Zobrazeno 1 - 10
of 420
pro vyhledávání: '"William L. Luyben"'
Publikováno v:
ACS Sustainable Chemistry & Engineering. 10:7409-7417
Autor:
William L. Luyben
Publikováno v:
Journal of Process Control. 113:96-100
Autor:
William L. Luyben
Publikováno v:
Journal of Process Control. 111:1-7
Autor:
William L. Luyben
Publikováno v:
Chemical Engineering and Processing - Process Intensification. 190:109412
Autor:
William L. Luyben
Publikováno v:
Computers & Chemical Engineering. 175:108284
Publikováno v:
ACS Sustainable Chemistry & Engineering. 9:13233-13244
Autor:
William L. Luyben
Publikováno v:
Chemical Engineering Research and Design. 170:69-75
Selecting the temperature of each vessel in a multi-effect evaporator process is typically a trial-and-error procedure because a practical design specifies that the heat-transfer areas are the same in each vessel. A method for directly calculating th
Autor:
William L. Luyben
Publikováno v:
Chemical Engineering Research and Design. 162:28-37
Many chemical processes require complex piping configurations to achieve a variety of objectives such as splitting a stream into multiple parallel streams, blending several streams, bypassing units and interconnecting process units. The plumbing requ
Autor:
William L. Luyben
Publikováno v:
Chemical Engineering Research and Design. 161:38-44
A recent paper developed a complex divided-wall column with two walls in a single vessel that was capable of separating a four-component mixture into four high-purity products. The walls created three internal sections in the middle of the column. On
Autor:
William L. Luyben
Publikováno v:
Journal of Process Control. 92:288-295
A recent paper explored the separation of the close-boiling mixture 1,2 propanediol (PDO) and ethylene glycol (EG). The optimum operating pressure using a traditional single vessel was 282 kPa with a reboiler duty of 399 kW. However, the vapor–liqu