Heat exchanger network retrofit by pinch design method using stage-model mathematical programming

Chemical Engineering Transactions

Volumn 29, Issue , 2012, Pages 367-372

  Siemanond, Kitipat ^a   Kosol, Supachai ^a  

^a CHULALONGKORN UNIVERSITY   (Thailand)

Author keywords

[No Author keywords available]

Indexed keywords

APPLICATION PROGRAMS; DISTILLATION; DISTILLATION EQUIPMENT; MATHEMATICAL PROGRAMMING; OPERATING COSTS; RETROFITTING; VISUAL BASIC;

CAPITAL COSTS; COMPOSITE CURVES; CRUDE DISTILLATION UNITS; DESIGN APPROACHES; GRAND COMPOSITE CURVES; HEAT EXCHANGER NETWORK; UTILITY CONSUMPTION; VISUAL BASIC FOR APPLICATIONS;

HEAT EXCHANGERS;

EID: 84870855374     PISSN: 22839216     EISSN: 22839216     Source Type: Journal    
DOI: 10.3303/CET1229062     Document Type: Conference Paper

References (5)

1. Tjoe T.N., Linnhoff B., 1986, Using Pinch Technology for Process Retrofit. Chemical Engineering Journal, 28, 47-60.
2. Yee T.F., Grossmann I.E., 1990, Simultaneous Optimization Models for Heat Integration. Computers and Chemical Engineering, 14, 1151.
3. Nguyen D.Q., Barbaro A., Vipanurat N., Bagajewicz M. J., 2010, All-At-Once and Step-Wise Detailed Retrofit of Heat Exchanger Networks using an MILP Model, Industrial and Engineering Chemistry Research, 49, 6080-6130.
4. Smith R., 1995, Chemical Process Design, McGraw-Hill, Inc., New York.
5. Promvitak P., Siemanond K., Bunluesriruang S., Raghareutai V., 2009, Retrofit Design of Heat Exchanger Networks of Crude Oil Distillation Unit, Chemical Engineering Transactions, 18, 99-104, DOI: 10.3303/CET0918014.