Process design and control: Rigorous procedure for the design of conventional atmospheric crude fractionation units. Part I: Targeting

Industrial and Engineering Chemistry Research

Volumn 40, Issue 2, 2001, Pages 617-626

  Bagajewicz, M ^a   Ji, S ^a  

^a University of Oklahoma   (United States)

Author keywords

[No Author keywords available]

Indexed keywords

PETROLEUM;

CRUDE OIL; DESIGN; FRACTIONATION; PROCESS CONTROL;

ARTICLE; DENSITY; DISTILLATION; ENERGY CONSUMPTION; ENERGY RESOURCE; FRACTIONATION; HEAT EXCHANGE;

CRUDE PETROLEUM; DISTILLATION; DISTILLATION COLUMNS; HEAT EXCHANGERS; PROCESS CONTROL; TEMPERATURE MEASUREMENT;

ENERGY COST; PREFRACTIONATION COLUMNS;

FRACTIONATING UNITS;

EID: 0034745784     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie000302+     Document Type: Article

References (18)

1. History and development of some important phases of petroleum refining in the United States
2. The Brugma process
3. On the design flexibility of crude atmospheric plants
4. Synthesis of distillation column configurations for a multicomponent separation
5. Distillation equipment in the oil refining industry
6. Integrated crude distillation design
7. Integration design of a conventional crude oil distillation tower using pinch analysis
8. Design/retrofit targets of pump-around refluxes for better energy integration of a crude distillation column
9. Optimizing the heat recovery of crude units
10. An intermediate heating and cooling method for a distillation column
11. A simple synthesis method based on utility bounding for heat-integrated distillation sequences
12. Temperature-heat diagrams for complex columns. 1. Intercooled/interheated distillation columns
13. Distillation column targets