Gotowe bibliografie tematyczne / Transesterification

Gotowa bibliografia na temat „Transesterification”

Autor: Grafiati
Data publikacji: 4 czerwca 2021
Data aktualizacji: 7 lipca 2024

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Artykuły w czasopismach na temat "Transesterification"

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Otera, Junzo. "Transesterification". Chemical Reviews 93, nr 4 (czerwiec 1993): 1449–70. http://dx.doi.org/10.1021/cr00020a004.

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Masumizu, Tatsuya, Koohei Nozawa, Ken-ichi Kawai i Shoichi Nakajima. "Electrocatalytic transesterification". Tetrahedron Letters 27, nr 1 (styczeń 1986): 55–56. http://dx.doi.org/10.1016/s0040-4039(00)83938-6.

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Whitney, M. B., B. W. Hess, J. E. Kaltenbach, H. J. Harlow i D. C. Rule. "Direct transesterification of lipids from feedstuffs and ruminal bacteria". Canadian Journal of Animal Science 79, nr 2 (1.06.1999): 247–49. http://dx.doi.org/10.4141/a98-110.

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Direct transesterification of feedstuffs, browse plants, and ruminal bacteria was compared to transesterification of solvent extracted lipids. Weight percentages were of similar magnitude between procedures. Direct transesterification often produced higher concentrations of fatty acids. Results indicate that direct transesterification is an acceptable method for analysis of total fatty acids. Key words: Transesterification, lipids, feedstuffs, bacteria
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Wicakso, Doni Rahmat, Anniy Nurin Najma i Diah Ayu Retnowati. "CRUDE BIODIESEL SYNTHESIS FROM RUBBER SEED OIL". Konversi 7, nr 1 (25.11.2019): 21. http://dx.doi.org/10.20527/k.v7i1.4872.

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Abstract-Biodiesel is a diesel engine fuel made from oil containing triglycerides as well as rubber seed oil. This research aims to study how the extraction process of rubber seed oil, to know the effect of crude biodiesel manufacturing process by transesterification and esterification-transesterification and the addition of different catalysts on the transesterification process of crude biodiesel produced. Esterification process use H2SO4 catalyst and transesterification process use KOH and NaOH catalyst. The process of making crude biodiesel done by transesterification and can also by the merging of esterification-transesterification process. Based on this research, yield of crude biodiesel produced by transesterfication and esterification-transesterification by using NaOH catalyst is 38% and 75,6%, while yielded by KOH catalyst is 22,5% and 80%. While the acid number obtained from the transesterification process and esterification-transesterification using KOH catalyst is the same that is 1.33 and for the NaOH catalyst is 1,83 and 1,68. Saponification number obtained from both processes using KOH catalysts were 24,68 and 26,37 and for NaOH catalysts were 18,51 and 20,20. Keywords: Rubber seed oil, crude biodiesel, acid number, saponification number.
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Prošková, A., Z. Kopicová, J. Kučera i L. Škarková. "Acid catalysed transesterification of animal waste fat". Research in Agricultural Engineering 55, No. 1 (11.02.2009): 24–28. http://dx.doi.org/10.17221/20/2008-rae.

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Rendering plant fat (RPF) was collected and different conditions were used for transesterification. The course of transesterification of RPF was compared with that of transesterification of lard under the same conditions. Significant diffe-rences were found between transesterification of RPF and that of lard. Optimum methanol excess for lard transesterification was found to be 30-fold, for RPF 10-fold, optimum sulfuric acid concentration was 1% for lard, 2.5% for RPF. Optimum temperature as well as optimum reaction time were similar in both cases. The fatty acid composition is similar but not identical in both fats. RPF contains a higher amount of free acid which could be the reason for the differences observed.
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Bérešová, Miroslava, András Peller i Michal Horňáček. "Biodiesel preparation from Camelina sativa oil by homogeneous and heterogeneous transesterification". E3S Web of Conferences 545 (2024): 03001. http://dx.doi.org/10.1051/e3sconf/202454503001.

