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Literatura académica sobre el tema "Scale-up"

Autor: Grafiati

Publicado: 4 de junio de 2021

Última modificación: 20 de julio de 2024

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Artículos de revistas sobre el tema "Scale-up"

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Chen, C. F., J. D. Chen y H. Y. Lu. "Scale Up, Spice Up". Synfacts 2010, n.º 12 (22 de noviembre de 2010): 1362. http://dx.doi.org/10.1055/s-0030-1258934.

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Azimi, Reza, Tyler Fox, Wendy Gonzalez y Sherief Reda. "Scale-Out vs Scale-Up". ACM Transactions on Modeling and Performance Evaluation of Computing Systems 3, n.º 4 (15 de septiembre de 2018): 1–23. http://dx.doi.org/10.1145/3232162.

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Sutherland, I. A., L. Brown, A. S. Graham, G. G. Guillon, D. Hawes, L. Janaway, R. Whiteside y P. Wood. "Industrial Scale-Up of Countercurrent Chromatography: Predictive Scale-Up". Journal of Chromatographic Science 39, n.º 1 (1 de enero de 2001): 21–28. http://dx.doi.org/10.1093/chromsci/39.1.21.

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Prabowo, Benedictus, Se Yoon Kim, Dong Hoon Choi y Soo Hyun Kim. "Scale-up Polymerization of L-Lactide in Supercritical Fluid". Polymer Korea 35, n.º 4 (31 de julio de 2011): 284–88. http://dx.doi.org/10.7317/pk.2011.35.4.284.

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VOITH, MELODY. "CELLULOSIC SCALE-UP". Chemical & Engineering News 87, n.º 17 (27 de abril de 2009): 10–13. http://dx.doi.org/10.1021/cen-v087n017.p010.

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Craig Bettenhausen. "Biosurfactants scale up". C&EN Global Enterprise 102, n.º 3 (29 de enero de 2024): 13. http://dx.doi.org/10.1021/cen-10203-buscon3.

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Makwana, Vinit D., G. Sivalingam y Suketu M. Vakil. "Catalyst Evaluation and Scale-up Studies for Polyethylene Production". International Journal of Chemical Engineering and Applications 5, n.º 1 (2014): 6–12. http://dx.doi.org/10.7763/ijcea.2014.v5.341.

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Snidero, Silvia, Roberto Corradetti y Dario Gregori. "network scale-up method". Advances in Methodology and Statistics 1, n.º 2 (1 de julio de 2004): 395–405. http://dx.doi.org/10.51936/rufc6731.

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The network scale-up method is a social network estimator for the size of hidden or hard-to-count subpopulations. These estimators are based on a simple model which have however strong assumptions. The basic idea is that the proportion of the mean number of people known by respondent in a subpopulation E of T of size e is the same of the proportion that the e subpopulation E forms in general population T of size t: mc = t , where c is the number of persons known by each respondent and m is the mean number of persons known by each respondent in the subpopulation E. The persons known by every subject is called the "social network", and its size is c, estimated by several estimators proposed in the recent literature. In this paper we present a Monte Carlo simulation study aimed at understanding the behavior of the scale-up method type estimators under several conditions. The first goal was to understand what would be the ideal number of subpopulations of known size to be used in planning the research. The second goal was to analyze what happens when we use overlapped subpopulations. Our results showed that with the scale-up estimator we always obtain biased estimates for any number of subpopulations employed in estimates. With the Killworth's ML estimator, the improvement of scale-up method, we have substantially unbiased estimates under any condition. Also in case of overlapping, and increasing the degree of it among subpopulations, bias raises with scale-up method, instead it remains close to zero with ML estimator.

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MURAKAMI, Sei, Susumu HARADA y Shuichi YAMAMOTO. "Scale-Up of Fermenter". Japan Journal of Food Engineering 2, n.º 2 (15 de junio de 2001): 53–61. http://dx.doi.org/10.11301/jsfe2000.2.53.

