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{userid:"faculty_of_engineering.university_of_malaya", "refid":333,"repocollections":"","attachment":"","_thumb":"","articletype":"article","sectionheading":"","title":"p-Benzoquinone Anodic Degradation by Carbon Black Diamond Composite Electrodes","year":"2015","author":"Ajeel M. A.,\r\nAroua M. K.,\r\nDaud Wmaw","journal":"Electrochimica Acta","volume":"169","number":"","pages":"46-51","month":"Jul 1","doi":"10.1016\/j.electacta.2015.04.037","pubmed":"","pdflink":"http:\/\/www.sciencedirect.com\/science\/article\/pii\/S0013468615009159","urllink":"http:\/\/ac.els-cdn.com\/S0013468615009159\/1-s2.0-S0013468615009159-main.pdf?_tid=05b4e9d2-4012-11e5-91c7-00000aab0f02&acdnat=1439288365_7eedf5f9c4421326bae6f9bdde1a83c0","abstract":"In this work, p-benzoquinone (p-BQ) electro-degradation in three carbon black diamond (CBD) composite electrodes is studied under conditions of 200 mg\/L initial concentration, 45 mA\/cm(2) applied current density, pH 3, and 0.25 M Na2SO4 as a supporting electrolyte. The performance of the CBD electrodes was compared with that of a platinum electrode. Results showed that the optimal p-BQ degradation, COD removal efficiency, and current efficiency may be obtained from the CBD electrode containing 20% carbon black (20CBD). After 20 min of electro-degradation, p-BQ removal on 20CBD reached 96% at pH 6 and 61.5% at pH 3. However, after 180 min of p-BQ degradation, COD removal on this electrode reached 45% at pH 6 and 70% at pH 3. Increases in applied current during p-BQ electro-oxidation were related to the initial p-BQ concentration. Significant differences were observed in the solution containing 200 mg\/L p-BQ as the current density was increased from 20 mA\/cm(2) to 45 mA\/cm(2); no such effects were observed in the solution with 1000 mg\/L p-BQ. (C) 2015 Elsevier Ltd. All rights reserved.\r\n\r\nLink to Full-Text Articles :\r\nhttp:\/\/www.sciencedirect.com\/science\/article\/pii\/S0013468615009159\r\nhttp:\/\/ac.els-cdn.com\/S0013468615009159\/1-s2.0-S0013468615009159-main.pdf?_tid=05b4e9d2-4012-11e5-91c7-00000aab0f02&acdnat=1439288365_7eedf5f9c4421326bae6f9bdde1a83c0","note":"ISI Document Delivery No.: CI8GC\r\nTimes Cited: 0\r\nCited Reference Count: 29\r\nCited References: \r\n     Ajeel MA, 2015, ELECTROCHIM ACTA, V153, P379, DOI 10.1016\/j.electacta.2014.11.163\r\n     Can OT, 2010, J HAZARD MATER, V173, P731, DOI 10.1016\/j.jhazmat.2009.08.146\r\n     Canizares P, 2004, J APPL ELECTROCHEM, V34, P87, DOI 10.1023\/B:JACH.0000005587.52946.66\r\n     Cartaxo MAM, 2012, CHEMOSPHERE, V86, P341, DOI 10.1016\/j.chemosphere.2011.09.040\r\n     Choi JY, 2010, J HAZARD MATER, V179, P762, DOI 10.1016\/j.jhazmat.2010.03.067\r\n     Chu YY, 2010, J HAZARD MATER, V180, P247, DOI 10.1016\/j.jhazmat.2010.04.021\r\n     Comninellis C, 2010, ELECTROCHEMISTRY FOR THE ENVIRONMENT, P1, DOI 10.1007\/978-0-387-68318-8\r\n     Cui YH, 2009, WATER RES, V43, P1968, DOI 10.1016\/j.watres.2009.01.026\r\n     Czupryniak J, 2012, CENT EUR J PHYS, V10, P1183, DOI 10.2478\/s11534-012-0058-3\r\n     Duan XY, 2013, ELECTROCHIM ACTA, V94, P192, DOI 10.1016\/j.electacta.2013.01.151\r\n     Elaoud SC, 2011, DESALINATION, V272, P148, DOI 10.1016\/j.desal.2011.01.011\r\n     El-Ghenymy Abdellatif, 2012, Chemosphere, V87, P1126, DOI 10.1016\/j.chemosphere.2012.02.006\r\n     El-Ghenymy A, 2013, J ELECTROANAL CHEM, V689, P149, DOI 10.1016\/j.jelechem.2012.11.013\r\n     Feng YJ, 2003, WATER RES, V37, P2399, DOI 