Academic literature on the topic 'Bioprocess engineering'
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Journal articles on the topic "Bioprocess engineering"
Galindo, E. "Bioprocess engineering." Trends in Biotechnology 16, no. 7 (July 1, 1998): 282–83. http://dx.doi.org/10.1016/s0167-7799(98)01211-6.
Full textBoudrant, Joseph, and Jack Legrand. "Bioprocess engineering." Process Biochemistry 45, no. 11 (November 2010): 1757. http://dx.doi.org/10.1016/j.procbio.2010.09.002.
Full textVilladsen, John. "“Bioprocess engineering”." Chemical Engineering Science 57, no. 7 (April 2002): 1235–36. http://dx.doi.org/10.1016/s0009-2509(02)00006-4.
Full textLightfoot, E. N. "Bioprocess engineering." Chemical Engineering Science 50, no. 6 (March 1995): 1069. http://dx.doi.org/10.1016/0009-2509(95)90139-6.
Full textJordan, M. A. "Bioprocess engineering principles." Minerals Engineering 9, no. 1 (January 1996): 133–35. http://dx.doi.org/10.1016/s0892-6875(96)90075-8.
Full textChisti, Yusuf. "Bioprocess engineering for everyone…" Biotechnology Advances 31, no. 2 (March 2013): 357. http://dx.doi.org/10.1016/j.biotechadv.2012.12.007.
Full textHu, Wei-Shou, and James C. Liao. "Biotechnology and bioprocess engineering." Current Opinion in Chemical Engineering 2, no. 4 (November 2013): 363–64. http://dx.doi.org/10.1016/j.coche.2013.10.004.
Full textSch�gerl, K. "Makers of bioprocess engineering." Bioprocess Engineering 11, no. 4 (September 1994): 121. http://dx.doi.org/10.1007/bf00518732.
Full textPAZOS, Marta, Maria A. LONGO, and M. Angeles SANROMAN. "Experiences of Innovation Teaching in Bioprocess Engineering University Course." Revista Romaneasca pentru Educatie Multidimensionala 5, no. 1 (June 30, 2013): 123–39. http://dx.doi.org/10.18662/rrem/2013.0501.09.
Full textChéruy, A. "Software sensors in bioprocess engineering." Journal of Biotechnology 52, no. 3 (January 1997): 193–99. http://dx.doi.org/10.1016/s0168-1656(96)01644-6.
Full textDissertations / Theses on the topic "Bioprocess engineering"
Zhang, Zhiyu Ph D. Massachusetts Institute of Technology. "Microbioreactors for bioprocess development." Thesis, Massachusetts Institute of Technology, 2006. http://hdl.handle.net/1721.1/39638.
Full textIncludes bibliographical references (leaves 109-113).
This thesis presents the design, fabrication, and characterization of a microbioreactor integrated with automated sensors and actuators as a step towards high-throughput bioprocess development. In particular, this thesis demonstrates the feasibility of culturing microbial cells in microliter-volume reactors in batch, continuous, fed-batch operations. The microbioreactor is fabricated out of poly(methylmethacrylate) and poly(dimethylsiloxane). Active mixing is made possible by a miniature magnetic stir bar. Online optical measurements for optical density, pH, and dissolved oxygen are integrated. Oxygenation in the microbioreactor is characterized and reproducible batch fermentation of Escherichia coli and Saccharomyces cerevisiae are demonstrated and benchmarked with benchscale bioreactors. Global gene expression analysis of S. cerevisiae exhibits physiological and molecular characteristics which parallel those of large-scales. A microchemostat, continuous culture of microbial cells, is realized in the microbioreactor. E. coli cells are fed by pressure-driven single phase flow of fresh medium through a microchannel. Chemotaxis, the back growth of bacterial cells into the medium feed channel, is prevented by local heating.