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DeBenedictis, Erik P., Travis S. Humble y Paolo A. Gargini. "Quantum Computer Scale-up". Computer 51, n.º 10 (octubre de 2018): 86–89. http://dx.doi.org/10.1109/mc.2018.3971356.

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Tesis sobre el tema "Scale-up"

1

Wiggenhorn, Michael. "Scale-Up of Liposome Manufacturing". Diss., lmu, 2007. http://nbn-resolving.de/urn:nbn:de:bvb:19-84870.

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Mankosa, Michael James. "Scale-up of column flotation". Diss., This resource online, 1990. https://scholar.lib.vt.edu/ETD-db/ETD-catalog/manage_bound.

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Zauner, Rudolf. "Scale-up of precipitation processes". Thesis, University College London (University of London), 1999. http://discovery.ucl.ac.uk/1317927/.

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This thesis concerns the scale-up of precipitation processes aimed at predicting product particle characteristics. Although precipitation is widely used in the chemical and pharmaceutical industry, successful scale-up is difficult due to the absence of a validated methodology. It is found that none of the conventional scale-up criteria reported in the literature (equal power input per unit mass, equal tip speed, equal stirring rate) is capable of predicting the experimentally observed effects of the mixing conditions on kinetic rates and particle characteristics. As a result of high gradients in the supersaturation field during precipitation, particularly in the feed zone, high local gradients in the nucleation rate are to be expected. In this thesis, a compartmental mixing model (Segregated Feed Model SFM) linked to the population balance is proposed for scaling up both continuous and semibatch precipitation processes, and is validated with experiments on different scales. Experiments were carried out using two chemical systems (calcium oxalate CaC₂O₄ and calcium carbonate CaCO₃), varying the residence time/feed time, feed concentration, feed point position, impeller type, feed tube diameter and stirring rate in geometrically similar reactors ranging from 0.3 to 301. A new procedure is introduced in order to solve the inverse problem for determination of the kinetic parameters for nucleation, growth, disruption and agglomeration from the particle size distributions obtained in the continuous laboratory-scale experiments. This method, where the kinetic rates were extracted separately and sequentially from the particle size distribution, was found to be a reliable alternative to the conventional simultaneous estimation of all kinetic parameters from the distribution. Using the kinetic parameters extracted from the laboratory-scale experiments, the population balance is solved within the Segregated Feed Model. The local mixing parameters also required for solving the SFM are obtained from a sliding mesh Computational Fluid Dynamics (CFD) model. These are used to specify the different micromixing and mesomixing conditions in the feed and bulk zones of the reactor. The model accurately predicts the mean size, coefficient of variation and nucleation rate on different scales for different process and mixing conditions in both continuous and semibatch mode of operation. Furthermore, the model confirms the observed greater effect of mixing on product particle characteristics in semibatch than in continuous operation. This is thought to be due to direct mixing of the feed solution in semibatch operation with the other component already present in the reactor. The methodology proposed here for the scale-up of precipitation processes is very versatile and computationally efficient. It combines the advantages of both a CFD and a population balance approach without having to solve the equations together, which is currently still impracticable due to the excessive computational demand and simulation time required.

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Smith, Keith Buchanan. "Scale-up of oscillatory flow mixing". Thesis, University of Cambridge, 2000. https://www.repository.cam.ac.uk/handle/1810/238305.

