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Relevant bibliographies by topics / Reactive extraction

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Academic literature on the topic 'Reactive extraction'

Author: Grafiati

Published: 4 June 2021

Last updated: 18 February 2022

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Journal articles on the topic "Reactive extraction"

1

Adams, Thomas A., and Warren D. Seider. "Semicontinuous reactive extraction and reactive distillation." Chemical Engineering Research and Design 87, no. 3 (March 2009): 245–62. http://dx.doi.org/10.1016/j.cherd.2008.08.005.

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Cascaval, Dan, and Anca-Irina Galaction. "New extraction techniques on bioseparations: 1. Reactive extraction." Chemical Industry 58, no. 9 (2004): 375–86. http://dx.doi.org/10.2298/hemind0409375c.

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The complexity of downstream processes for biosynthetic products constitutes a particularity of industrial biotechnologies, especially because of the biosynthetic product high dilution in fermentation broth, their chemical and thermal liability and the presence of secondary products. For these reasons, new separation techniques have been developed and applied to bioseparations. Among them, reactive extraction, pertraction (extraction and transport through liquid membranes) and direct extraction from broths have considerable potential and are required for the further development of many biotechnologies. This review is structured on two parts and presents our original results of the studies on the separation of some biosynthetic products (antibiotics, carboxylic acids, amino acids, alcohols) by reactive extraction in the first part, and by pertraction and direct extraction from broths without biomass filtration in the second. For all the analyzed cases, these extraction techniques simplify the technologies by reducing material and energy consumption, by avoiding product inhibition, by increasing the separation selectivity, therefore decreasing the overall cost of the product.

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Hano, Tadashi, Michiaki Matsumoto, Takaaki Ohtake, and Fumiaki Hori. "Reactive extraction of cephalosporin C." JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 25, no. 3 (1992): 293–97. http://dx.doi.org/10.1252/jcej.25.293.

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Lavie, Ram. "Kinetic Reactive Thin Layer Extraction." Industrial & Engineering Chemistry Research 53, no. 47 (November 12, 2014): 18283–90. http://dx.doi.org/10.1021/ie5026387.

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5

Marchitan, Natalia. "Reactive Extraction of Tartaric Acid." Chemistry Journal of Moldova 4, no. 2 (December 2009): 28–33. http://dx.doi.org/10.19261/cjm.2009.04(2).15.

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The present paper describes the results of reactive extraction of tartaric acid in model systems, which can be used for its separation from secondary wine products. As extractant have been used a normal/isododecyl mixed secondary amine Amberlite LA-2. The following parameters of the separation process have been varied: nature of diluent and modifier; modifier concentration; concentration, temperature and pH of the tartaric acid solution and the stirring time, and the work intervals have been established. It was concluded that in determinated conditions the extent of tartaric acid extraction attains value 85-95%.

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Zahari, Mohamed Shahrir Mohamed, Mohd Zamri Ibrahim, Su Shiung Lam, and Ramli Mat. "Prospect of Parallel Biodiesel and Bioethanol Production from JatrophaCurcas Seed." Applied Mechanics and Materials 663 (October 2014): 44–48. http://dx.doi.org/10.4028/www.scientific.net/amm.663.44.

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This study focuses on the utilization prospect of JatrophaCurcas seed solely as transport sector renewable fuel for producing biodiesel and bioethanol in a parallel system. Diesel (biodiesel) and petrol (bioethanol as petrol additive) engine fuel could be produce from J. Curcas seed oil portion and its’ seed residue, respectively. Ultrasonic-assisted reactive extractions were used for simultaneous oil extraction and esterification/transesterification of J. Curcas seed. The use of acid/alkaline catalyst and ultrasound resulted in a completely de-oiled seed residual by extracting about 50% oil which is equivalent to the Soxhlet extraction performance. The seeds were being chemically and physically characterized with ultimate analyses and TGA for its suitability as bioethanol raw material. Ultimate analyses revealed similarity with other bioconversion feedstock having carbon and oxygen as the major chemical compositions; with slightly lower carbon content in the residuals due to the oil extraction during the in-situ process. However, TG profile exhibited better decomposition of mass in the ultrasonicated residues having easier accessible and better degradable fiber for bioethanol production process. These shown positive effects on the J. Curcasseed pre-treatment during biodiesel reactive extraction process and for further bioconversion toward bioethanol.

