textAkintoye, Ayodele. "Continuous chromatographic biochemical reaction-separation." Thesis, Aston University, 1989. http://publications.aston.ac.uk/9739/.
Full textMcEuen, Scott Jacob. "Thermal analysis of biochemical systems." Thesis, Massachusetts Institute of Technology, 2013. http://hdl.handle.net/1721.1/81702.
Full textCataloged from PDF version of thesis.
Includes bibliographical references (p. 109-112).
Scientists, both academic and industrial, develop two main types of drugs: 1) small molecule drugs, which are usually chemically synthesized and are taken orally and 2) large molecule, biotherapeutic, or protein-based drugs, which are often synthesized via ribosome transcription in bacteria cells and are injected. Historically, the majority of drug development, revenue, and products has come from small molecule drugs. However, recently biotherapeutic drugs have become more common due to their increased potency and specificity (the ability to chemically bond to the targeted protein of interest). Researchers now estimate that as much as 50% of current drug development activities (pre-market approval) are focused on these protein-based drugs. There are several well-documented steps necessary in the development of a new large molecule drug. One critical element during the end of the biotherapeutic drug discovery phase and the beginning of the manufacturing phase is known as preformulation or formulation development. During this stage scientists systematically test the effects of adding various excipients (non-protein additives added to enhance the protein stability, solubility, activity of the drug, etc.) to the potential large molecule drug. Differential scanning calorimetry (DSC) is a common technique used to perform these formulation studies. In a classic DSC experiment, a protein is heated from 20-80°C and the heat absorbed while the protein unfolds is measured. Many researchers prefer the use of a DSC instrument because of its label-free nature, meaning that no fluorescent or radio-labeled tag is necessary to perform the measurement. The heat absorbed during the unfolding event(s) is directly measured. However, current commercial DSC instruments suffer from high protein consumption (especially when compared to other labeled techniques), low sensitivity, and slow throughput. The aim of this thesis is to address two of the three areas mentioned above: high protein consumption and slow throughput. Since many formulation development studies are performed at therapeutic or high protein concentrations, one can reduce the experimental cell volume and thereby reduce the amount of protein material consumed. However, since there is less sample, less heat is produced. While in the literature there are several heat transfer models that describe how a DSC instrument literature there are several heat transfer models that describe how a DSC instrument functions, there are surprisingly few heat transfer models that detail how ambient temperature disturbances impact the thermal measurement. To better describe this behavior, a simplified state-space thermal model was created to predict the disturbance rejection of a custom DSC instrument. This model was verified experimentally using linear stochastic system identification techniques. To reduce sample throughput, the prototype calorimeter cell was made from disposable materials. Because the majority of protein systems are thermodynamically irreversible, at elevated temperatures the protein solution often aggregates and needs to be cleaned before a subsequent experiment can be run. This cleaning process constitutes a significant portion of the overall time to run an experiment. This thesis documents a fully functional DSC instrument that, while not completely disposable, has been designed, built, and tested with disposable microfluidic materials. Future work would then solve the technical hurdles of repeatably loading disposable microfluidic cells into the DSC instrument.
by Scott Jacob McEuen.
Ph.D.
Goel, Gautam. "Biochemical Systems Toolbox." Thesis, Georgia Institute of Technology, 2006. http://hdl.handle.net/1853/14509.
Full textBooks on the topic "Biochemical engineering"
Katoh, Shigeo, Jun-ichi Horiuchi, and Fumitake Yoshida, eds. Biochemical Engineering. Weinheim, Germany: Wiley-VCH Verlag GmbH & Co. KGaA, 2015. http://dx.doi.org/10.1002/9783527684984.
Full text1957-, Clark Douglas S., ed. Biochemical engineering. New York: M. Dekker, 1996.
Find full textDumont, Fabian E. Biochemical engineering. Hauppauge, NY: Nova Science Publishers, 2009.
Find full textF, Ollis David, ed. Biochemical engineering fundamentals. 2nd ed. New York: McGraw-Hill, 1986.
Find full text1935-, Lim Henry C., Venkatasubramanian K, Engineering Foundation (U.S.), and International Conference on Biochemical Engineering (4th : 1984 : Galway, Ireland), eds. Biochemical engineering IV. New York, N.Y: New York Academy of Sciences, 1986.
Find full textMatthias, Reuss, and International Symposium on Biochemical Engineering--Stuttgart (2nd : 1990), eds. Biochemical engineering, Stuttgart. Stuttgart: Fischer, 1991.
Find full text1928-, Bungay Henry R., and Belfort Georges, eds. Advanced biochemical engineering. New York: Wiley, 1987.
Find full text1947-, Shuler Michael L., Weigand William A, Engineering Foundation (U.S.), and Biochemical Engineering Conference (5th : 1987 : New England College), eds. Biochemical engineering V. New York, N.Y: New York Academy of Sciences, 1987.
