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| 1 | The influence of temperature and inlet velocity on cyclone pressure drop: a CFD study 显示文摘 | Gimbun J Chuah T G Fakhru'l-Razi A | 2005 | Chemical Engineering and Processing2005，44，1： | 1 |
| 2 | The influence of temperature and inlet velocity on cyclone pres- sure drop:A CFD smdy显示文摘 | Gimbun J Chuah T G Fakhru'l-Razi A | 2005 | Chem Eng Process2005，44，1： | 1 |
| 3 | The influence of temperature and inlet velocity on cyclone pressure drop: a CFD study 显示文摘 | GIMBUN J CHUAH T G FAKHRU' L - RAZI A | 2005 | Chemical Engineering and Processing2005，44，8： | 1 |
| 4 | Application of computational fluid dynamics (CFD) simulations to spray-freezing operations显示文摘 | Anandharamakrishnan C Gimbun J Stapley A G F | 2010 | Drying Technology2010，28，1： | 1 |
| 5 | A CFD study on the prediction of cyclone collection efficiency显示文摘 | Gimbun J Chuah T G Thomas S Y el al | | 0，，03： | 1 |
| 6 | A CFD study on the effect of cone dimensions on sampling aero-cyclones performance and hydrodynamics显示文摘 | CHUAN T GIMBUN J CHOONG T S | 2006 | Powder Technology2006，162，2： | 1 |
| 7 | The influence of temperature and inlet velocity on cyclone pressure drop:a CFD study显示文摘 | JOLIUS GIMBUN CHUAH T G FAKHUR'L-RAZI A | 2005 | Chemical Engineering and Processing2005，44，： | 1 |
| 8 | Prediction of the effects of cone tip diameter on the cyclone per-formance显示文摘 | Gimbun J Chuah T J Thomas S Y | 2005 | Journal of Aerosol Science2005，36，8： | 1 |
| 9 | Modelling of mass transfer in gas–liquid stirred tanks agitated by Rushton turbine and CD-6 impeller: A scale-up study显示文摘 | J. Gimbun C.D. Rielly Z.K. Nagy | 2008 | Chemical Engineering Research and Design2008，，4： | 1 |
| 10 | The influence of temperature and inlet velocity on cyclone pressure drop:A CFD study显示文摘 | Gimbun J Chuah T G Fakhru' 1-Razi A | 2005 | Chemical Engineering and Processing2005，44，： | 1 |
| 11 | The influence of temperature and inlet velocity on cyclone drop:a CFD study 显示文摘 | Gimbun J Chuah T G Fakhru'l-Razi A | 2005 | Chemical Engineering and Processing2005，44，1： | 1 |
| 12 | Prediction of the effects of cone tip diameter on the cyclone performance显示文摘 | GIMBUN J CHUAH T G CHOONG T S Y | 2005 | Journal of Aerosol Science2005，36，8： | 1 |
| 13 | The influence of temperature and inlet velocity on cyclone pressure drop:a CFD study显示文摘 | Jolius Gimbun T G Chuah A Fakhrul - Razi | 2005 | Chemical Engineering and Processing2005，44，： | 1 |
| 14 | A CFD study of the effect of cone dimensions on sampling aerocy- clones performance and hydrodynamics 显示文摘 | Chuah T G Gimbun Jolius Choong Thomas S Y | 2006 | Powder Tech- nology2006，162，2： | 1 |
| 15 | Biodiesel Production from Rubber Seed Oil using Activated Cement Clinker as Catalyst显示文摘 | Jolius Gimbun Shahid Ali Chitra Charan Suri Charan Kanwal Liyana Amer Shah Nurul Hidayah Muhamad @ Ghazali Chin Kui Cheng Said Nurdin | 2013 | Procedia Engineering2013，，： | 1 |
| 16 | A CFD study of the effect of cone dimensions on sampling aerocyclones performance and hydrodynamics显示文摘 | Gimbun J | 2006 | Powder Technology2006，162，2： | 1 |
| 17 | A CFD study of the effect of cone dimensions on sampling aerocyclones performance and hydrodynamics显示文摘 | CHUAH T G GIMBUN J CHOONG T S Y | | 0，，162： | 1 |
| 18 | The influence of temperature and inlet velocity on cyclone pressure drop: A CFD study显示文摘 | GIMBUN J CHUAH T G FAKHRU' L-RAZI A | 2005 | Chemical Engineering and Processing2005，44，1： | 1 |
| 19 | The influence of temperature and inlet velocity on cyclone pressure drop:A CFD study显示文摘 | Jolius Gimbun Chuah T G Faljru'l-Razi A | 2005 | Chemical Engineering and Processing2005，44，1： | 1 |
| 20 | Characterization of La-promoted Ni/Al_2O_3 catalysts for hydrogen production from glycerol dry reforming显示文摘In the current paper, dry(CO2)-reforming of glycerol, a new reforming route, was carried out over alumina(Al2O3)-supported, non-promoted and lanthanum-promoted nickel(Ni) catalysts. Both sets of catalysts were synthesized via a wet co-impregnation procedure. Physicochemical characterization of the catalysts showed that the promoted catalyst possessed smaller metal crystallite size, hence higher metal dispersion compared to the virgin Ni/Al2O3catalyst. This was also corroborated by the surface images captured by the FESEM analysis. From temperature-programmed calcination analysis, the derivative weight profiles revealed two peaks, which represent a water elimination peak at a temperature range of 373 to 473 K followed by nickel nitrate decomposition from 473 to 573 K. In addition, BET surface area measurements gave 85.0 m2 g-1for the non-promoted Ni catalyst, whilst the promoted catalysts showed an average of 1% to 6% improvement depending on the La loadings. Significantly, reaction studies at 873 K showed that glycerol dry reforming successfully produced H2. The 2%La-Ni/Al2O3catalyst, which possessed the largest BET surface area, gave an optimum H2generation(9.70%) at a glycerol conversion of 24.5%. | Kah Weng Siew Hua Chyn Lee Jolius Gimbun Chin Kui Cheng | 2014 | Journal of Energy Chemistry2014，23，1： | 1 |
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