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Oscillatory Flow Mixing is a recent development in mixing technology which has evolved over the past decade. It has a number of similarities to other mixing technologies, particularly pulsed and reciprocating plate columns, but at the laboratory scale has demonstrated a number of advantageous properties. These properties (such as control of residence time distribution, improved heat transfer and predictable mixing times) have been demonstrated at the laboratory scale for a wide range of different potential applications, but until now there has been a lack of firm understanding and research into how the technology could be scaled-up into an industrial scale process. This thesis addresses the problem of scale-up in Oscillatory Flow Mixing. It reports on a programme of experiments on geometrically scaled apparatus with the measurement of residence time distributions and flow visualisation as the principal methods of investigating the wide range of flow conditions that can be achieved by control of net flow and of oscillatory conditions. Results from these investigations are interpreted as axial dispersion coefficients and also compared with results obtained computationally using a fluid mechanics approach to simulate flow fields and the injection of inert tracers into those flow fields. Significant clarification is reported concerning the analysis of axial dispersion measurements using the diffusion model for which conflicting solutions were identified in the literature. The development of a flow visualisation technique using fluorescent dye streaklines is also reported. Using the latter technique stable manifolds in Oscillatory Flow Mixing have for the first time been experimentally observed as well as a range of other flow regimes. The study of scale-up was extended by the successful construction and investigation of an alternative reactor geometry with the potential for use in large-scale plant. From the work presented in the thesis it is concluded that Oscillatory Flow Mixing is a technology which in general lends itself readily to scaling-up from laboratory to pilot plant scale, and most probably to industrial scale. Experiments performed on small laboratory apparatus (containing less than one litre of fluid) can with confidence be used to predict mixing behaviour in much larger plant (containing hundreds of litres of fluid.)

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Colby, Christopher Brett. "Optimisation of scale-up of chromatography /". Title page, table of contents and abstract only, 1997. http://web4.library.adelaide.edu.au/theses/09PH/09phc686.pdf.

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Scholtzova, Angela. "Scale up and modelling of HPLC". Thesis, University College London (University of London), 2000. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.368109.

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Davis, Ryan Z. "Design and Scale-Up of Production Scale Stirred Tank Fermentors". DigitalCommons@USU, 2010. https://digitalcommons.usu.edu/etd/537.

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In the bio/pharmaceutical industry, fermentation is extremely important in pharmaceutical development, and in microbial research. However, new fermentor designs are needed to improve production and reduce costs of complex systems such as cultivation of mammalian cells and genetically engineered micro-organisms. Traditionally, stirred tank design is driven by the oxygen transfer capability needed to achieve cell growth. However, design methodologies available for stirred tank fermentors are insufficient and many times contain errors. The aim of this research is to improve the design of production scale stirred tank fermentors through the development of dimensionless correlations and by providing information on aspects of fermentor tanks that can aid in oxygen mass transfer. This was accomplished through four key areas. Empirical studies were used to quantify the mass transfer capabilities of several different reactors. Computational fluid dynamics (CFD) was used to assess the impact of certain baffle and impeller geometries. Correction schemes were developed and applied to the experimental data. Dimensionless correlations were created from corrected experimental data to act as a guide for future production scale fermentor design. The methods for correcting experimental data developed in this research have proven to be accurate and useful. Furthermore, the correlations found from the corrected experimental data in this study are of great benefit in the design of production scale stirred tank fermentors. However, when designing a stirred tank fermentor of a different size, further experimentation should be performed to refine the correlations presented.

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8

Coleman, Simon James. "Scale-up of enface electrochemical reactor systems". Thesis, University of Newcastle upon Tyne, 2015. http://hdl.handle.net/10443/3071.

