| 473 - 477 |
Heat consumption and irreversibilities in rectification processes
Knoche KF |
| 478 - 485 |
Exergy analysis of distillation processes
LeGoff P, Cachot T, Rivero R |
| 486 - 488 |
Reduction of investment costs by improvement of thermodynamic efficiency in cryogenic systems
Quack H, Philipp J |
| 489 - 497 |
Dynamic behavior and operational aspects of heat-integrated distillation processes
Lang L |
| 498 - 502 |
Opportunities and limits for exergy analysis in cryogenics
Streich M |
| 503 - 509 |
Power consumption of multiple shaft agitators
Pahl MH, Brenke A, Luo YN |
| 510 - 513 |
Adaptation of hydrocyclone to varying solid load by air injection
Mittal M |
| 514 - 525 |
Models describing the behavior of new carbon fiber packings in rectification processes
Becker O, Steiner R |
| 526 - 537 |
Characterization of small- and intermediate-pore zeolites by means of temperature-programmed desorption of amines
Merz C, Fetting F |
| 538 - 542 |
Comparison study of Lewis acid type catalysts on the esterification of octanoic acid and n-octyl alcohol
Santos AMB, Martinez M, Mira JA |
| 543 - 549 |
Tailor-made additives to influence the habit of barite (BaSO4) obtained by precipitation
Kipp S, Lacmann R, Reichelt M, Schroder W |
| 550 - 552 |
Simulation of removal of HCl gas in a spray dry tower
Maezawa A, Suzuki H, Seno T, Uchida S |