(cont.) Using poly(ethylene glycol) -grafted poly(acrylic acid) copolymer films, PMMA and PDMS surfaces are modified to generate bio-inert surfaces resistant to nonspecific protein adsorption and cell adhesion. These advances enable cell growth kinetics and stoichoimetry to be obtained in the microchemostat consistent with reported phenomena from conventional stirred-tank bioreactors, as indicated by the time profiles of OD600nm, pH, and DO measurements at steady states. Water evaporation from the microbioreactor allows feeding of base and glucose solutions into the small reactor to realize fed-batch operations. Commercial microvalves are integrated to obtain closed-loop pH control. pH value in the microbioreactor is successfully maintained within a physiological scale during the time course of E. coli cell cultivation in rich media. One key issue for high-throughput bioprocessing is the parallel operation of multiple microbial fermentations while keeping each single microbioreactor disposable. Plug-in-and-flow microfluidic connectors and fabricated polymer micro-optical lenses/connectors are integrated in the microbioreactor "cassettes" for fast set-up and easy operation.
(cont.) A protocol multiplexed system for the parallel operation of four microbioreactors is demonstrated. The demonstrated functionality of the microbioreactor with integrated measurements and flexible operations could potentially have a large impact in bioprocess developments.
by Zhiyu Zhang.
Ph.D.
Prior, John Joseph. "Data reconciliation in bioprocess development." Thesis, Massachusetts Institute of Technology, 1997. http://hdl.handle.net/1721.1/10304.
Full textSolé, Ferré Jordi. "Oxidoreductive bioprocess intensification through reaction engineering and enzyme immobilization." Doctoral thesis, Universitat Autònoma de Barcelona, 2019. http://hdl.handle.net/10803/669346.
Full textThe research performed and disclosed in this thesis deals with the reaction engineering and the enzyme immobilization principles as tools to improve biocatalyzed oxidoreductive reactions. On a first stage, the co-immobilization of the P450 BM3 monooxygenase together with a NADPH cofactor regeneration enzyme, the glucose dehydrogenase (GDH-Tac), was studied. The best derivates were obtained when using two agarose supports, an epoxy functionalized (83% and 20% retained activity respectively) and an amino functionalized (28% and 25% retained activity respectively). Later on, the re-cycling of the immobilized enzymes was tested in reaction cycles using one of the natural substrates of the P450 BM3, the sodium laurate. Once it could be demonstrated that re-cycling of both P450 BM3 and GDH-Tac was possible, both enzymes were studied in two of the project’s target reactions, the hydroxylation of α- isophorone and the hydroxylation of diclofenac. In the first case, the optimization of the reaction conditions had to be performed prior to the reaction cycles. The reactor configuration, the oxygen income or the glucose concentration were adjusted. However, when the reaction was performed using the co-immobilized enzymes, the P450 BM3 was deactivated and it could not be re-used. The same happened with the hydroxylation of diclofenac. On the other hand, the reaction using soluble enzymes, resulted in 86.2% conversion for the α-isophorone (50 mM initial concentration) and 100% for the diclofenac (3.5 mM initial concentration). The product resulting from the hydroxylation of α-isophorone, the 4-hydroxy-isophorone, can be further oxidized to keto-isophorone, an intermediary for the synthesis of carotenoids and vitamin E. In order to enzymatically perform this step, an alcohol dehydrogenase and a NADPH oxidase, as a cofactor regenerator, were employed. When used in their soluble form, after 24 hours, 95.7% yield and a space time yield of 6.52 g L-1 day-1 were achieved. Moreover, the alcohol dehydrogenase was immobilized on epoxy-agarose and 58.2% retained activity was obtained. When re-used, the derivate could operate for 96h (4 cycles) improving the biocatalyst yield 2.5- fold compared with the reaction with soluble enzymes. The hydrogenation of α-isophorone results in 3,3,5-trimethylcyclohexanone, an industrial interesting substrate due to the polymers that can be obtained from its oxidized product, the trimethyl-ε-caprolactone. This compound is obtained by the Baeyer-Villiger insertion of an oxygen atom into