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Pahari, Pradip K., and Man Mohan Sharma. "Recovery of morpholine via reactive extraction." Industrial & Engineering Chemistry Research 30, no. 8 (August 1991): 2015–17. http://dx.doi.org/10.1021/ie00056a054.

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Galaction, A. I., M. Postaru, A. Tucaliuc, I. Ungureanu, and D. Cascaval. "Reactive extraction of 6-aminopenicillanic acid." New Biotechnology 44 (October 2018): S138. http://dx.doi.org/10.1016/j.nbt.2018.05.1102.

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Bart, H. J., C. Drumm, and M. M. Attarakih. "Process intensification with reactive extraction columns." Chemical Engineering and Processing: Process Intensification 47, no. 5 (May 2008): 745–54. http://dx.doi.org/10.1016/j.cep.2007.11.005.

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Pascalis Novalina, Arya Josua S, Taslim, and Tjahjono Herawan. "PENGARUH VARIASI VARIABEL REAKSI PADA PROSES EKSTRAKSI REAKTIF MESOKARP SAWIT UNTUK MENGHASILKAN BIODIESEL." Jurnal Teknik Kimia USU 4, no. 4 (December 24, 2015): 18–24. http://dx.doi.org/10.32734/jtk.v4i4.1509.

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The conventional method for the production of biodiesel needed the oil that is extracted from the biomass before it can be transesterified into fatty acid methyl esters (FAME). Reactive extraction can be used to produce biodiesel with high-yield, low production costs, reduce the reaction time and the use of reagents and co-solvents, making it easier to produce biodiesel. In this study, reactive extraction applied to produce biodiesel from palm fruit mesocarp extracted using dimethyl carbonate as a solvent and reagents, and novozym®435 as a catalyst. Methanol was replaced by dialkyl carbonates, particularly dimethyl carbonate. Dimethyl carbonate can be used as a solvent and as a reagent, so reactive extraction is very easy to apply. The parameters will be study are reaction temperature (50, 60, and 70 °C), reaction time (8, 16, 24 hours), the molar ratio of reactants (50: 1, 60: 1, 70: 1 n/n ), the concentration of novozym® 435 (5%, 10%, 15% wt).The results showed that the highest biodiesel yield can be achivied at conditions temperature of 60 °C, reaction time 24 hours, molar ratio of reactants palm mesocarp to DMC 1:60, and novozym®435 concentration of 10wt%. The results showed that the synthesis of biodiesel via reactive extraction using palm mesocarp as raw material requires a low production cost.

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Dissertations / Theses on the topic "Reactive extraction"

1

Lukhezo, Muchinyarawo. "Reactive solvent extraction of amino acids." Thesis, London South Bank University, 1998. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.245090.

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Zakaria, Rabitah. "Reactive Extraction of Rapeseed for Biodlesel Production"." Thesis, University of Newcastle upon Tyne, 2010. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.525042.

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Salam, Kamoru Adio. "Reactive extraction of microalgae for biodiesel production." Thesis, University of Newcastle upon Tyne, 2015. http://hdl.handle.net/10443/3088.