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Biodiesel is one of the possible alternatives to diesel fuel to address the issue of fossil fuels and their impact on the environment. Substituting homogeneous transesterification with heterogeneous offers advantages such as improved catalyst and product separation, catalyst regeneration, and avoidance of saponification during the reaction. To compare homogeneous and heterogeneous transesterification, the commonly used homogenous catalyst NaOH was tested. As a heterogeneous catalyst, a mixed oxide prepared from hydrotalcite with added nickel in its structure was used. By employing suitable conditions, it is possible to achieve biodiesel through heterogeneous transesterification with a comparable FAME (Fatty acid methyl ester) content to homogeneous transesterification, meeting the standardized value of over 96.7 wt.%. Implementing a two-step heterogeneous transesterification process decreases the reaction time needed to reach the desired FAME quantity. Furthermore, following heterogeneous transesterification, glycerol as a valuable secondary product showed visibly higher purity.
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Watcharakitti, Jidapa, Jaturavit Nimnuan, Kuakarun Krusong, Suwat Nanan i Siwaporn Meejoo Smith. "Insight into the Molecular Weight of Hydrophobic Starch Laurate-Based Adhesives for Paper". Polymers 15, nr 7 (31.03.2023): 1754. http://dx.doi.org/10.3390/polym15071754.

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Instead of using finite petroleum-based resources and harmful additives, starch can be used as a biodegradable, low-cost, and non-toxic ingredient for green adhesives. This work employs K3PO4 catalyzed transesterifications of cassava starch and methyl laurate at varying reaction times (1–10 h), resulting in the enhanced hydrophobicity of starch laurates. At longer reaction times, starch laurates having higher degrees of substitution (DS) were obtained. While starch laurates are the major products of transesterification, relatively low-molecular-weight byproducts (1%) were detected and could be hydrolyzed starches based on gel permeation chromatography results. Contact angle measurements confirmed the relatively high hydrophobicity of the modified starches compared with that of native starch. The modified starches were then employed to prepare water-based adhesives on paper (without any additional additives). Notably, the shear strength of the esterified starch adhesives appears to be independent of the DS of esterified samples, hence the transesterification reaction times. Additionally, the shear strength of water-based adhesives (0.67–0.73 MPa) for bonding to paper substrates is superior to that of two other commercially available glues by a factor of 10 to 80 percent.
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RITTER, STEVE. "FLUOROUS BIPHASIC TRANSESTERIFICATION". Chemical & Engineering News 79, nr 40 (październik 2001): 15. http://dx.doi.org/10.1021/cen-v079n040.p015.

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OTERA, J. "ChemInform Abstract: Transesterification". ChemInform 24, nr 39 (20.08.2010): no. http://dx.doi.org/10.1002/chin.199339347.

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Golmakani, M. T., M. Niakousari, A. Peykar i T. Safaeipour. "Microwave-assisted transesterification of sour cherry kernel oil for biodiesel production: comparison with ultrasonic bath-, ultrasonic probe-, and ohmic-assisted transesterification methods". Grasas y Aceites 75, nr 1 (10.04.2024): e545. http://dx.doi.org/10.3989/gya.0429231.

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In this study, sour cherry kernel oil was converted to biodiesel by microwave-assisted transesterification. Evaluations were made of several variables, namely, reaction time (1, 2, 3, 4, and 5 min), microwave power (100, 200, 300, 400, and 500 W), methanol/oil mole ratio (3, 6, 9, 12, and 15), and catalyst (KOH) concentration (0.3%, 0.6%, 0.9%, 1.2%, and 1.5%). The efficiency of fatty acid methyl esters increased in response to lengthier reaction times, greater microwave power, higher methanol/oil mole ratio, and higher catalyst concentrations up to the optimal level. The optimal reaction conditions for microwave-assisted transesterification were 300 W microwave power, 1.2% catalyst concentration, a methanol/oil mole ratio of 1:2, and a reaction time of 4 min. Microwave-assisted transesterification was more effective than ohmic-, magnetic stirrer-, ultrasonic probe-, and ultrasonic bath-assisted transesterification methods. In conclusion, microwave-assisted transesterification can be suggested as a fast, efficient, and economical method compared to other transesterification methods.
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Rozprawy doktorskie na temat "Transesterification"