the carbon ring. For this purpose, a cyclohexanone monooxygenase together with a commercial glucose dehydrogenase (GDH-01) were used. Different parameters of the reaction were optimized such as the biocatalyst formulation, the substrate addition rate or the biocatalyst loading. Afterwards, the reaction was scaled up to 1 liter first and then up to 100 liters. In this last pre-industrial reaction, 85% conversion, a space time yield of 2.7 g L-1 h-1 and a biocatalyst yield of 0.83 g g-1 cww could be obtained. Finally, this same reaction was performed using both enzymes immobilized and re-cycling was intended. The cyclohexanone monooxygenase could be immobilized following a previously described method and 62.4% retained activity was achieved. In the GDH-01 case, different supports were screened albeit at the end, it was also the amino functionalized agarose that resulted successful. A retained activity of 62.6% was obtained. In the reaction cycles, the immobilized enzymes were used either separately or both together. In the best case scenario, after six cycles of reaction (132.5 mM initial substrate) 3.6-fold and 1.9-fold higher biocatalysts yields were obtained for the monooxygenase and the GDH-01, respectively.
Nieto, Taype Miguel Angel. "Combining bioprocess and strain engineering strategies as efficient tools for the optimization of recombinant protein production in Pichia pastoris." Doctoral thesis, Universitat Autònoma de Barcelona, 2020. http://hdl.handle.net/10803/670163.
Full textLas factorías celulares microbianas pueden ser utilizadas para producir un amplio rango de bioproductos de interés para la biotecnología industrial, los cuales comprenden principalmente la producción de proteínas recombinantes y metabolitos. Pichia pastoris (Komagataela phaffii), emerge como un hospedero prometedor para la producción de proteína recombinante (RPP) debido a que comparte muchas características con Saccharomyces cerevisiae, sin embargo, muestra ventajas en relación con el consumo de oxígeno, tener un patrón de glicosilación más simple, y una menor secreción de proteínas endógenas. Por estas razones, se han realizado grandes esfuerzos con el objetivo de optimizar la eficiencia de este hospedero, los cuales pueden agruparse en dos principales y complementarios enfoques: la ingeniería de cepas y bioproceso. La presente tesis doctoral se basó en el uso de ambos enfoques para mejorar bioprocesos de producción de lipasas recombinantes con interés industrial. En primer lugar, se demostró la importancia del conocimiento de las cinéticas de producción como una potente herramienta para el diseño de estrategias óptimas en la RPP a través de la caracterización de dos clones con un diferente comportamiento, debido a su diferente dosis génica, expresando la lipasa 1 de Candida rugosa bajo la regulación del promotor GAP (PGAP) llevando a cabo cultivos en quimiostato y fed-batch. Los resultados, también justificados mediante análisis transcripcional de varios genes clave como importante novedad, demostraron que la cinética de producción depende de las características intrínsecas de cada clon usado. De esta manera, la selección de una µ adecuada para cada caso permite, de una manera diferente, un desarrollo racional del de proceso para poder optimizar los bioprocesos RPP. Después, se evaluó la potencial implementación de la deprivación de carbono (carbon-starving) como una innovadora estrategia que mejore las velocidades de producción y rendimientos de Crl1 en cultivos fed-batch con una previa caracterización fisiológica para cultivos en quimiostato. Los resultados evidenciaron que el efecto positivo de utilizar esta estrategia es altamente dependiente de las particularidades intrínsecas del clon utilizado. Se realizó un análisis transcripcional adicional (RNAseq) sobre muestras de quimiostato, resaltándose la diferencia en la transcripción para todos los genes de la levadura. Además, el comportamiento del bioproceso durante el uso del promotor GAP (PGAP) se comparó con la utilización del promotor inducible AOX1 (PAOX1) llevando a cabo cultivos en quimiostato para la producción de Crl1. Aunque en el caso del PAOX1 se apreció una mayor producción, se debería considerar una evaluación económica previa al escalado del bioproceso, considerando los numerosos inconvenientes del uso de metanol como sustrato. Finalmente, siguiendo el enfoque de la ingeniería de cepas, se