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Fatty acid methyl ester (FAME “biodiesel”) is a renewable transport fuel that can be produced from waste/refined oil, pre-extracted oil from oilseeds or microalgae. The most common method converts extracted oil from biomass to FAME through transesterification using acidified or alkalised methanol. Alternatively, FAME can be made by contacting the oil-bearing biomass directly with an alcohol containing a catalyst. This approach is potentially a cost-effective alternative way of making algal FAME due to its elimination of the solvent extraction step and its higher water tolerance. This study reports reactive extraction of Nannochloropsis occulata and Chlorella vulgaris for FAME production using NaOH, H2SO4, zirconium dodecyl sulphate (“ZDS”) or H2SO4/SDS (a surfactant) as catalysts. It is possible to produce FAME using all of them. A relationship was found between FAME yield, catalyst concentration, methanol to oil molar ratio, moisture content or algal cell wall chemistry. NaOH is the most effective catalyst, producing high FAME yields (96 %) in relatively short reaction times (10 min), at 925:1 methanol to oil molar ratio and 0.5N NaOH. This was achieved despite high levels of free fatty acid (6 % lipid) in Chlorella vulgaris. A numerical model derived by Eze et al. (2014) fitted with experimental data from this study shows that other side reactions including FAME and triglyceride saponification, free fatty acid neutralisation occur alongside the desired FAME synthesis in a NaOH-catalysed reactive extraction. Regardless of the catalysts used, methanol to oil molar ratios in the range 600:1-1277:1 caused 5-30 wt %/(wt dry algae) moisture tolerance: significantly greater than the 0.5 wt % oil moisture required in conventional transesterifications. Both the phosphorus mass balance and conversion of the isolated algal phospholipids into FAME revealed that pre-soaking pre-treatment solubilises the phospholipid bilayer to some degree, and iii [Abstract continued] contributes to an increased FAME yield in Nannochloropsis occulata (98.4 %) and Chlorella vulgaris (93.4 %). Residual protein loss in Chlorella vulgaris and Nannochloropsis occulata were respectively 6.5 and 10 %. The carbohydrate content was significantly reduced by 71 % in Chlorella vulgaris and 65 % in Nannochloropsis occulata.

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Pfeuffer, Bernhard [Verfasser]. "Process intensification by heterogeneous reactive extraction / Bernhard Pfeuffer." Clausthal-Zellerfeld : Universitätsbibliothek Clausthal, 2012. http://d-nb.info/1021739839/34.

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Rambocus, Subhas. "Reactive solvent extraction of dicarboxylic and carboxylic-sulfonic acids." Thesis, London South Bank University, 1997. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.245144.

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6

Willersinn, Stefan [Verfasser]. "Reactive Extraction Kinetics in a Membrane-based Microcontactor / Stefan Willersinn." Aachen : Shaker, 2017. http://d-nb.info/1149278234/34.

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McGillivary, Angela. "Reactive solvent extraction of #beta#-lactam antibiotics and other anions." Thesis, London South Bank University, 1999. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.326763.

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8

Xu, Xin. "Direct conversion of carboxylate salts to carboxylic acids via reactive extraction." Texas A&M University, 2008. http://hdl.handle.net/1969.1/86006.

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The MixAlco process, a proprietary technology owned by Texas A&M University, converts biomass (e.g., municipal solid waste, sewage sludge, paper, agricultural residues, and energy crops) into usable chemicals (e.g., acetic acid) and fuels (e.g., ethanol). Historically, calcium carbonate has been used as the buffer. Recently, it was found that using ammonium bicarbonate as the buffering agent enhances the fermentation conversion. In this case, fermentation broth contains ammonium salts (e.g., ammonium acetate, propionate, butyrate, pentanoate). Therefore, the downstream processing steps (including extraction, purification, esterification, and product separation) must be compatible with the ammonium carboxylate salts formed in the fermentation. This research focuses on converting fermentation broth carboxylate salts into their corresponding acids via "acid springing." Reactive extraction and thermal conversion (distillation) are crucial parts of the acid springing process. Because the components of the fermentation broth are over 80% ammonium acetate and 20% other ammonium carboxylate salts (ammonium propionate, butyrate, pentanoate, etc.), all the initial experiments in this study were performed using reagentgrade ammonium acetate to simplify the reaction. Later, actual fermentation broth was employed. The primary objective of this study was to provide the optimal operating conditions to make the downstream processing steps of the MixAlco process compatible with ammonium carboxylate salts formed in the fermentation. The optimal initial concentration for reactive extraction should be 150-200 g/L and the volume ratio of aqueous phase and extractant should be 1:1. The distribution coefficient reaches the maximum value when the concentration of TOA is 20% (vol %) in n-octanol. The batch distillation study shows that there are two reaction stages: (1) water leaves the system at 100-106 °C and (2) the acid-amine complex decomposes at 160-180 °C.