10.1016\/S0043-1354(03)00026-5\r\n     Houk LL, 1998, J APPL ELECTROCHEM, V28, P1167, DOI 10.1023\/A:1003439727317\r\n     Iniesta J, 2001, ELECTROCHIM ACTA, V46, P3573, DOI 10.1016\/S0013-4686(01)00630-2\r\n     Kapalka A, 2007, ELECTROCHIM ACTA, V53, P1954, DOI 10.1016\/j.electacta.2007.08.066\r\n     KIRK DW, 1985, J APPL ELECTROCHEM, V15, P285, DOI 10.1007\/BF00620944\r\n     Li N, 2007, CHEM PHYS LETT, V447, P241, DOI 10.1016\/j.cplett.2007.09.025\r\n     Liu L, 2009, J HAZARD MATER, V168, P179, DOI 10.1016\/j.jhazmat.2009.02.004\r\n     Oliveira RTS, 2007, CHEMOSPHERE, V66, P2152, DOI 10.1016\/j.chemosphere.2006.09.024\r\n     Panizza M., 2014, ENVIRON SCI POLLUT R, P1\r\n     Panizza M, 2005, ELECTROCHIM ACTA, V51, P191, DOI 10.1016\/j.electacta.2005.04.023\r\n     Panizza M., 2008, J ENV ENG MANAGE, V18, P139\r\n     Panizza M, 2009, CHEM REV, V109, P6541, DOI 10.1021\/cr9001319\r\n     PULGARIN C, 1994, WATER RES, V28, P887, DOI 10.1016\/0043-1354(94)90095-7\r\n     Wang Y, 2010, J HAZARD MATER, V178, P867, DOI 10.1016\/j.jhazmat.2010.02.018\r\n     Wei JJ, 2011, INT J MIN MET MATER, V18, P589, DOI 10.1007\/s12613-011-0482-1\r\n     Yoon JH, 2007, B KOR CHEM SOC, V28, P403\r\nAjeel, Mohammed A. Aroua, Mohamed Kheireddine Daud, Wan Mohd Ashri Wan\r\nEngineering, Faculty \/I-7935-2015\r\nEngineering, Faculty \/0000-0002-4848-7052\r\n0\r\nPERGAMON-ELSEVIER SCIENCE LTD\r\nOXFORD\r\nELECTROCHIM ACTA","tags":"carbon black diamond composite electrodes, p-benzoquinone, electro-degradation, current efficiency, cod, boron-doped diamond, waste-water treatment, electrochemical oxidation, aqueous-solution, phenol, 1,4-benzoquinone, bdd,","weight":333}
,

{userid:"faculty_of_engineering.university_of_malaya", "refid":147,"repocollections":"","attachment":"","_thumb":"","articletype":"article","sectionheading":"","title":"Progress, prospect and challenges in glycerol purification process: A review","year":"2015","author":"Ardi M. S.,\r\nAroua M. K.,\r\nHashim N. Awanis","journal":"Renewable & Sustainable Energy Reviews","volume":"42","number":"","pages":"1164-1173","month":"","doi":"DOI 10.1016\/j.rser.2014.10.091","pubmed":"","pdflink":"http:\/\/www.sciencedirect.com\/science\/article\/pii\/S1364032114009162","urllink":"https:\/\/ideas.repec.org\/a\/eee\/rensus\/v42y2015icp1164-1173.html","abstract":"Glycerol surplus in recent decades due to global increase in biodiesel production has created a new form of challenge in terms of purification for crude glycerol. This review summarizes the progress of crude glycerol purification technologies using various techniques. Critical insights are given regarding the application of suitable techniques for crude glycerol purification which includes chemical pre-treatment, methanol removal, vacuum distillation, ion exchange, activated carbon and membrane separation technology. Extensive discussion is made in relation with stages and processes in the conventional, current and emerging glycerol purification technologies. Lastly, aspects concerning the challenges of glycerol utilization and purification are thoroughly discussed. (C) 2014 Elsevier Ltd. All rights reserved.","note":"Az2ti\r\nTimes Cited:0\r\nCited References Count:125","tags":"crude glycerol, biodiesel, purification, membrane, waste cooking oil, economize biodiesel production, membrane separation processes, crude glycerol, vegetable-oils, seawater desalination, palm oil, osmotic distillation, reverse-osmosis, current state,","weight":147}
,