caracterizó el uso de dos nuevos promotores independientes del uso de metanol sobre la expresión de la lipasa B de Candida antarctica (CalB) como una poderosa herramienta que permita explotar el potencial de P. pastoris en la RPP. Ambos promotores mostraron mucho mejores resultados en comparación a los obtenidos con el PGAP aunque los patrones de producción entre los promotores fue significativamente diferente para cada caso. En resumen, los resultados mostrados a lo largo de los diferentes capítulos de la presente tesis refuerzan la utilidad de la ingeniería de bioprocesos y de cepas a través de los diferentes estudios realizados, los cuales permitieron obtener mejoras significativas en la eficiencia de la RPP. El conocimiento de los factores clave involucrados en la expresión recombinante abre una amplia ventana de nuevas oportunidades que hacen posible que P. pastoris se establezca como una plataforma robusta para la RPP, mostrándose altamente competitiva frente a los sistemas convencionales.
Microbial cell factories can be used to produce a wide range of bioproducts of interest for the biotechnological industry, which comprises mainly the production of recombinant proteins and metabolites. Pichia pastoris (Komagataela phaffii), emerges as a promising host for recombinant protein production (RPP) due to it shares many features with Saccharomyces cerevisiae, however, displays some advantages in terms of oxygen consumption, simpler glycosylation pattern, and lower endogenous protein secretion. For these reasons, great efforts have been performed with the objective to optimize the efficiency of this host which can be grouped in two main and complementary approaches: the strain and bioprocess engineering. The present PhD thesis was focused in the use of both approaches, in order to improve the production bioprocess of recombinant lipases with industrial interest. At first, it was demonstrated the importance of the knowledge of production kinetics as strong tool to design optimal strategies for RPP through the characterization of two clones with contrasting production performance, due to its different gene dosage, expressing Candida rugosa lipase 1 (Crl1) regulated under GAP promoter (PGAP) using chemostat and fed-batch cultures. The results, also supported by transcriptional analysis of some target genes as marked novelty, demonstrated that production kinetics depends on the intrinsic characteristics of each clone used. Therefore, the selection of adequate µ for each case enables, in a different way, the rational process development to optimize RPP bioprocesses. Later, it was also evaluated the potential implementation of carbon-starving as innovative strategy to enhance the Crl1 production rates and yields on fed-batch cultures with a previous physiological characterization on chemostat cultivation. Results showed that positive effects observed using this strategy are highly dependent on the specific features of the clone used. An additional transcriptomic analysis (RNAseq) was carried out with chemostat samples, pointing out the difference on the transcription of all the genes of the yeast. In addition, bioprocess performance of the GAP promoter (PGAP) was compared with the inducible AOX1 promoter (PAOX1) by carrying out chemostat cultures producing Crl1. Although PAOX1 displayed higher production, an economical evaluation should be necessary before scale-up of the bioprocess, considering the numerous drawbacks of using methanol as substrate. Finally, following the strain engineering approach, it was characterized the use of two alternative methanol free novel promoters on the expression of lipase B from Candida antarctica (CalB) as strong tool that allows to exploit P. pastoris potential on RPP. Both promoters displayed much better production parameters than the observed with PGAP although the production pattern between promoters were significantly different on each case. Overall, the results presented along the different chapters of this current thesis support the usefulness of bioprocess and strain engineering through the different studies performed, which gave significant improvements in RPP efficiency. The knowledge of key factors involved on recombinant expression opens a window of new opportunities that allows P. pastoris to be established as a robust platform for RPP and showing it as highly competitive to conventional systems.