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Photolithography, the standard pattern transfer technique, has many sustainable issues due to the application of a mask to the substrate. A ‘maskless’ pattern transfer method, called the Enface technique, has recently been proposed for metal plating and etching. This method introduces the idea of bringing a patterned tool and a substrate together in close proximity and a current or voltage is passed between them enabling metal to be selectively deposited or removed from the substrate. The process requires sufficient electrolyte agitation within a narrow inter-electrode gap and has previously been shown to hold in a vertical flow channel reactor. However, the process has to be adapted for tank-type systems for industrial implementation. Mass transfer during electrodeposition can be enhanced by ultrasonic waves. It has therefore been investigated whether this would be an appropriate agitation method for Enface. In order to scale-up the process, 3 types of Enface reactors were investigated; a vertical flow cell, a 500 ml lab-scale tank-type cell and an 18 L ultrasound plating tank. The limiting current technique was used to study the mass transfer in these systems. Electrodeposition of copper pattern features in 0.1 M CuSO4 was achieved in each of these geometries. The scalability was quantified by measuring the uniformity of deposit roughness and deposit thickness of the features across the substrate using profilometry. The lab-scale tank-type cell with a 20 kHz ultrasound probe was used to investigate the effect of ultrasound agitation within narrow inter-electrode gaps. Mass transfer correlations showed that turbulent flow becomes fully developed when using ultrasound in this narrow geometry. Limiting current experiments showed that relatively low ultrasound powers of 9 – 18 W/cm2 should be used and current distribution modelling showed that the ultrasound source should be placed no less than 30 mm from the substrate. Copper pattern features were deposited onto 10 mm diameter substrates and using long current pulses with bursts of ultrasound during the off-time was the most suitable plating mode. Specially designed electrode holders in the large-scale 18 L ultrasound tank was used to deposit copper patterns onto larger substrates. Features of μm-scale were deposited onto A7 size substrates, but there was an unacceptable variation in deposit thickness of ±80% due to the non-uniformity of the electrode gap across the plate. However, mm-scale features were successfully deposited onto A7 size substrates with an acceptable deposit thickness uniformity and deposit roughness uniformity of ±18% and ±40% respectively across the plate. Enface is therefore currently scalable for mm-scale features on substrates of this size.

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9

Heider, Patrick Louis. "Scale-up of continuous chemical synthesis systems". Thesis, Massachusetts Institute of Technology, 2013. http://hdl.handle.net/1721.1/86870.

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Thesis: Ph. D., Massachusetts Institute of Technology, Department of Chemical Engineering, 2013.
This electronic version was submitted by the student author. The certified thesis is available in the Institute Archives and Special Collections.
Cataloged from student-submitted PDF version of thesis.
Includes bibliographical references (pages 72-80).
Continuous flow systems for chemical synthesis have become increasingly important in the pharmaceutical and fine chemical industry in the past decade. Initially, this work was confined primarily to microfluidic systems, but recently there has been a growing demand for milliscale systems capable of making material for clinical trials and pilot plant testing. The objective of this thesis is to demonstrate a practical system to accomplish continuous chemical synthesis within the context of a fully integrated pilot plant. The plant provided a platform to test scaled-up membrane-based liquid-liquid separators which were studied in detail. Previous work demonstrated the use of microfiltration membranes to separate liquid-liquid systems by leveraging the dominance of interfacial tension over gravity at small scales. When scaling up, it was determined that pressure control was critical to the operation of the separators. A pressure control module was designed and integrated into the separator device to provide the appropriate conditions to guarantee separation. The separators required no outside control to accomplish separation when connected to various downstream conditions including pumps, backpressure controllers, and other separators. This allowed for easy design and operation of multistep processes such as solvent swaps and countercurrent extraction. The main accomplishment covered in this thesis is the building and operation of an integrated continuous manufacturing plant for a small molecule pharmaceutical product (aliskiren tablets). An advanced intermediate was continuously processed through two synthetic steps with workup which are detailed here. The remainder of the process purified and formulated the drug substance and formed the final tablet which met many key performance criteria. This work opens avenues to look at even more complex liquid-liquid and even gas-liquid separation processes. Improved processes for continuous manufacturing which make use of recycling, multistage extraction, and novel chemistries can build on the research performed here to further improve synthesis systems. These results demonstrate that continuous processes are possible even for complex, industrially-relevant products.
by Patrick Louis Heider.
Ph. D.

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10

Eraydin, Mert Kerem. "Scale-up of Using Novel Dewatering Aids". Diss., Virginia Tech, 2009. http://hdl.handle.net/10919/27990.