{userid:"faculty_of_engineering.university_of_malaya", "refid":295,"repocollections":"","attachment":"","_thumb":"","articletype":"article","sectionheading":"","title":"Removal of zinc and lead ions by polymer-enhanced ultrafiltration using unmodified starch as novel binding polymer","year":"2015","author":"Baharuddin N. H.,\r\nSulaiman N. M. N.,\r\nAroua M. K.","journal":"International Journal of Environmental Science and Technology","volume":"12","number":"6","pages":"1825-1834","month":"Jun","doi":"10.1007\/s13762-014-0549-4","pubmed":"","pdflink":"http:\/\/link.springer.com\/article\/10.1007%2Fs13762-014-0549-4","urllink":"http:\/\/link.springer.com\/article\/10.1007%2Fs13762-014-0549-4","abstract":"The removal of zinc and lead from aqueous dilute solutions by polymer-enhanced ultrafiltration process using unmodified starch as a new binding polymer was studied. Experiments were performed to determine the effects of transmembrane pressure, pH, concentration of metal ions on the retention and permeate flux. The performance of the proposed new binding polymer was compared to that of polyethyleneimine a conventional polymer frequently used in polymer-enhanced ultrafiltration. The retention of zinc and lead ions reached 96 and 66 %, respectively, using 0.05 % unmodified starch at pH 7. Overall unmodified starch showed better retention for zinc ions then polyethyleneimine, whereas polyethyleneimine retention for lead ions was higher. Solution pH was found to have little effect on flux.\r\n\r\nLink to Full-Text Articles :\r\nhttp:\/\/link.springer.com\/article\/10.1007%2Fs13762-014-0549-4","note":"ISI Document Delivery No.: CF9FB\r\nTimes Cited: 0\r\nCited Reference Count: 34\r\nCited References: \r\n     Alpatova A, 2004, SEP PURIF TECHNOL, V40, P155, DOI 10.1016\/j.seppur.2004.02.003\r\n     Alto K, 1977, TOXICITY XANTHATES F\r\n     Aratani T, 1983, REMOVAL METALS COMBI\r\n     Aroua MK, 2007, J HAZARD MATER, V147, P752, DOI 10.1016\/j.jhazmat.2007.01.120\r\n     Barakat MA, 2010, DESALINATION, V256, P90, DOI 10.1016\/j.desal.2010.02.008\r\n     Bello-Perez LA, 2009, FOOD ENG REV, V1, P50, DOI 10.1007\/s12393-009-9004-6\r\n     BeMiller JN, 2007, CARBOHYD POLYM, V64, P158\r\n     Bertolini A.C., 2010, STARCHES CHARACTERIZ\r\n     Yurum A, 2013, DESALINATION, V320, P33, DOI 10.1016\/j.desal.2013.04.020\r\n     BOLTO BA, 1995, PROG POLYM SCI, V20, P987, DOI 10.1016\/0079-6700(95)00010-D\r\n     Bosch X., 2003, SCIENCE, V609, P1\r\n     Camarillo R, 2012, DESALINATION, V286, P193, DOI 10.1016\/j.desal.2011.11.021\r\n     Chabot JF, 1976, INTERACTION IRON COM, P264\r\n     Chang JE, 2007, ENV INFORM ARCH, V5, P684\r\n     Doane WM, 1978, J APPL POLYM SCI, V24, P105\r\n     Eilers H, 1936, DEP CHEM, V69, P819\r\n     Gray JA, 2005, CARBOHYD POLYM, V60, P147, DOI 10.1016\/j\/carbpol.2004.11.032\r\n     Gray JA, 2004, CEREAL CHEM, V81, P278, DOI 10.1094\/CCHEM.2004.81.2.278\r\n     Hoover R, 2001, CARBOHYD POLYM, V45, P253, DOI 10.1016\/S0144-8617(00)00260-5\r\n     Zeng JX, 2009, J HAZARD MATER, V161, P1491, DOI 10.1016\/j.jhazmat.2008.04.123\r\n     Huber KC, 2001, CEREAL CHEM, V78, P173, DOI 10.1094\/CCHEM.2001.78.2.173\r\n     Islamoglu S, 2006, DESALINATION, V200, P288, DOI 10.1016\/j.desal.2006.03.335\r\n     Kadioglu SI, 2009, SEPAR SCI TECHNOL, V44, P2559, DOI 10.1080\/01496390903018061\r\n     Khaidar MS, 2009, DESALINATION, V249, P577\r\n     Kim BS, 1999, CARBOHYD POLYM, V39, P217, DOI 10.1016\/S0144-8617(99)00011-9\r\n     Kozuka H, 1985, J POLYM