1 - 6 |
NEW TECHNOLOGY FOR HYDROGEN-PRODUCTION BY THE CATALYTIC-OXIDATION AND STEAM REFORMING OF METHANOL AT LOW-TEMPERATURES JIANG CJ, TRIMM DL, WAINWRIGHT MS |
7 - 11 |
BASIC SITES ON THE SURFACE OF OXIDE CATALYSTS RESPONSIBLE FOR OXIDATIVE METHANE COUPLING DAVYDOV AA |
12 - 16 |
ECONOMICS OF THE OXIDATIVE COUPLING OF METHANE AS AN ADD-ON UNIT FOR NAPHTHA CRACKING HOEBINK JHBJ, VENDERBOSCH HM, VANGEEM PC, DENOOSTERKAMP PF, MARIN GB |
17 - 22 |
SELECTIVE OXIDATION OF O-XYLENE TO PHTHALIC-ANHYDRIDE OVER VANADIA-TITANIA - A COMPARATIVE-STUDY OF INTEGRAL AND RECYCLE REACTOR OPERATION NOBBENHUIS MG, BARNICKEL P, WOKAUN A, BAIKER A |
23 - 24 |
LIMITATION BY ZEOLITE PROTONS OF THE OXYGENATE YIELD IN SYNGAS CONVERSION OVER RHMN/NAY CATALYSTS TREVINO H, SACHTLER WMH |
25 - 32 |
MODIFICATION OF THE CATALYTIC PROPERTIES OF SUPPORTED NOBLE-METAL CATALYSTS BY CARRIER DOPING IOANNIDES T, VERYKIOS XE |
33 - 40 |
SINGLE LIQUID-DROP VELOCITIES AND BREAKAGE MECHANISM IN SECTIONS OF STRUCTURED PACKINGS MAO ZQ, GODFREY JC, SLATER MJ |
41 - 48 |
SINGLE LIQUID-DROP BREAKAGE PROBABILITIES AND CHARACTERISTIC VELOCITIES IN KUHNI COLUMNS FANG J, GODFREY JC, MAO ZQ, SLATER MJ, GOURDON C |
49 - 58 |
3-STAGE WIPED-FILM MOLECULAR EVAPORATOR - DESIGN AND APPLICATION CVENGROS J |
59 - 62 |
GAS MIXING IN THE COCURRENT DOWNFLOW CIRCULATING FLUIDIZED-BED WEI F, JIN Y, YU ZQ, LIU JZ |
63 - 67 |
RECOMMENDED OPERATING RANGE FOR A ROTATING-DISC CONTACTOR NIEDZIALKOWSKI W, KACZMARSKI K |
68 - 74 |
VORTEX DEPTH IN UNBAFFLED SINGLE AND MULTIPLE IMPELLER AGITATED VESSELS MARKOPOULOS J, KONTOGEORGAKI E |