449 - 459 |
Properties of char particles obtained under O-2/N-2 and O-2/CO2 combustion environments Li QZ, Zhao CS, Chen XP, Wu WF, Lin BQ |
460 - 467 |
Improvement of hydrocyclone separation performance by incorporating a conical filtering wall Vieira LGM, Damasceno JJR, Barrozo MAS |
468 - 475 |
Kinetics of emulsification and rheological properties of highly concentrated explosive emulsions Mudeme S, Masalova I, Haldenwang R |
476 - 483 |
Diafiltration and water recovery of Reactive Brilliant Blue KN-R solution by two-stage membrane separation process He Y, Li GM, Wang H, Jiang ZW, Zhao JF, Su HX, Huang QY |
484 - 489 |
Phase transfer catalysis of alkaline hydrolysis of n-butyl acetate: Comparison of performance of batch and micro-reactors Cherlo SKR, Devaki K, Pushpavanam S |
490 - 499 |
Insights into fry-drying process of wood through a simplified approach of heat and mass transport phenomena Grenier D, Bohuon P, Meot JM, Bailleres H |
500 - 507 |
Factorial design of experiment (DOE) for parametric exergetic investigation of a steam methane reforming process for hydrogen production Hajjaji N, Renaudin V, Houas A, Pons MN |
508 - 513 |
Application of HIGEE process intensification technology in synthesis of petroleum sulfonate surfactant Zhang D, Zhang PY, Zou HK, Chu GW, Wu W, Zhu ZW, Shao L, Chen JF |
514 - 522 |
Influence of flow field on sedimentation efficiency in a circular settling tank with peripheral inflow and central effluent Bajcar T, Gosar L, Sirok B, Steinman F, Rak G |
523 - 529 |
Heat transfer and bubble dynamics in a three-phase inverse fluidized bed Myre D, Macchi A |
530 - 535 |
Coupling reaction and azeotropic distillation for the synthesis of glycerol carbonate from glycerol and dimethyl carbonate Li JB, Wang T |
536 - 546 |
Numerical modelling of swirl flow induced by a three-lobed helical pipe Fokeer S, Lowndes IS, Hargreaves DM |