SCI, V23, P2109\r\n     LIM S, 1993, CEREAL CHEM, V70, P145\r\n     Malaysia DOE, 1994, MAL ENV QUAL ACT REP\r\n     Malaysia DOE, 2011, MAL ENV QUAL REP\r\n     Rivas BL, 2003, PROG POLYM SCI, V28, P173, DOI 10.1016\/S0079-6700(02)00028-X\r\n     Uludag Y, 1997, J MEMBRANE SCI, V129, P93, DOI 10.1016\/S0376-7388(96)00342-0\r\n     VANWARNERS A, 1994, IND ENG CHEM RES, V33, P981, DOI 10.1021\/ie00028a028\r\n     WING RE, 1975, J APPL POLYM SCI, V19, P847, DOI 10.1002\/app.1975.070190320\r\n     WU YS, 1990, CEREAL CHEM, V67, P202\r\nBaharuddin, N. H. Sulaiman, N. M. N. Aroua, M. K.\r\nEngineering, Faculty \/I-7935-2015\r\nEngineering, Faculty \/0000-0002-4848-7052\r\nUniversity of Malaya, Kuala Lumpur, Malaysia [PS 104-2010B, PV 092-2011B]\r\nThe authors acknowledge financial support from the University of Malaya, Kuala Lumpur, Malaysia through the Postgraduate Research Fund (PPP Grant) with grant PS 104-2010B and PV 092-2011B.\r\n0\r\nSPRINGER\r\nNEW YORK\r\nINT J ENVIRON SCI TE","tags":"complexing agents, metals, polyethyleneimine, separation, water soluble, heavy-metal ions, aqueous-solutions, polyethyleneimine pei, water, complexation, granules, location, sites, peuf,","weight":295}
,

{userid:"faculty_of_engineering.university_of_malaya", "refid":35,"repocollections":"","attachment":"","_thumb":"","articletype":"article","sectionheading":"","title":"Removal of Heavy Metal Ions from Mixed Solutions via Polymer-Enhanced Ultrafiltration using Starch as a Water-Soluble Biopolymer","year":"2015","author":"Baharuddin N. H.,\r\nSulaiman N. M. N.,\r\nAroua M. K.","journal":"Environmental Progress & Sustainable Energy","volume":"34","number":"2","pages":"359-367","month":"Mar","doi":"Doi 10.1002\/Ep.11995","pubmed":"","pdflink":"http:\/\/onlinelibrary.wiley.com\/doi\/10.1002\/ep.11995\/full","urllink":"http:\/\/onlinelibrary.wiley.com\/store\/10.1002\/ep.11995\/asset\/ep11995.pdf?v=1&t=i9c7hlfh&s=895e45e663147014dd138501e790f110807b8248","abstract":"In this study, aqueous solutions containing mixtures of heavy metals namely Zn (II), Pb (II), Cr (III), and Cr (VI) were treated by polymer-enhanced ultrafiltration (PEUF) using unmodified starch as binding biopolymer. The performance of starch in removing these heavy metals was compared with that of polyethylene glycol (PEG) a commonly used polymer in PEUF processes. Rejection coefficients and flux were studied under different values of pH solution and metal ion concentrations maintaining the transmembrane pressure constant at 1.5 bar. At pH 7, and starch concentration of 0.05%, the rejection was the highest at around 90%. As metal ion concentration increased from 10 to 50 mg\/L, the rejection of metal ions decreased. It was found that starch gave higher rejection for Zn (II) and Cr (III) at 0.05 g\/L of polymer concentration, whereas 1 g\/L of PEG concentration gave higher rejection for Cr (VI) at 10 mg\/L. The influence of metal ion concentration on Pb (II) rejection is not significant for the two selected polymers. The rejection of these metal ions by starch in this study is found to be influenced by granule structure that generally behaved in a non-ionic manner. (c) 2014 American Institute of Chemical Engineers Environ Prog, 34: 359-367, 2015","note":"Ce2fw\r\nTimes Cited:0\r\nCited References Count:29","tags":"polymer-enhanced ultrafiltration, multivalent metal ions removal, complexing agents, unmodified starch, polyethylene glycol, aqueous effluents, polyacrylic-acid, separation, membrane, recovery, cadmium, lead,","weight":35}