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Hobson, James E. "Metal alkoxides as transesterification catalysts". Thesis, University of York, 2004. http://etheses.whiterose.ac.uk/10972/.

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Drummond, Graham R. "Novel oilfield polymers via transesterification reactions". Thesis, University of Strathclyde, 2007. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.436103.

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Balch, Brian Palmer. "Industrial Transesterification of Cultivated Algae for Biofuel". Thesis, The University of Arizona, 2016. http://hdl.handle.net/10150/612548.

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The objective of our design was to create a chemical plant that uses cultivated algae grown on site in order to produce a biofuel as an alternative energy source. Currently there is a push for sustainable energy sources and biologically produced fuels are attractive due to their near net-zero carbon emissions. Algae provides a valuable source of energy due to its growth rate and sustainability. Chemical engineering principles were utilized in design; a supercritical carbon dioxide extractor for the triglycerides in the algae cells, base catalyzed transesterification reaction in continuously stirred reactors in series and separation processes at the end in order to produce a high grade biofuel for consumer applications. Emphasis on environmental consideration also went into the design, such as the use of carbon dioxide for both the growth of the algae and solid extraction process and methanol used for the transesterification and liquid extraction, allowing for easy recycle and further reducing the environmental footprint the product fuel will have.
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LaRue, Kate, Brian Balch, Chris Jabczynski i Connor Swensen. "INDUSTRIAL TRANSESTERIFICATION OF CULTIVATED ALGAE FOR BIOFUEL". Thesis, The University of Arizona, 2016. http://hdl.handle.net/10150/613238.

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McCullagh, Cindy Marie. "Transesterification in blends of liquid crystalline copolyesters". Case Western Reserve University School of Graduate Studies / OhioLINK, 1995. http://rave.ohiolink.edu/etdc/view?acc_num=case1058534808.

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Tri, Rachmanto. "Monitoring of biodiesel transesterification process using impedance measurement". Thesis, Liverpool John Moores University, 2014. http://researchonline.ljmu.ac.uk/4337/.

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Alternative diesel fuels have been the subject of extensive investigation. Fatty acid methyl ester (FAME) based Biodiesel manufactured from vegetable oils or animal fats is an excellent candidate to replace common diesel fuel being renewable, non-toxic and often giving rise to reduced exhaust gas emissions. The transesterification process has been commonly and widely used to produce biodiesel from vegetable oil or animal fat. Vegetable oils or animal fats generally have viscosities higher than standard diesel oil. This means that it is necessary to reduce the viscosity by means of reacting vegetable oil with alcohol in the presence of a suitable catalyst. The target product for this reaction is methyl ester, with glycerol and potentially soap produced as by products with the process of transesterification. Methylester (Biodiesel) is produced by converting triglycerides to alkylesters. A batch transesterification process has two significant mechanisms, and exhibits a mass transfer controlled region that precedes a second order kinetically controlled region. In order to control the conversion process it is useful to employ process monitoring. In particular monitoring of the mass transfer processes that limits the initial reaction rates could prove to be beneficial in allowing for process optimization and control. This thesis proposes the use of a new method of biodiesel process monitoring using low frequency (15kHz) impedance sensing which is able to provide information regarding the progress of mass transfer and chemical reaction during biodiesel production. An interdigitated (ID) sensor has been used to monitoring the biodiesel process The ID sensor is of simple construction and consists of two sets of interleaved electrodes (fingers). The two sets of electrodes are separated by a gap and when an AC excitation voltage is applied across the interleaved electrodes an oscillating electric field is developed. The response of the fluid surrounding the sensor to the applied excitation was then used to determine progress of the chemical reaction by evaluating the real and complex impedance. A significant and unambiguous change in the components of impedance has been shown to occur during mixing (mass transfer) and transesterification. The impedance measurements gained during transesterification were then used for the development of a system model. A systematic approach was used to select mathematical models and system identification techniques were evaluated. The system identification investigation used real process measurement data in conjunction with the Matlab system identification toolbox.
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Sanvoisin, Jonathan. "Biotransformations using lipase enzymes in organic solvents". Thesis, Durham University, 1993. http://etheses.dur.ac.uk/5647/.