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Coal preparation plants use large quantities of water for cleaning processes. Upon cleaning, the spent water must be removed such that the final product moisture level meets market constraints. However, removal of free water from the surface of fine particles is difficult and costly, and often the results are less than desirable. Fine particles inherently have very large surface areas, and hence retain large amounts of water. Increased amounts of fines also cause denser particle packing, which creates relatively small capillaries in filter cakes and, thus, cause slower dewatering kinetics. As a result, dewatering costs for fine particles are much higher than for dewatering coarse particles. Considering the technical and economic issues associated with dewatering coal and mineral fines, an extensive matrix of laboratory- and pilot-scale dewatering tests have been conducted to evaluate the use of novel dewatering aids. The reagents are designed to lower the surface tension of water, increase the hydrophobicity of the particles to be dewatered, and increase the capillary radius by hydrophobic coagulation. All of these are designed to lower the moisture of the filter cakes produced in mechanical dewatering processes. Laboratory-scale dewatering tests confirmed that using the novel dewatering aids can lower the final cake moisture of coal by 20-50%, while increasing the dewatering kinetics. Several on-site, pilot-scale tests were conducted to demonstrate that the process of using the novel dewatering aids can be scaled. Based on the laboratory- and pilot-scale tests conducted, a scale-up model for the process of using the novel dewatering aids has been developed. It can predict the final cake moistures as a function of vacuum pressure, filtration time and specific cake weight. The model can be useful for the scale-up of vacuum disc filters (VDF) and horizontal belt filters (HBF). Simulation results indicate that dewatering aids can be very effective, especially when used in conjunction with HBF due to its ability to control cake thickness and drying cycle time independently. In light of the promising laboratory- and pilot-scale test results, an industrial demonstration of the novel dewatering aids has been conducted at the Smith Branch impoundment site, which contains 2.9 million tons of recoverable coal. When the reagent was used for dewatering flotation products using a VDF, the moisture content was reduced from 26 to 20% at 0.5 lb/ton of reagent addition and to 17.5% at 1 lb/ton. The use of the dewatering aid also improved the kinetics of dewatering, increased the throughput, and reduced the power consumption of vacuum pumps by 30%. The novel dewatering aids were also tested successfully for dewatering of kaolin clays. In this case, the mineral was treated with a cationic surfactant before adding the dewatering aids. This two-step hydrophobization process was able to reduce the cake moisture and also increase the throughput.
Ph. D.

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Libros sobre el tema "Scale-up"

1

Zlokarnik, Marko. Scale-up. Weinheim, FRG: Wiley-VCH Verlag GmbH & Co. KGaA, 2000. http://dx.doi.org/10.1002/352760328x.

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Stichlmair, Johann. Scale-up engineering. New York: Begell House, 2001.

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Kasuga, Yoshiko. World up-scale supermarkets. [Tokyo]: Shotenkenchiku-sha, 2000.

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1946-, Levin Michael, ed. Pharmaceutical process scale-up. 2^a ed. New York: Taylor & Francis, 2006.

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Kasuga, Yoshiko. World up-scale supermarkets. [Tokyo]: Shotenkenchiku-sha, 2000.

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L, Schneider Barbara y McDonald Sarah-Kathryn, eds. Scale-up in education. Lanham: Rowman & Littlefield Publishers, 2007.

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1946-, Levin Michael, ed. Pharmaceutical process scale-up. New York: Marcel Dekker, 2002.

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8

Scale-up in chemical engineering. Weinheim: Wiley-VCH, 2002.

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9

Johnson, David. Sart-up to scale up: Buying a business. [Charleston, S.C: Booksurge], 2008.

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Grezdo, Stanislav, Dusty Folwarczny y Terrence Karpowicz. Process of scale: Sizing up sculpture. Chicago: Ukrainian Institute of Modern Art, 2012.

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Capítulos de libros sobre el tema "Scale-up"

1

Biener, Richard. "Scale-up". En Fernstudium Master Biotechnologie, 67–87. Berlin, Heidelberg: Springer Berlin Heidelberg, 2018. http://dx.doi.org/10.1007/978-3-662-56727-2_2.