Gil, Gustavo Adolfo. "Online Raman spectroscopy for bioprocess monitoring." Thesis, Massachusetts Institute of Technology, 2005. http://hdl.handle.net/1721.1/36757.
Full textAuthor received the S.B. degree, June 2005 and the M. Eng. degree, Sept. 2005.
Includes bibliographical references (p. 195-202).
Online monitoring of bioprocesses is essential to expanding the potential of biotechnology. In this thesis, a system to estimate concentrations of chemical components of an Escherichia Coli fermentation growth medium via a remote fiber-optic Raman spectroscopy probe was studied in depth. The system was characterized to determine sources of instability and systematic error. A complete first-order error analysis was conducted to determine the theoretical sensitivity of the instrument. A suite of improvements and new features, including an online estimation of optical density and biomass, a method to correct for wavelength shifts, and a setup to increase repeatability and throughput for offline and calibration methods was developed accordingly. The theoretical and experimental ground work for developing a correction for spectrum distortions caused by elastic scattering, a fundamental problem for many spectroscopic applications, was laid out. In addition, offline Raman spectroscopy was used to estimate concentrations of fructose, glucose, sucrose, and nitrate in an oil palm (Elais guineensis) bioreaction. Finally, an expansion of optical techniques into new scale-up applications in plant cell bioprocesses, such as plant call differentiation was explored.
by Gustavo Adolfo Gil.
M.Eng.and S.B.
De, Beer Adrian. "Modelling and simulation based assessment in sustainable bioprocess development." Master's thesis, University of Cape Town, 2011. http://hdl.handle.net/11427/10365.
Full textVerster, Bernelle. "Exploring the factors at play to make wastewater biorefineries a reality." Doctoral thesis, Faculty of Engineering and the Built Environment, 2019. http://hdl.handle.net/11427/30090.
Full textDavids, Natasha. "An investigation into the enzymatic activity of deepsea actinobacteria in decolourising crystal violet dye." Master's thesis, Faculty of Engineering and the Built Environment, 2019. http://hdl.handle.net/11427/31145.
Full textMudenda, Lee. "Assessment of water pollution arising from copper mining in Zambia: a case study of Munkulungwe stream in Ndola, Copperbelt province." Master's thesis, University of Cape Town, 2018. http://hdl.handle.net/11427/27984.
Full textMoyo, Annah. "Characterizing the potential environmental risks of South African coal processing wastes." Master's thesis, University of Cape Town, 2018. http://hdl.handle.net/11427/29832.
Full textBooks on the topic "Bioprocess engineering"
Show, Pau Loke, Chien Wei Ooi, and Tau Chuan Ling, eds. Bioprocess Engineering. Boca Raton, FL : Taylor & Francis Group, 2019.: CRC Press, 2019. http://dx.doi.org/10.1201/9780429466731.
Full textFikret, Kargı, ed. Bioprocess engineering: Basic concepts. Englewood Cliffs, N.J: Prentice Hall, 1992.
Find full textFikret, Kargi, ed. Bioprocess engineering: Basic concepts. 2nd ed. Upper Saddle River, NJ: Prentice Hall, 2002.
Find full textPogaku, Ravindra, ed. Horizons in Bioprocess Engineering. Cham: Springer International Publishing, 2019. http://dx.doi.org/10.1007/978-3-030-29069-6.
Full textJerold, Manuel, Santhiagu Arockiasamy, and Velmurugan Sivasubramanian, eds. Bioprocess Engineering for Bioremediation. Cham: Springer International Publishing, 2020. http://dx.doi.org/10.1007/978-3-030-57911-1.
Full textSimpson, Ricardo, and Sudhir K. Sastry. Chemical and Bioprocess Engineering. New York, NY: Springer New York, 2013. http://dx.doi.org/10.1007/978-1-4614-9126-2.
Full textGalindo, Enrique, and Octavio T. Ramírez, eds. Advances in Bioprocess Engineering. Dordrecht: Springer Netherlands, 1994. http://dx.doi.org/10.1007/978-94-017-0641-4.