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Enzymatic transformations in organic solvents have received increasing attention over the past 10 years and lipases have become by far the most popular enzymes in this area.The initial aim of the research was to assess the effect of small modifications to the acyl donor in the transesterification reactions mediated by the Candida cylindracea lipase. 2.2.2-Trichloroethyl butyrate (TCEB) was used as a standard for the rate studies. In the event the acyl donor, trichloroethyl methoxyacetate (TCEMA), accelerated the transesterification reaction with hexan-1-ol by an order of magnitude over that with TCEB. This observation, and the absence of an acceleration with trichloroethyl methoxypropionate (and ethyl 2- fluorobutyrate over ethyl butyrate) suggested that the effect is due to the ~oxygen. A solvent activity profile indicated that the most hydrophobic solvents supported faster initial rates. This was attributed to the ability of the hydrophilic solvents to strip the hydrated water from the enzyme surface thus deactivating it. The switch to organic solvents allowed a wider temperature range to be studied. For the reactions between heptan-2-ol and TCEMA the reaction could be conducted in the temperature range -23 C to 80 C. It was of interest to assess how the alcohol moiety effected the transesterification reaction. A series of alcohols were presented to the enzyme and a pattern emerged with substrates containing an acetylene functionality being processed faster than those with a vinyl group, which were faster than those containing a methyl group (all other groups being the same). A series of heterocyclic alcohols were presented to the enzyme and it was observed that the order of reaction was thiophene > furan > pyridyl. The secondary alcohols in this series, 2-thiopheneethan-1-ol and o pyridylethan-1-ol, were resolved at various temperatures from -1soc to sooc with no variation in. enantioselectivity. These are the first resolutions to be accomplished at temperatures below zero degrees.
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Kasim, Farizul Hafiz. "In situ transesterification of Jatropha curcas for biodiesel production". Thesis, University of Newcastle Upon Tyne, 2012. http://hdl.handle.net/10443/1788.

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Biodiesel is primarily produced by transesterification of edible oils. Increasing concern about using food supplies for fuel has generated interest in alternative raw materials. Furthermore, there are numerous steps between harvesting of oilseeds and final production of biodiesel that can be integrated, thereby simplifying the process and making it more suitable for distributed production. Hence, in this study, the production of biodiesel via in situ transesterification of non-edible Jatropha curcas seed has been investigated. The main aim was to investigate the parameters of the process, with a view to reducing the substantial excess of methanol required. A significant secondary aim was to investigate the possibility of utilising other compounds that come out from the process. “Design of experiments” was employed to study the parameters at lab-scale, with the matrix boundary being determined beforehand using one-at-a-time experiments. The reduction of methanol excess was attempted by use of two co-solvents, hexane and diethylmethane (DEM), and by replacing methanol with methyl acetate. It was found that in situ transesterification run using particle sizes below 0.71 mm, a 400:1 molar ratio of methanol to oil, 60 minutes, and a minimum of 300 rpm mixing intensity yielded the highest biodiesel yield of 83 wt %. NaOH concentration and reaction temperature were not found to be significant variables, and were set at 1.0 N and 30oC respectively. DEM was a more effective co-solvent than hexane. The addition of DEM to the process at 400:1 molar ratio experiment increased the yield from 83 to 92 wt %. When methyl acetate was used to replace methanol, the requirement of molar ratio of solvent:oil reduced significantly to 175:1 to achieved 86.8 wt% of biodiesel. The solid meal was shown to contain substantial amounts of protein, making it a valuable co-product stream. Previously J. curcas meal had had little value as animal feed due to its toxicity, but this may be reduced or removed by this process.
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Cannon, Michael J. "Transesterification of poly(ethylene terephthalate) and bisphenol-A-polycarbonate". Thesis, Durham University, 2006. http://etheses.dur.ac.uk/2589/.