Find full text1947-, Shuler Michael L., Weigand William A, New York Academy of Sciences., Engineering Foundation, and Biochemical Engineering Conference, (5th : 1987 : New England College), eds. Biochemical engineering 5. New York: New York Academy of Sciences, 1987.
Find full textHenrik, Pedersen, Mutharasan Rajakannu, DiBiasio David, and Biochemical Engineering Conference (7th : 1991 : Santa Barbara, Calif.), eds. Biochemical engineering VII. New York, N.Y: New York Academy of Sciences, 1992.
Find full textBook chapters on the topic "Biochemical engineering"
Dutta, Rajiv. "Genetic Engineering." In Fundamentals of Biochemical Engineering, 176–96. Berlin, Heidelberg: Springer Berlin Heidelberg, 2008. http://dx.doi.org/10.1007/978-3-540-77901-8_7.
Full textNielsen, Jens, John Villadsen, and Gunnar Lidén. "Biochemical Reaction Networks." In Bioreaction Engineering Principles, 119–88. Boston, MA: Springer US, 2003. http://dx.doi.org/10.1007/978-1-4615-0767-3_5.
Full textVilladsen, John, Jens Nielsen, and Gunnar Lidén. "Biochemical Reaction Networks." In Bioreaction Engineering Principles, 151–214. Boston, MA: Springer US, 2011. http://dx.doi.org/10.1007/978-1-4419-9688-6_5.
Full textBoghossian, Nicolas, Oliver Kohlbacher, and Hans-Peter Lenhof. "BALL: Biochemical Algorithms Library." In Algorithm Engineering, 330–44. Berlin, Heidelberg: Springer Berlin Heidelberg, 1999. http://dx.doi.org/10.1007/3-540-48318-7_26.
Full textHumphrey, Arthur E. "Biochemical Engineering — Past, Present, and Future." In Biochemical Engineering for 2001, 3–7. Tokyo: Springer Japan, 1992. http://dx.doi.org/10.1007/978-4-431-68180-9_1.
Full textRogers, Peter L. "Strategic Planning and New Directions in Biochemical Engineering." In Biochemical Engineering for 2001, 8–13. Tokyo: Springer Japan, 1992. http://dx.doi.org/10.1007/978-4-431-68180-9_2.
Full textXiao, Shou-Jun, Gregory Kenausis, and Marcus Textor. "Biochemical Modification of Titanium Surfaces." In Engineering Materials, 417–55. Berlin, Heidelberg: Springer Berlin Heidelberg, 2001. http://dx.doi.org/10.1007/978-3-642-56486-4_13.
Full textKazuyuki, Shimizu. "An Overview and Future Perspective for Bioprocess Systems Engineering." In Biochemical Engineering for 2001, 765–67. Tokyo: Springer Japan, 1992. http://dx.doi.org/10.1007/978-4-431-68180-9_204.
Full textRyu, Dewey D. Y., and J. Y. Kim. "Engineering and Genetic Approaches to Optimization of Recombinant Fermentation Process." In Biochemical Engineering for 2001, 133–37. Tokyo: Springer Japan, 1992. http://dx.doi.org/10.1007/978-4-431-68180-9_34.
Full textNielsen, Jens, John Villadsen, and Gunnar Lidén. "Biochemical Reactions — A First Look." In Bioreaction Engineering Principles, 47–93. Boston, MA: Springer US, 2003. http://dx.doi.org/10.1007/978-1-4615-0767-3_3.
Full textConference papers on the topic "Biochemical engineering"
Ghosh, Soma, Saraswathi Vishveshwara, and Nagasuma Chandra. "Inferring biochemical routes from biochemical networks." In 2013 Biomedical Sciences and Engineering Conference (BSEC). IEEE, 2013. http://dx.doi.org/10.1109/bsec.2013.6618500.
Full textWilliams, A. P. "A practice initiated learning strategy for biochemical engineering." In Third Conference on Engineering Education - Access, Retention and Standards. IEE, 2003. http://dx.doi.org/10.1049/ic:20030225.
Full text"Biochemical Signals and Material Characteristics." In 2018 7th International Conference on Medical Engineering and Biotechnology. Clausius Scientific Press, 2018. http://dx.doi.org/10.23977/medeb.2018.07014.
Full textByun, Eunjeong, Juhong Nam, Hyunji Shim, Esther Kim, Albert Kim, and Seunghyun Song. "Ultrasonic Hydrogel Biochemical Sensor System." In 2020 42nd Annual International Conference of the IEEE Engineering in Medicine and Biology Society (EMBC) in conjunction with the 43rd Annual Conference of the Canadian Medical and Biological Engineering Society. IEEE, 2020. http://dx.doi.org/10.1109/embc44109.2020.9176216.
Full textHori, Yutaka, and Richard M. Murray. "Engineering principles of synthetic biochemical oscillators with negative cyclic feedback." In 2015 54th IEEE Conference on Decision and Control (CDC). IEEE, 2015. http://dx.doi.org/10.1109/cdc.2015.7402292.