Full textGalindo, Enrique, and Octavio T. Ramírez, eds. Advances in Bioprocess Engineering. Dordrecht: Springer Netherlands, 1998. http://dx.doi.org/10.1007/978-94-017-0643-8.
Full textHu, Wei-Shou. Cell Culture Bioprocess Engineering. Edited by Wei-Shou Hu. Second edition. | Boca Raton : CRC Press, [2020]: CRC Press, 2020. http://dx.doi.org/10.1201/9780429162770.
Full textBook chapters on the topic "Bioprocess engineering"
Bellgardt, Karl-Heinz. "Bioprocess Models." In Bioreaction Engineering, 44–105. Berlin, Heidelberg: Springer Berlin Heidelberg, 2000. http://dx.doi.org/10.1007/978-3-642-59735-0_3.
Full textDochain, D., and M. Perrier. "Bioprocess Control." In Bioreaction Engineering, 145–66. Berlin, Heidelberg: Springer Berlin Heidelberg, 2000. http://dx.doi.org/10.1007/978-3-642-59735-0_6.
Full textRamalakshmi, Subbarayalu. "Cell Disruption." In Bioprocess Engineering, 1–14. Boca Raton, FL : Taylor & Francis Group, 2019.: CRC Press, 2019. http://dx.doi.org/10.1201/9780429466731-1.
Full textHu, Xing, and Peng Zhang. "Centrifugation." In Bioprocess Engineering, 15–25. Boca Raton, FL : Taylor & Francis Group, 2019.: CRC Press, 2019. http://dx.doi.org/10.1201/9780429466731-2.
Full textChia, Shir Reen, Winn Sen Lam, Wei Hon Seah, and Pau Loke Show. "Filtration." In Bioprocess Engineering, 27–54. Boca Raton, FL : Taylor & Francis Group, 2019.: CRC Press, 2019. http://dx.doi.org/10.1201/9780429466731-3.
Full textChew, Kit Wayne, Bervyn Qin Chyuan Tan, Jiang Chier Bong, Kevin Qi Chong Hwang, and Pau Loke Show. "Membrane-Based Separation Processes." In Bioprocess Engineering, 55–76. Boca Raton, FL : Taylor & Francis Group, 2019.: CRC Press, 2019. http://dx.doi.org/10.1201/9780429466731-4.
Full textYu, Kai Ling, Sho Yin Chew, Shuk Yin Lu, Yoong Xin Pang, and Pau Loke Show. "Reverse Osmosis." In Bioprocess Engineering, 77–101. Boca Raton, FL : Taylor & Francis Group, 2019.: CRC Press, 2019. http://dx.doi.org/10.1201/9780429466731-5.
Full textMuthuvelu, Kirupa Sankar, and Senthil Kumar Arumugasamy. "Chromatography." In Bioprocess Engineering, 103–42. Boca Raton, FL : Taylor & Francis Group, 2019.: CRC Press, 2019. http://dx.doi.org/10.1201/9780429466731-6.
Full textHiew, Billie Yan Zhang, Lai Yee Lee, Suchithra Thangalazhy-Gopakumar, and Suyin Gan. "Biosorption." In Bioprocess Engineering, 143–64. Boca Raton, FL : Taylor & Francis Group, 2019.: CRC Press, 2019. http://dx.doi.org/10.1201/9780429466731-7.
Full textLeong, Hui Yi, Pau Loke Show, K. Vogisha Kunjunee, Qi Wye Neoh, and Payal Sunil Thadani. "Liquid-Liquid Separation." In Bioprocess Engineering, 165–87. Boca Raton, FL : Taylor & Francis Group, 2019.: CRC Press, 2019. http://dx.doi.org/10.1201/9780429466731-8.