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Blends of Poly(ethylene terephthalate) (PET) and bisphenol-A-polycarbonate (PC) have been made by solution and melt blending and these blends were subject to isothermal heating to induce a transesterification reaction. The raw materials and products of this reaction have been studied by a variety of different methods to ascertain the chemical, physical and mechanical properties they possess. The conclusions drawn are listed below. PET and PC are immiscible but are compatibilised by transesterification. Transesterification is a second order reversible process and is fast only when water is present, when absent the rate of transesterification is so slow that little or no reaction is observed in after 60 minutes at 300 c. When water is present in the blend significant chain scission and degradation takes place, this is not observed in the absence of water• The material obtained from melt blending has a molecular weight higher than that of commercial PET and it is possible to increase it further by standard solid state polymerization techniques. The PC concentration in PET is critical to the existence and extent of crystallisation. PET blends containing 10% PC are not significantly stronger or weaker than commercial PET and perform very similarly to the yield point. PET blends containing 10% PC are less ductile than commercial PET and will therefore fail sooner when they have yielded under tension. PET blends containing 10% PC do not injection mould as well as commercial PET under conventional procedures for PET, surface crazing and voiding is observed.
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Jebrane, Mohamed. "Fonctionnalisation chimique du bois par transesterification des esters d'enol". Thesis, Bordeaux 1, 2009. http://www.theses.fr/2009BOR13833/document.

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Au cours de cette étude, une méthode inédite de fonctionnalisation chimique de la matière lignocellulosique a été développée. Des groupes acyles de taille et de fonctionnalité variées ont ainsi été greffés à l’intérieur du bois, grâce à une réaction de transestérification entre les esters d’énol et les groupes hydroxyles des polymères lignocellulosiques. Les greffages ont été confirmés grâce aux spectroscopies infrarouge et RMN du 13C en phase solide. La stabilité dimensionnelle du bois acétylé à partir de l’acétate de vinyle ainsi que sa résistance aux attaques fongiques a été également évaluée, de même que la photostabilité du bois estérifié à partir des esters de vinyle aromatiques
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Książki na temat "Transesterification"

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Wychen, S. Van. Determination of total lipids as fatty acid methyl esters (FAME) by in situ transesterification: Laboratory analytical procedure (LAP), issue date December 2, 2013. Golden, Colorado: National Renewable Energy Laboratory, 2013.

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Becker, Anita. Transesterification: Process, Mechanism and Applications. Nova Science Publishers, Incorporated, 2019.

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Zhou, Weiyang. Kinetics and phase behaviour of transesterification of triglycerides. 2006.

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Ying, Loo Hui. BIODIESEL FROM REFINED BLEACHED DEODORIZED Palm Kernel Oil: Transesterification. LAP Lambert Academic Publishing, 2011.

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Części książek na temat "Transesterification"

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Bodanszky, Miklos, i Agnes Bodanszky. "Transesterification". W The Practice of Peptide Synthesis, 167–68. Berlin, Heidelberg: Springer Berlin Heidelberg, 1994. http://dx.doi.org/10.1007/978-3-642-85055-4_22.

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Gooch, Jan W. "Transesterification". W Encyclopedic Dictionary of Polymers, 758. New York, NY: Springer New York, 2011. http://dx.doi.org/10.1007/978-1-4419-6247-8_12011.