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9

Marbaugh, Kelly Renee. "Theoretical and Experimental Studies on Simultaneous-Isomerization and Reactive-Extraction Followed By Back-Extraction of Biomass Hydrolysate sugars." University of Toledo / OhioLINK, 2015. http://rave.ohiolink.edu/etdc/view?acc_num=toledo1449876597.

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10

Acan, Basak. "Equilibrium Studies On The Reactive Extraction Of Lactic Acid From Fermentation Broth." Master's thesis, METU, 2003. http://etd.lib.metu.edu.tr/upload/1120781/index.pdf.

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Lactic acid recovery from dilute fermentation broths is a growing requirement due to the increasing demand for pure lactic acid. Reactive extraction is proposed as an alternative to conventional methods of recovery, since the selectivity of separation is remarkably enhanced in reactive extraction. The aim of this study is to perform the equilibrium studies for the recovery of lactic acid from its synthetic aqueous solutions (not from real fermentation broths) by reactive extraction and investigate the effects of various parameters such as initial lactic acid concentration in the aqueous phase (0.25 - 1.3 M), initial pH of the aqueous phase (2 &ndash
6), organic phase extractant concentration (0.1 &ndash
0.5 M), type of the extractant (chloride, hydrogensulphate and hydroxide salts of tri-n-octylmethylammonium) and the type of diluent (oleyl alcohol or octanol). The results of the experiments showed that the degrees of extraction decreased with increasing use of diluent with the extractant and increasing initial lactic acid concentration of the aqueous phase. Highest degrees of extraction were achieved for undiluted extractants. The performance of the diluents were investigated by performing extraction experiments with solutions of TOMAC in oleyl alcohol or octanol at different pH values and it was observed that octanol had a higher solvating power than oleyl alcohol especially at lower aqueous phase pH values. Higher extraction efficiencies were obtained for TOMAC dissolved in octanol rather than oleyl alcohol. Initial aqueous pH of 6 was identified as the optimum pH for the extraction, also due to its being equal the average fermentation pH for the extractions with Lactobacillus species. Among the different salts of tri-n-octylmethylammonium, hydroxide salt exhibited the highest degrees of extraction (83% with undiluted TOMA(OH) and 78% with 0.5 M TOMA(OH) in octanol for the extraction of 0.316 M lactic acid solutions). The present work is the first step in the design of an industrial reactive extraction process that is going to attempt forward and backward extraction of lactic acid simultaneously in a hollow fiber membrane module that is going to be attached to the lactic acid fermentor to achieve continuous product recovery. The equilibrium data obtained from this study can be combined with the kinetic studies as the next step of designing a separation module.

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Books on the topic "Reactive extraction"

1

Bart, Hans-Jörg. Reactive Extraction. Berlin, Heidelberg: Springer Berlin Heidelberg, 2001.

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Bart, Hans-Jörg. Reactive Extraction. Berlin, Heidelberg: Springer Berlin Heidelberg, 2001. http://dx.doi.org/10.1007/978-3-662-04403-2.

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3

Kuzmanovic, Boris. Reactive extraction of oxygenates with aqueous salt solutions. [S.l: s.n.], 2003.

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4

Mishra, Brajendra, ed. Review of Extraction, Processing, Properties & Applications of Reactive Metals. Hoboken, NJ, USA: John Wiley & Sons, Inc., 1999. http://dx.doi.org/10.1002/9781118788417.

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5

Steensma, Maria. Chiral separation of amino-alcohols and amines by fractional reactive extraction. [S.l: s.n.], 2005.

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6

International, Symposium on Extraction and Processing of Trace and Reactive Metals (1995 Las Vegas Nev ). Trace and reactive metals--processing and technology: Proceedings of International Symposium on Extraction and Processing of Trace and Reactive Metals. Warrendale, Pa: TMS, 1995.