Full textConference papers on the topic "Bioprocess engineering"
Pischel, Dennis, Kai Sundmacher, and Robert J. Flassig. "Efficient Simulation of Variability and Heterogeneity in Bioprocess Engineering." In 9th Vienna Conference on Mathematical Modelling. ARGESIM Publisher Vienna, 2018. http://dx.doi.org/10.11128/arep.55.a55232.
Full textSaravanan, V., and S. Nagammai. "Intelligent controller implementation for a bioprocess." In 2017 IEEE International Conference on Electrical, Instrumentation and Communication Engineering (ICEICE). IEEE, 2017. http://dx.doi.org/10.1109/iceice.2017.8191935.
Full textXing, Xin-Hui, Pei-Xia Jiang, Cheng Yang, Ruiping Zhang, and Chong Zhang. "Reconstruction of Violacein Biosynthetic Pathway and Bioprocess for Violacein Production." In 14th Asia Pacific Confederation of Chemical Engineering Congress. Singapore: Research Publishing Services, 2012. http://dx.doi.org/10.3850/978-981-07-1445-1_069.
Full textMarenbach, P. "Evolutionary versus inductive construction of neurofuzzy systems for bioprocess modelling." In Second International Conference on Genetic Algorithms in Engineering Systems. IEE, 1997. http://dx.doi.org/10.1049/cp:19971200.
Full textTamagawa, Masaaki, and Ichiro Yamanoi. "Analysis of Deformation Process of a Bubble in a Cell Model by Shock Wave for Developing Drug Delivery Systems." In ASME 2004 International Mechanical Engineering Congress and Exposition. ASMEDC, 2004. http://dx.doi.org/10.1115/imece2004-59675.
Full textSharma, Chandra, Kanika Prasad, and Monika Sharma. "Various advanced applications of bioprocess engineering in the field of biomedical sciences—an insight." In The International Conference on Communication and Computing Systems (ICCCS-2016). Taylor & Francis Group, 6000 Broken Sound Parkway NW, Suite 300, Boca Raton, FL 33487-2742: CRC Press, 2016. http://dx.doi.org/10.1201/9781315364094-189.
Full textBaicu, Laurentiu, Sergiu Caraman, Laurentiu Frangu, and Mihaela Miron. "Measurement of the biomass concentration from a bioprocess by image processing techniques." In 2017 5th International Symposium on Electrical and Electronics Engineering (ISEEE). IEEE, 2017. http://dx.doi.org/10.1109/iseee.2017.8170681.
Full text"Potential of Grass for Biomethane Production in Anaerobic Digestion using Bioprocess Control AMPTS II." In 7th International Conference on Latest Trends in Engineering and Technology. International Institute of Engineers, 2015. http://dx.doi.org/10.15242/iie.e1115037.
Full textBaruch, I. S., E. E. Saldierna, and R. Galvan-Guerra. "Centralized anaerobic digestion bioprocess plant identification and direct I-term neural control using second order learning." In 2011 8th International Conference on Electrical Engineering, Computing Science and Automatic Control (CCE 2011). IEEE, 2011. http://dx.doi.org/10.1109/iceee.2011.6106671.
Full textWinkler, Wolfgang G., and Mark C. Williams. "Reversible Process Structures as a Base of Sustainable Engineering." In ASME 2011 International Mechanical Engineering Congress and Exposition. ASMEDC, 2011. http://dx.doi.org/10.1115/imece2011-65407.
Full textReports on the topic "Bioprocess engineering"
Mark A. Eiteman. Multidisciplinary Graduate Education in Bioprocess Engineering. Office of Scientific and Technical Information (OSTI), April 2006. http://dx.doi.org/10.2172/881268.
Full textClark, Elizabeth J., J. M. H. Levelt Sengers, and J. B. Hubbard. A survey of selected topics relevant to bioprocess engineering. Gaithersburg, MD: National Bureau of Standards, 1990. http://dx.doi.org/10.6028/nist.tn.1276.
Full text