,

{userid:"faculty_of_engineering.university_of_malaya", "refid":112,"repocollections":"","attachment":"","_thumb":"","articletype":"article","sectionheading":"","title":"Impact of in situ physical and chemical cleaning on PVDF membrane properties and performances","year":"2015","author":"Rabuni M. F.,\r\nSulaiman N. M. Nik,\r\nAroua M. K.,\r\nChee Ching Yern,\r\nHashim N. Awanis","journal":"Chemical Engineering Science","volume":"122","number":"","pages":"426-435","month":"Jan 27","doi":"DOI 10.1016\/j.ces.2014.09.053","pubmed":"","pdflink":"http:\/\/www.sciencedirect.com\/science\/article\/pii\/S0009250914005661","urllink":"http:\/\/repository.um.edu.my\/95281\/1\/Fairus%20ChemEngSci%202014.pdf","abstract":"Appropriate selection of cleaning agent is an important factor to achieve a better cleaning efficiency and this topic has become an ongoing discussion. This work assesses the impacts of sodium hydroxide (NaOH) and sodium hypochlorite (NaOCl) aqueous solution towards polyvinylidene fluoride (PVDF) stability at the typical concentrations used in membrane cleaning. The cleaned membranes were characterised using held emission scanning electron microscopy (FESEM), Fourier transform infrared (FTIR), pure water flux measurement, contact angle, protein retention and tensile testing. Membrane cleaned at elevated temperature and higher concentration presented a higher water flux than the virgin membrane which can be a worrying sign of alteration in membrane properties. The FIR spectra indicated that the alteration in chemical composition of the membrane causes a reduction in the degree of hydrophilicity. The mechanical properties of the membrane were compromised based on the declination of tensile strength. The findings from this work suggest that the usage of NaOCl as compared to NaOH causes a more detrimental effect towards the stability of the PVDF membrane. (C) 2014 Elsevier Ltd. All rights reserved","note":"Aw1se\r\nTimes Cited:0\r\nCited References Count:34","tags":"poly(vinylidene fluoride), membrane cleaning, chemical, naoh, naocl, poly(vinylidene fluoride), uf membranes, sodium-hypochlorite, alkaline treatment, ultrafiltration, degradation, stability, phase, water,","weight":112}
,

{userid:"faculty_of_engineering.university_of_malaya", "refid":143,"repocollections":"","attachment":"","_thumb":"","articletype":"article","sectionheading":"","title":"Practical performance analysis of an industrial-scale ultrafiltration membrane water treatment plant","year":"2015","author":"Chew Chun Ming,\r\nAroua M. K.,\r\nHussain M. A.,\r\nIsmail W. M. Z. Wan,","journal":"Journal of the Taiwan Institute of Chemical Engineers","volume":"46","number":"","pages":"132-139","month":"Jan","doi":"DOI 10.1016\/j.jtice.2014.09.013","pubmed":"","pdflink":"http:\/\/www.sciencedirect.com\/science\/article\/pii\/S187610701400279X","urllink":"http:\/\/www.sciencedirect.com\/science\/article\/pii\/S187610701400279X","abstract":"Common design and operational issues to evaluate the performance of an ultrafiltration (UF) membrane water treatment plant are highlighted with a case study on an industrial-scale drinking water treatment plant located in Malaysia. This treatment plant has been in operation since February 2013 using dead-end polyethersulfone UF membrane filtration system to produce up to 14 million litres a day of drinking water to a small township. Literature solutions are compared with the practised solutions and elucidated with the case