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Kossen, N. W. F. "Scale-up". En Advances in Bioprocess Engineering, 53–65. Dordrecht: Springer Netherlands, 1994. http://dx.doi.org/10.1007/978-94-017-0641-4_8.

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Dickey, David S. "Scale-Up". En Pharmaceutical Blending and Mixing, 345–68. Chichester, UK: John Wiley & Sons, Ltd, 2015. http://dx.doi.org/10.1002/9781118682692.ch13.

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Oliver-Hoyo, Maria y Robert Beichner. "Scale-Up". En Teaching and Learning Through Inquiry, 51–69. New York: Routledge, 2023. http://dx.doi.org/10.4324/9781003447351-7.

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Noorman, Henk. "Scale-Up and Scale-Down". En Fundamental Bioengineering, 463–98. Weinheim, Germany: Wiley-VCH Verlag GmbH & Co. KGaA, 2015. http://dx.doi.org/10.1002/9783527697441.ch16.

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Kohlgrüber, Klemens. "Scale-up and Scale-down". En Co-Rotating Twin-Screw Extruders: Applications, 87–138. München: Carl Hanser Verlag GmbH & Co. KG, 2020. http://dx.doi.org/10.3139/9781569907825.002.

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Kohlgrüber, Klemens. "Scale-up und Scale-down". En Der gleichläufige Doppelschneckenextruder, 535–89. München: Carl Hanser Verlag GmbH & Co. KG, 2016. http://dx.doi.org/10.3139/9783446435971.006.

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Kohlgrüber, Klemens. "Scale-up und Scale-down". En Der gleichläufige Doppelschneckenextruder, 535–89. München, Germany: Carl Hanser Verlag GmbH & Co. KG, 2016. http://dx.doi.org/10.1007/978-3-446-43597-1_6.

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Kohlgrüber, Klemens. "Scale-up and Scale-down". En Co-Rotating Twin-Screw Extruders: Applications, 87–138. München, Germany: Carl Hanser Verlag GmbH & Co. KG, 2021. http://dx.doi.org/10.1007/978-1-56990-782-5_2.

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Mahdinia, Ehsan, Deniz Cekmecelioglu y Ali Demirci. "Bioreactor Scale-Up". En Essentials in Fermentation Technology, 213–36. Cham: Springer International Publishing, 2019. http://dx.doi.org/10.1007/978-3-030-16230-6_7.

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Actas de conferencias sobre el tema "Scale-up"

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Gibbons, Phillip B. "Big data: Scale down, scale up, scale out". En 2015 IEEE International Parallel and Distributed Processing Symposium (IPDPS). IEEE, 2015. http://dx.doi.org/10.1109/ipdps.2015.123.

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Yoneki, Eiko y Amitabha Roy. "Scale-up graph processing". En SIGMOD/PODS'13: International Conference on Management of Data. New York, NY, USA: ACM, 2013. http://dx.doi.org/10.1145/2484425.2484433.

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Weisiger, Dan. "Scale-up considerations: Pilot to commercial scale". En The 13th NREL photovoltaics program review meeting. AIP, 1996. http://dx.doi.org/10.1063/1.49363.

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Appuswamy, Raja, Christos Gkantsidis, Dushyanth Narayanan, Orion Hodson y Antony Rowstron. "Scale-up vs scale-out for Hadoop". En SOCC '13: ACM Symposium on Cloud Computing. New York, NY, USA: ACM, 2013. http://dx.doi.org/10.1145/2523616.2523629.

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Mukundakrishnan, K., R. Gandham, K. P. Esler, D. Dembeck, J. Shumway y V. Natoli. "Scale Out vs. Scale Up for Ultra-Scale Reservoir Simulation". En Third EAGE Workshop on High Performance Computing for Upstream. Netherlands: EAGE Publications BV, 2017. http://dx.doi.org/10.3997/2214-4609.201702313.

