| 249 - 256 |
PYROLYSIS OF BLACK LIQUOR BY USING SOME BASIC CATALYSTS
KUCUK MM |
| 257 - 271 |
GLOBAL KINETIC-MODELS OF METHANOL SYNTHESIS IN 3-PHASE AGITATED SLURRY REACTOR
YING WY, CHEN MS, FANG DY, ZHU BC |
| 273 - 287 |
HYDROGEN-SULFIDE POISONING OF METHANOL SYNTHESIS CU-BASED CATALYST .1. INTRINSIC DEACTIVATION KINETICS
YING WY, FANG DY, ZHU BC |
| 289 - 302 |
HYDROGEN-SULFIDE POISONING OF METHANOL SYNTHESIS CU-BASED CATALYST .2. POISONING OF COMMERCIAL CATALYST
YING WY, FANG DY, ZHU BC |
| 303 - 315 |
HYDROGEN-SULFIDE POISONING OF METHANOL SYNTHESIS CU-BASED CATALYST .3. EFFECTIVENESS FACTOR OF POISONED CATALYST
YING WY, FANG DY, ZHU BC |
| 317 - 329 |
KINETIC RATE EXPRESSION FOR METHANOL SYNTHESIS IN A LIQUID ENTRAINED REACTOR
VIJAYARAGHAVAN P, KULIK CJ, LEE S |
| 331 - 343 |
LIQUID-PHASE METHANOL SYNTHESIS IN AN ENTRAINED REACTOR-DEVELOPMENT OF A GAS-LIQUID MASS-TRANSFER CORRELATION
VIJAYARAGHAVAN P, LEE S |
| 345 - 359 |
A COMPARATIVE-STUDY OF HYDROCARBONS PRESENT IN NARROW BOILING RANGE NAPHTHA FRACTIONS OF SAUDI-ARABIAN CRUDE OILS
ALI MA |