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International Symposium on Extraction and Processing of Trace and Reactive Metals (1995 Las Vegas, Nev.). Trace and reactive metals: Processing and technology : proceedings of International Symposium on Extraction and Processing of Trace and Reactive Metals. Warrendale, Pa: Minerals, Metals & Materials Society, 1995.

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8

Vignes, Alain. Extractive metallurgy: Metallurgical reaction processes. London: ISTE, 2011.

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9

Minerals, Metals and Materials Society. Meeting. Refractory metals: Extraction, processing and applications : proceedings of a symposium sponsored by the Reactive Metals Committee, held at the Annual Meeting of the Minerals, Metals & Materials Society in New Orleans, February 17-21, 1991. Warrendale, Pa: The Society, 1990.

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Refractory Metals Symposium (1991 New Orleans). Refractory metals: Extraction, processing and applications : proceedings of a symposium sponsored by the Reactive Metals Committee, held at the annual meeting of the Minerals, Metals & Materials Society in New Orleans, February 17-21, 1991. Warrendale, PA: Minerals, Metals & Materials Society, 1991.

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Book chapters on the topic "Reactive extraction"

1

Bart, Hans-Jörg. "Reactive Extraction." In Reactive Extraction, 1–16. Berlin, Heidelberg: Springer Berlin Heidelberg, 2001. http://dx.doi.org/10.1007/978-3-662-04403-2_1.

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Bart, Hans-Jörg. "Reactive Mass Transfer." In Reactive Extraction, 51–130. Berlin, Heidelberg: Springer Berlin Heidelberg, 2001. http://dx.doi.org/10.1007/978-3-662-04403-2_3.

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Bart, Hans-Jörg. "Liquid-Liquid Phase Equilibria." In Reactive Extraction, 17–50. Berlin, Heidelberg: Springer Berlin Heidelberg, 2001. http://dx.doi.org/10.1007/978-3-662-04403-2_2.

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Bart, Hans-Jörg. "Current Developments and Apparatus Techniques." In Reactive Extraction, 131–49. Berlin, Heidelberg: Springer Berlin Heidelberg, 2001. http://dx.doi.org/10.1007/978-3-662-04403-2_4.

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Kiss, Anton Alexandru. "Reactive Extraction Technology." In Process Intensification Technologies for Biodiesel Production, 77–86. Cham: Springer International Publishing, 2014. http://dx.doi.org/10.1007/978-3-319-03554-3_7.

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Lee, Keat T., and Steven Lim. "Reactive Extraction Technology." In Process Intensification for Green Chemistry, 275–87. Chichester, UK: John Wiley & Sons, Ltd, 2013. http://dx.doi.org/10.1002/9781118498521.ch10.

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Thorgule, A., and R. P. Ugwekar. "Reactive Extraction of Propionic Acid." In Novel Water Treatment and Separation Methods, 191–99. Toronto ; Waretown, NJ : Apple Academic Press, 2017. | "Outcome of national conference REACT- 16, organized by the Laxminarayan Institute of Technology, Nagpur, Maharashtr , India, in 2016"--Introduction. || Includes bibliographical references and index.: Apple Academic Press, 2017. http://dx.doi.org/10.1201/9781315225395-14.

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Bart, Hans-Jörg. "Reactive Extraction: Principles and Apparatus Concepts." In Integrated Chemical Processes, 313–37. Weinheim, FRG: Wiley-VCH Verlag GmbH & Co. KGaA, 2005. http://dx.doi.org/10.1002/3527605738.ch10.

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Harris, Tim A. J., Simi Khan, Bryan G. Reuben, and Tina Shokoya. "Reactive Solvent Extraction of Beta-Lactam Antibiotics." In Separations for Biotechnology 2, 172–80. Dordrecht: Springer Netherlands, 1990. http://dx.doi.org/10.1007/978-94-009-0783-6_19.