study. Gaps between literature solutions which are mainly based on lab-scale research and industry practices are identified. Reducing this gap will have vast implication to improve the design and operation of industrial-scale UF treatment system. (C) 2014 Taiwan Institute of Chemical Engineers. Published by Elsevier B.V. All rights reserved.","note":"Ca5pf\r\nTimes Cited:0\r\nCited References Count:38","tags":"ultrafiltration, water treatment, design, operation, wound uf membrane, treatment facility, permeate flow, humic-acid, filtration, backwash, ro, foulants, removal, design,","weight":143}
,

{userid:"faculty_of_engineering.university_of_malaya", "refid":141,"repocollections":"","attachment":"","_thumb":"","articletype":"article","sectionheading":"","title":"Physicochemical characterization and thermal behavior of biodiesel and biodiesel\u2013diesel blends derived from crude Moringa peregrina seed oil","year":"2015","author":"Salaheldeen Mohammed,\r\nAroua M. K.,\r\nMariod A. A.,\r\nCheng Sit Foon,\r\nAbdelrahman Malik A.,\r\nAtabani A. E.","journal":"Energy Conversion and Management","volume":"92","number":"","pages":"535-542","month":"Mar 1","doi":"10.1016\/j.enconman.2014.12.087","pubmed":"","pdflink":"http:\/\/www.sciencedirect.com\/science\/article\/pii\/S0196890414011364","urllink":"http:\/\/www.sciencedirect.com\/science\/article\/pii\/S0196890414011364","abstract":"Moringaceae is a monogeneric family with a single genus i.e. Moringa. This family includes 13 species. All these species are known as medicinal, nutritional and water purification agents. This study reports, for the first time, on characterization of the biodiesel derived from crude Moringa peregrina seed oil and its blends with diesel. The crude oil was converted to biodiesel by the transesterification reaction, catalyzed by potassium hydroxide. High ester content (97.79%) was obtained. M. peregrina biodiesel exhibited high oxidative stability (24.48 h). Moreover, the major fuel properties of M. peregrina biodiesel conformed to the ASTM D6751 standards. However, kinematic viscosity (4.6758 mm(2)\/s), density (876.2 kg\/m(3)) and flash point (156.5 degrees C) were found higher than that of diesel fuel. In addition, the calorific value of M. peregrina biodiesel (40.119 MJ\/kg) was lower than the diesel fuel. The fuel properties of M. peregrina biodiesel were enhanced significantly by blending with diesel fuel. In conclusion, M. peregrina is a suitable feedstock for sustainable production of biodiesel only blended up to 20% with diesel fuel, considering the edibility of all other parts of this tree. (C) 2015 Elsevier Ltd. All rights reserved.","note":"Times Cited: 0\r\n0","tags":"Moringa peregrina, Biodiesel, Fuel properties, Thermal stability,","weight":141}
,

{userid:"faculty_of_engineering.university_of_malaya", "refid":346,"repocollections":"","attachment":"","_thumb":"","articletype":"article","sectionheading":"","title":"Fabrication modeling of industrial CO2 ionic liquids absorber by artificial neural networks","year":"2015","author":"Abdollahi Y.,\r\nSairi N. A.,\r\nAroua M. K.,\r\nMasoumi H. R. F.,\r\nJahangirian H.,\r\nAlias Y.","journal":"Journal of Industrial and Engineering Chemistry","volume":"25","number":"","pages":"168-175","month":"May 25","doi":"10.1016\/j.jiec.2014.10.029","pubmed":"","pdflink":"http:\/\/www.sciencedirect.com\/science\/article\/pii\/S1226086X14005188","urllink":"http:\/\/ac.els-cdn.com\/S1226086X14005188\/1-s2.0-S1226086X14005188-main.pdf?