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Harrison, P. G. "By Transesterification". W Inorganic Reactions and Methods, 331–32. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2007. http://dx.doi.org/10.1002/9780470145234.ch133.

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Raj, Samuel Paul, Pravin Raj Solomon i Baskar Thangaraj. "Catalysts for Transesterification". W Biodiesel from Flowering Plants, 567–631. Singapore: Springer Singapore, 2022. http://dx.doi.org/10.1007/978-981-16-4775-8_44.

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Ohshima, Takashi. "Tetranuclear Zinc Cluster-Catalyzed Transesterification". W New Horizons of Process Chemistry, 65–87. Singapore: Springer Singapore, 2017. http://dx.doi.org/10.1007/978-981-10-3421-3_6.

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da Cruz, Rosenira Serpa, Ivon Pinheiro Lôbo, José Faustino Souza de Carvalho Filho, Rafael Costa Amaral i Felipe Oliveira Souza. "Jatropha Oil Transesterification and Byproducts". W Jatropha, Challenges for a New Energy Crop, 509–35. New York, NY: Springer New York, 2012. http://dx.doi.org/10.1007/978-1-4614-4806-8_27.

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Chengareddy, P., S. Arumugam, P. H. Pavan Kumar Reddy i P. Madhan Mohan Reddy. "A Review on Ultrasonicated Transesterification Process". W Springer Proceedings in Materials, 579–85. Singapore: Springer Singapore, 2020. http://dx.doi.org/10.1007/978-981-15-6267-9_65.

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Zaman, Khurshid, Atta-Ur-Rahman i Saleh Shekhani. "Asymmetric Enzymatic Hydrolysis, Resolution and Transesterification". W Yearbook of Asymmetric Synthesis 1991, 202–14. Dordrecht: Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-011-0235-3_5.

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Fauzi, Ahmad Hafiidz Mohammad, Ramli Mat i Anwar Johari. "In-Situ Transesterification Reaction for Biodiesel Production". W Biomass and Bioenergy, 89–105. Cham: Springer International Publishing, 2014. http://dx.doi.org/10.1007/978-3-319-07578-5_5.

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Zighmi, Souad, Mohamed Bilal Goudjil, Salah Eddine Bencheikh i Segni Ladjel. "Biodiesel Production by Transesterification of Recycled Vegetable Oils". W Exergy for A Better Environment and Improved Sustainability 2, 183–95. Cham: Springer International Publishing, 2018. http://dx.doi.org/10.1007/978-3-319-62575-1_14.

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Streszczenia konferencji na temat "Transesterification"

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Lukasiewicz, Marcin. "Microwave assisted transesterification of β-cyclodextrin". W The 17th International Electronic Conference on Synthetic Organic Chemistry. Basel, Switzerland: MDPI, 2013. http://dx.doi.org/10.3390/ecsoc-17-c001.

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Ramadhani, Anggia Putri, Muhammad Hafizh Prashantyo, Thea Prastiwi Soedarmodjo i Arief Widjaja. "The effect UV-B mutation on biodiesel from microalgae Botryococcus braunii using esterification, transesterification and combination of esterification-transesterification". W THE 5TH INTERNATIONAL CONFERENCE ON INDUSTRIAL, MECHANICAL, ELECTRICAL, AND CHEMICAL ENGINEERING 2019 (ICIMECE 2019). AIP Publishing, 2020. http://dx.doi.org/10.1063/5.0000554.

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"Kinetic study for biodiesel production from dairy waste via catalytic microwave heating". W Sustainable Processes and Clean Energy Transition. Materials Research Forum LLC, 2023. http://dx.doi.org/10.21741/9781644902516-34.