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Gambogi, Joseph, and S. J. Gerdemann. "Titanium Metal: Extraction to Application." In Review of Extraction, Processing, Properties & Applications of Reactive Metals, 175–210. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2013. http://dx.doi.org/10.1002/9781118788417.ch5.

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Conference papers on the topic "Reactive extraction"

1

Karimi-Ghartemani, Masoud, and Hossein Mokhtari. "Extraction of Harmonics and Reactive Current for Power Quality Enhancement." In 2006 IEEE International Symposium on Industrial Electronics. IEEE, 2006. http://dx.doi.org/10.1109/isie.2006.295821.

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Niza, N. M., and M. H. Hamzah. "Influence of seed particle sizes on extraction and reactive extraction for biodiesel production from cotton and palm kernel seeds." In 2012 IEEE Symposium on Humanities, Science and Engineering Research (SHUSER). IEEE, 2012. http://dx.doi.org/10.1109/shuser.2012.6268858.

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Yazdani, Davood, Alireza Bakhshai, and Praveen Jain. "A three-phase approach to harmonic and reactive current extraction and harmonic decomposition." In IECON 2009 - 35th Annual Conference of IEEE Industrial Electronics (IECON). IEEE, 2009. http://dx.doi.org/10.1109/iecon.2009.5415218.

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Yin, Xin, Han Hua, and Lisa Axe. "Determining the Speciation of Reactive Iron Mineral Coatings in Redox Transition Zones with Sequential Extraction." In Goldschmidt2020. Geochemical Society, 2020. http://dx.doi.org/10.46427/gold2020.3029.

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Yazdani, Davood, Alireza Bakhshai, Geza Joos, and Mohsen Mojiri. "An adaptive notch filtering approach for harmonic and reactive current extraction in active power filters." In IECON 2008 - 34th Annual Conference of IEEE Industrial Electronics Society. IEEE, 2008. http://dx.doi.org/10.1109/iecon.2008.4758010.

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Hu, Bihua, Longyun Kang, and Jiancai Cheng. "Extraction of Active and Reactive Powers DC Components for Grid-Connected Converters Under Unbalanced Network." In 2018 21st International Conference on Electrical Machines and Systems (ICEMS). IEEE, 2018. http://dx.doi.org/10.23919/icems.2018.8549469.

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"In Situ Biodiesel Production by non-Catalytic Supercritical Reactive Extraction of Low Grade Sunflower Seeds." In International Conference on Advances in Science, Engineering, Technology and Natural Resources. International Academy of Engineers, 2016. http://dx.doi.org/10.15242/iae.iae1116424.

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LEE, SANG CHEOL, BYOUNG SUNG AHN, and DONG JU MOON. "EQUILIBRIUM STUDIES ON REACTIVE EXTRACTION OF A WEAK ACID BY AN AMINE EXTRACTANT IN KEROSENE." In Proceedings of the 4th International Conference. WORLD SCIENTIFIC, 2004. http://dx.doi.org/10.1142/9789812702623_0062.

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Hailegiorgis, Sintayehu Mekuria, Shuhaimi Mahadzir, and Duvvuri Subbarao. "Reactive extraction of Jatropha curcas l assisted by phase transfer catalyst for the production of biodiesel." In 2011 National Postgraduate Conference (NPC). IEEE, 2011. http://dx.doi.org/10.1109/natpc.2011.6136248.

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Schael, Frank, Krishna Nigam, and Patrick Rojahn. "Continuous Reactive Extraction for Manufacturing of CMF and HMF from Fructose with Milli-/microstructured Coiled Flow Inverter." In Virtual 2021 AOCS Annual Meeting & Expo. American Oil Chemists' Society (AOCS), 2021. http://dx.doi.org/10.21748/am21.269.

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Reports on the topic "Reactive extraction"

1

Deo, M. D., and F. V. Hanson. Asphaltene reaction via supercritical fluid extraction. Office of Scientific and Technical Information (OSTI), March 1993. http://dx.doi.org/10.2172/10134823.

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