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CONTROL FOR HEAT EXCHANGE. M. B. JENNINGS CHE 185 FEB 2006. OUTLINE. EXCHANGER DESIGN CONCEPTS GENERAL CONTROL CONFIGURATION SPECIFIC TYPES OF PROCESSES HEAT RECOVERY REACTORS DISTILLATION COLUMNS. SINGLE HEAT EXCHANGERS. SHELL & TUBE EXCHANGERS
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CONTROL FOR HEAT EXCHANGE M. B. JENNINGS CHE 185 FEB 2006
OUTLINE • EXCHANGER DESIGN CONCEPTS • GENERAL CONTROL CONFIGURATION • SPECIFIC TYPES OF PROCESSES • HEAT RECOVERY • REACTORS • DISTILLATION COLUMNS
SINGLE HEAT EXCHANGERS • SHELL & TUBE EXCHANGERS • USED FOR SINGLE PHASE OR TWO PHASE FLOWS • From: http://www.me.wustl.edu/ME/labs/thermal/me372b5.htm
EXCHANGER FLOW PATTERNS • COCURRENT OR COUNTERCURRENT
MULTIPASS EXHANGERS • 1 SHELL- 2 TUBE PASS EXCHANGER • COMBINED COUNTERCURRENT AND COCURRENT FLOW
HEAT EXCHANGE LIMITS • FOR PURE COUNTERCURRENT FLOWS • TEMPERATURE CROSSES ARE NOT POSSIBLE WITH MULTIPASS EXCHANGERS
BASIC CONTROL SCHEMESFOR SINGLE EXCHANGERS -1 FLUID TEMPERING EXCHANGER WITH FEEDBACK CONTROL
BASIC CONTROL SCHEMESFOR SINGLE EXCHANGERS - 2 FLUID TEMPERING EXCHANGER WITH FEEDBACK AND FEEDFORWARD CONTROL
HEAT RECOVERY SYSTEMS • HEAT RECOVERY FOR A SIMPLE SYSTEM
REACTOR TEMPERATURE CONTROL WITH JACKET - 1 • FEEDBACK CONTROL BASED ON PRODUCT TEMPERATURE
REACTOR TEMPERATURE CONTROL WITH JACKET - 2 • FEEDFORWARD CONTROL BASED ON JACKET COOLANT INLET TEMPERATURE
CONCLUSIONS • A FEW TYPES OF CONTROL CONFIGURATIONS CAN BE APPLIED TO A WIDE RANGE OF HEAT EXCHANGE PROCESSES • SPECIFIC TYPES OF UNIT OPERATIONS MAY BE ABLE TO USE MORE COMPLEX HEAT EXCHANGE CONTROL