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Smith: Chemical Process Design and Integration (Chapters 16,18) Kemp: Pinch Analysis and Process Integration (Chapter 9)
Process Integration for Efficient Use of Energy
Cheng-Liang Chen
PSE
LABORATORY
Department of Chemical Engineering National TAIWAN University
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Important Global Crises Ten Most Important Global Crises: Energy Water Food • Environment Poverty Terrorism Disease Education Democracy Population
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Outline ➢ Systematic Approach for Chemical Process Design How do we go about the design of a chemical process? ➢ What Is Process Integration? Onion model for process integration ➢ Pinch Analysis: Targeting Heat Recovery in Processes ➢ The Pinch Design Method for Heat Recovery Systems ➢ A Pinch Study Performed on A Major Operating Plant ➢ Utility Selection for Individual Processes ➢ Putting It into Practice ➢ Concluding Remarks
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Systematic Approach for
Chemical Process Design
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Chemical Process Design How do we go about the design of a chemical process?
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Chemical Process Design How do we go about the design of a chemical process?
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Chemical Process Design How do we go about the design of a chemical process?
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Chemical Process Design How do we go about the design of a chemical process?
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Chemical Process Design How do we go about the design of a chemical process?
Finished Process ? UNFORTUNATELY This is inefficient in energy use! So let’s consider heat recovery to reduce the energy consumption
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Chemical Process Design How do we go about the design of a chemical process?
Some streams need to be cooled down and some need to be heated up
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Chemical Process Design How do we go about the design of a chemical process?
Recover heat between a stream that needs to be cooled down and one that needs to be heated up
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Chemical Process Design How do we go about the design of a chemical process?
· · · and more heat recovery completes the design
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Chemical Process Design How do we go about the design of a chemical process?
different possibilities for heat integration
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Chemical Process Design How do we go about the design of a chemical process?
Changing the reactor dictates a different separation and recycle problem
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Chemical Process Design How do we go about the design of a chemical process?
Changing the reactor dictates a different separation and recycle problem
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Chemical Process Design How do we go about the design of a chemical process?
· · · leads to a different separation system and different heat recovery
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Chemical Process Design How do we go about the design of a chemical process?
· · · leads to a different separation system and different heat recovery
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What Is Process Integration ?
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What Is Process Integration? First choose a series of processing steps
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What Is Process Integration? Then connect these processing steps together
To give an integrated manufacturing system that is: Environmentally acceptable; Safe; Profitable; Operable
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What Is Process Integration? First Process Integration:
Then Process Simulation:
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Onion Model for
Process Integration
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Onion Model Start With The Reactor
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Onion Model Then Add Separation System and Connect Up Recycle
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Onion Model Recover Heat Where Possible
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Onion Model Dictate The Need for External Utilities
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Hierarchy of Process Design Reactor Design ⇓ Separation System Design ⇓ HEN Design ⇓ Utility System Design Process design is strongly coupled with Heat Exchanger Networks
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Process Integration (for Heat Recovery) ➢ Process Integration: using process streams to heat and cool other streams ☞ Hot streams gives off heat to another streams ☞ Cold streams absorbs heat from another streams ➢ Additional heating or cooling is done using utility streams ➢ Heat recovery reduces utility requirements, and therefore operating costs
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Process Integration (for Heat Recovery) Ex: The Front End of A Specialty Chemicals Process
Six heat transfer units (i.e. heaters, coolers and exchangers) are used and the energy requirements are 1, 722 kW for heating and 654 kW for cooling.
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Process Integration (for Heat Recovery) Ex: The Front End of A Specialty chemicals Process
The alternative flowsheet uses only four heat transfer units and the utility heating load is reduced by about 40% (1, 068 kW) with cooling no longer required.
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