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Kowalczyk, Alexandra, Sebastian Schwede, Mandy Gerber y Roland Span. "Scale Up of Laboratory Scale to Industrial Scale Biogas Plants". En World Renewable Energy Congress – Sweden, 8–13 May, 2011, Linköping, Sweden. Linköping University Electronic Press, 2011. http://dx.doi.org/10.3384/ecp1105748.

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Lake, L. W. "Scales, Scaling and Scale-Up". En IOR 2005 - 13th European Symposium on Improved Oil Recovery. European Association of Geoscientists & Engineers, 2005. http://dx.doi.org/10.3997/2214-4609-pdb.12.c25.

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E. Pickup, G. y K. D. Stephen. "Steady-State Scale-Up Models". En ECMOR VI - 6th European Conference on the Mathematics of Oil Recovery. European Association of Geoscientists & Engineers, 1998. http://dx.doi.org/10.3997/2214-4609.201406662.

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Goldman, Lee M., Mark Smith, Mohan Ramisetty, Uday Kashalikar, Santosh Jha y Suri Sastri. "Scale up of large ALON windows". En Window and Dome Technologies and Materials XVI, editado por W. Howard Poisl. SPIE, 2019. http://dx.doi.org/10.1117/12.2518899.

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Benjamin, Thomas G., Gennady L. Reznikov, Richard Donelson y Dennis N. Burmeister. "IMHEX® MCFC Stack Scale-Up". En 27th Intersociety Energy Conversion Engineering Conference (1992). 400 Commonwealth Drive, Warrendale, PA, United States: SAE International, 1992. http://dx.doi.org/10.4271/929162.

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Informes sobre el tema "Scale-up"

1

Davis, Jonathan M. V., Jonathan Guryan, Kelly Hallberg y Jens Ludwig. The Economics of Scale-Up. Cambridge, MA: National Bureau of Economic Research, octubre de 2017. http://dx.doi.org/10.3386/w23925.

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Bromberg, L., P. Titus, D. Cohn y C. Bolton. IGNITOR scale-up studies (DIGNITOR). Office of Scientific and Technical Information (OSTI), abril de 1990. http://dx.doi.org/10.2172/7185023.

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Orr, F. M. Jr. Scale-up of miscible flood processes. Office of Scientific and Technical Information (OSTI), junio de 1993. http://dx.doi.org/10.2172/10156622.

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Orr, F. M. Jr. Scale-up of miscible flood processes. Office of Scientific and Technical Information (OSTI), mayo de 1992. http://dx.doi.org/10.2172/5251677.

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Daniel, Richard C., Justin M. Billing, Maria L. Luna, Kirk J. Cantrell, Reid A. Peterson, Michael L. Bonebrake, Rick W. Shimskey y Lynette K. Jagoda. Characterization of Filtration Scale-Up Performance. Office of Scientific and Technical Information (OSTI), marzo de 2009. http://dx.doi.org/10.2172/962841.

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Orr, F. M. Scale-up of miscible flood processes. Office of Scientific and Technical Information (OSTI), junio de 1991. http://dx.doi.org/10.2172/5788092.

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Orr, Jr, F. Scale-up of miscible flood processes. Office of Scientific and Technical Information (OSTI), enero de 1990. http://dx.doi.org/10.2172/6842651.

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Louge, M. Y. Scale-up circulating fluidized bed coal combustors. Office of Scientific and Technical Information (OSTI), noviembre de 1991. http://dx.doi.org/10.2172/5520104.

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Pope, G., L. Lake y K. Sepehrnoori. Modelling and scale-up of chemical flooding. Office of Scientific and Technical Information (OSTI), marzo de 1990. http://dx.doi.org/10.2172/7014577.

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Baral, Arun y Ekin Birol. Catalyzing the scale-up of crop biofortification. Washington, DC: International Food Policy Research Institute, 2020. http://dx.doi.org/10.2499/p15738coll2.133959.

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