_tid=413a7008-4012-11e5-bd2f-00000aab0f6b&acdnat=1439288465_081e064b9a30b845ced3cbe977c1ca64","abstract":"The fabrication of industrial CO2 blended solution absorber was modeled by artificial neutral network. First the generated model had been statistically evaluated and then its ability of prediction was confirmed by validation test. The validated model was used to predict the desirable density and relative importance of the fabrication's effective variables. In conclusion, the importance included x[H2O], 36.18%, x[gua], 25.37%, x[MDEA], 25.34% and temperature, 13.11% which showed none of them is negligible as well as the density (g cm(-3)) was validated by further experiment that showed the actual density, 1.101, was quite close to the predicted value, 1.017. (C) 2014 The Korean Society of Industrial and Engineering Chemistry. Published by Elsevier B.V. All rights reserved.\r\n\r\nLink to Full-Text Articles :\r\nhttp:\/\/www.sciencedirect.com\/science\/article\/pii\/S1226086X14005188\r\nhttp:\/\/ac.els-cdn.com\/S1226086X14005188\/1-s2.0-S1226086X14005188-main.pdf?_tid=413a7008-4012-11e5-bd2f-00000aab0f6b&acdnat=1439288465_081e064b9a30b845ced3cbe977c1ca64","note":"ISI Document Delivery No.: CK4NL\r\nTimes Cited: 1\r\nCited Reference Count: 36\r\nCited References: \r\n     Abdollahi Y., 2013, CHEM CENT J, V7, P1\r\n     Abdollahi Y., 2012, CHEM CENT J, V6, P1\r\n     Abdollahi Y, 2014, CLEAN-SOIL AIR WATER, V42, P1292, DOI 10.1002\/clen.201300451\r\n     Aber S, 2009, J HAZARD MATER, V171, P484, DOI 10.1016\/j.jhazmat.2009.06.025\r\n     Aijun L., 2004, ACTA MAT, V52, DOI 10.1016\/j.actamat.2003.09.020\r\n     Bates D. 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,

{userid:"faculty_of_engineering.university_of_malaya", "refid":153,"repocollections":"","attachment":"","_thumb":"","articletype":"article","sectionheading":"","title":"A review: Conversion of bioglycerol into 1,3-propanediol via biological and chemical method","year":"2015","author":"Lee C. S.,\r\nAroua M. K.,\r\nDaud W. M. A. W.,\r\nCognet P.,\r\nPeres-Lucchese Y.,\r\nFabre P. L.,\r\nReynes O.,\r\nLatapie L.","journal":"Renewable & Sustainable Energy Reviews","volume":"42","number":"","pages":"963-972","month":"Feb","doi":"DOI 10.1016\/j.rser.2014.10.033","pubmed":"","pdflink":"http:\/\/www.sciencedirect.com\/science\/article\/pii\/S1364032114008582","urllink":"https:\/\/ideas.repec.org\/a\/eee\/rensus\/v42y2015icp963-972.html","abstract":"Today, the price of glycerol has dramatically dropped due to its oversupply from biodiesel production as well as oleochemical industry. Thus, it is essential to develop processes to transform bioglycerol into commercially valued products which is important to ensure sustainability in the biodiesel and oleochemical industries. One possibility is to transform it in propanediols, which have numerous applications such as food additives, raw material in pharmaceutical and cosmetic industries. In this paper, methods of conversion of glycerol into 1,3-propanediol are reviewed and discussed in detail. (C) 2014 Elsevier Ltd. All rights reserved.","note":"Az2ti\r\nTimes Cited:0\r\nCited References Count:89","tags":"1,3-propanediol, biocatalysis, bioglycerol, catalysis, biodiesel, micro-aerobic conditions, value-added products, klebsiella-pneumoniae, crude glycerol, sp-nov, biodiesel production, raw glycerol, clostridium-pasteurianum, lactobacillus-reuteri, citrobacter-freundii,","weight":153}
  ]
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