Full textLin, Ying, Vladimir Ilchenko, Jay Nadeau, and Lute Maleki. "Biochemical detection with optical whispering-gallery resonaters." In Lasers and Applications in Science and Engineering, edited by Alexis V. Kudryashov, Alan H. Paxton, and Vladimir S. Ilchenko. SPIE, 2007. http://dx.doi.org/10.1117/12.716591.
Full textPark, Sung-Yong, Sheraz Kalim, Caitlin Callahan, Michael A. Teitell, and Eric P. Y. Chiou. "Light-driven microfluidic platforms for droplet-based biochemical analysis." In SPIE NanoScience + Engineering, edited by Kishan Dholakia and Gabriel C. Spalding. SPIE, 2009. http://dx.doi.org/10.1117/12.828134.
Full textVoloshynska, Katerina, Tetjana Ilashchuka, Olexander Prydij, and Maria Gruia. "Dynamics of blood plasma by spectropolarimetry and biochemical techniques." In SPIE NanoScience + Engineering, edited by Hooman Mohseni, Massoud H. Agahi, and Manijeh Razeghi. SPIE, 2014. http://dx.doi.org/10.1117/12.2061731.
Full textChiang, Hui-Ju Katherine, Jie-Hong R. Jiang, and Francois Fages. "Reconfigurable neuromorphic computation in biochemical systems." In 2015 37th Annual International Conference of the IEEE Engineering in Medicine and Biology Society (EMBC). IEEE, 2015. http://dx.doi.org/10.1109/embc.2015.7318517.
Full textFan, W. J., M. X. Lin, M. Y. Zhao, Q. H. Xie, and B. Wang. "High-speed automatic biochemical immune assembly line." In 2022 5th World Conference on Mechanical Engineering and Intelligent Manufacturing (WCMEIM). IEEE, 2022. http://dx.doi.org/10.1109/wcmeim56910.2022.10021551.
Full textReports on the topic "Biochemical engineering"
Zhong, Xiaojing. Aggregation Effects in Generalized Linear Models: A Biochemical Engineering Application. Ames (Iowa): Iowa State University, January 2019. http://dx.doi.org/10.31274/cc-20240624-126.
Full textEly, Roger L., and Frank W. R. Chaplen. Metabolic Engineering of Light and Dark Biochemical Pathways in Wild-Type and Mutant Strains of Synechocystis PCC 6803 for Maximal, 24-Hour Production of Hydrogen Gas. Office of Scientific and Technical Information (OSTI), March 2014. http://dx.doi.org/10.2172/1122862.
Full textStern, David, and Gadi Schuster. Manipulating Chloroplast Gene Expression: A Genetic and Mechanistic Analysis of Processes that Control RNA Stability. United States Department of Agriculture, June 2004. http://dx.doi.org/10.32747/2004.7586541.bard.
Full textDudareva, Natalia, Alexander Vainstein, Eran Pichersky, and David Weiss. Integrating biochemical and genomic approaches to elucidate C6-C2 volatile production: improvement of floral scent and fruit aroma. United States Department of Agriculture, September 2007. http://dx.doi.org/10.32747/2007.7696514.bard.
Full textBarkan, Alice, and Zach Adam. The Role of Proteases in Regulating Gene Expression and Assembly Processes in the Chloroplast. United States Department of Agriculture, January 2003. http://dx.doi.org/10.32747/2003.7695852.bard.
Full textFridman, Eyal, and Eran Pichersky. Tomato Natural Insecticides: Elucidation of the Complex Pathway of Methylketone Biosynthesis. United States Department of Agriculture, December 2009. http://dx.doi.org/10.32747/2009.7696543.bard.
Full textLewinsohn, Efraim, Eran Pichersky, and Shimon Gepstein. Biotechnology of Tomato Volatiles for Flavor Improvement. United States Department of Agriculture, April 2001. http://dx.doi.org/10.32747/2001.7575277.bard.
Full textZhao, Bingyu, Saul Burdman, Ronald Walcott, Tal Pupko, and Gregory Welbaum. Identifying pathogenic determinants of Acidovorax citrulli toward the control of bacterial fruit blotch of cucurbits. United States Department of Agriculture, January 2014. http://dx.doi.org/10.32747/2014.7598168.bard.
Full textSchuster, Gadi, and David Stern. Integration of phosphorus and chloroplast mRNA metabolism through regulated ribonucleases. United States Department of Agriculture, August 2008. http://dx.doi.org/10.32747/2008.7695859.bard.
Full textSessa, Guido, and Gregory Martin. MAP kinase cascades activated by SlMAPKKKε and their involvement in tomato resistance to bacterial pathogens. United States Department of Agriculture, January 2012. http://dx.doi.org/10.32747/2012.7699834.bard.
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