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Abstract. Biodiesel production from waste such as wastewater sludge, palm oil mill effluent and dairy waste provide more sustainable approach and greener energy. This paper analyzes the kinetic modelling for biodiesel production from dairy waste scum oil via microwave heating transesterification. The results from this study show that transesterification of dairy waste scum oil is a first order kinetic which defines that the biodiesel production is dependent on the concentration of one reactant linearly. The activation energy for the reaction was validated to be 18.12 J/mol and frequency factor was 3.163 s-1. It is validated that the activation energy of transesterification process in this study is lower than the past works have been done. The comparison of the value is as tabulated in the kinetic analysis section.
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Hsiao, Ming-Chien, Pei-Hung Liao i Hsiu-Ling Hsu. "Microwave-Assisted Heterogeneous Catalytic Transesterification of Soybean Oil". W 2012 International Symposium on Computer, Consumer and Control (IS3C). IEEE, 2012. http://dx.doi.org/10.1109/is3c.2012.98.

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ALI, FAKKRUDEEEN, i HARIPRASAD VP. "Enhancement of Co Solvent Transesterification Using Reactive Distillation". W Sixth International Conference on Advances in Applied Science and Environmental Technology - ASET 2017. Institute of Research Engineers and Doctors, 2017. http://dx.doi.org/10.15224/978-1-63248-119-1-67.

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Mockel, Wayne D., i Mark P. Thomas. "Determination of transesterification reaction endpoint using NIR spectroscopy". W SPIE's 1992 Symposium on Process Control and Monitoring, redaktorzy David S. Bomse, Harry Brittain, Stuart Farquharson, Jeremy M. Lerner, Alan J. Rein, Cary Sohl, Terry R. Todd i Lois Weyer. SPIE, 1992. http://dx.doi.org/10.1117/12.137739.

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Shengwei Cai, Xuan Zhou, Jiangbo Chen, Hui Yu i Cuijuan Zhou. "Transesterification reaction reduce viscosity of vegetable insulating oil". W 2012 International Conference on High Voltage Engineering and Application (ICHVE). IEEE, 2012. http://dx.doi.org/10.1109/ichve.2012.6357102.

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Shanmughom, Rupesh, i Shreyas K. Raghu. "Purification strategies for crude glycerol: A transesterification derivative". W LOW RADIOACTIVITY TECHNIQUES 2022 (LRT 2022): Proceedings of the 8th International Workshop on Low Radioactivity Techniques. AIP Publishing, 2023. http://dx.doi.org/10.1063/5.0155313.

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Xu, Guizhuan, Xiaoyan Cui, Shuaiyao Fan, Bailiang Zhang, Huamin Song, Xiaobin Yan, Xiaoqin Ma i Dechuan Kong. "Optimization of Transesterification of Beef Tallow for Biodiesel Production". W 2011 Asia-Pacific Power and Energy Engineering Conference (APPEEC). IEEE, 2011. http://dx.doi.org/10.1109/appeec.2011.5749079.

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Supriadi, Eko, Lenny Marlinda, Danawati Hari Prajitno i Mahfud Mahfud. "Transesterification of coconut oil for FAME production using ultrasound". W INTERNATIONAL SEMINAR ON FUNDAMENTAL AND APPLICATION OF CHEMICAL ENGINEERING 2016 (ISFAChE 2016): Proceedings of the 3rd International Seminar on Fundamental and Application of Chemical Engineering 2016. Author(s), 2017. http://dx.doi.org/10.1063/1.4982274.

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Raporty organizacyjne na temat "Transesterification"

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Van Wychen, Stefanie, Kelsey Ramirez i Lieve M. L. Laurens. Determination of Total Lipids as Fatty Acid Methyl Esters (FAME) by in situ Transesterification: Laboratory Analytical Procedure (LAP). Office of Scientific and Technical Information (OSTI), styczeń 2016. http://dx.doi.org/10.2172/1118085.

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Możesz być także zainteresowany rozszerzonymi bibliografiami na temat „Transesterification” dla poszczególnych typów źródeł:
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