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Design Methods and Algorithms for Multicomponent Distillation Processes

Design Methods and Algorithms for Multicomponent Distillation Processes. Lei Huang. Outline. Introduction Basic configurations Mathematical framework for searching basic configurations Practice. Introduction. Is it necessary to search all possible configurations?

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Design Methods and Algorithms for Multicomponent Distillation Processes

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  1. Design Methods and Algorithms for Multicomponent Distillation Processes Lei Huang

  2. Outline • Introduction • Basic configurations • Mathematical framework for searching basic configurations • Practice

  3. Introduction • Is it necessary to search all possible configurations? • If not, can we find a smallest adequate search space? • If so, how to implement it?

  4. Basic and Non-Basic Configurations • Each column has a condenser on top. • Each column has a reboiler at the bottom. • There are (n-1) distillation columns, after full consolidation of sections. • There are n product streams, each rich in one component. • Each component is recovered in only one product stream. • Each product is recovered from only one location. • There are no intermediate reboilers or condensers. • There is no thermal coupling between columns.

  5. Basic and Non-Basic Configurations Three cases of quaternary distillation configurations • 3 columns (N-1) • Only 1 stream for each product • Each column has 1 condenser at the top and 1 reboiler at the bottom • 4 columns (N) • 2 streams for product C • Each column has 1 condenser at the top and 1 reboiler at the bottom • 3 columns (N-1) • Only 1 stream for each product • Fully coupled Basic Non-Basic Non-Basic

  6. Basic and Non-Basic Configurations • Multiplicity: the number of section groupings for a given topology. • Same nodes, same edges, different way of connecting nodes and edges-different graphs. • Multiplicity=1 for all basic configurations

  7. How many basic configurations?

  8. For quaternary distillations, the best network vapor flow for all basic and non-basic configurations(V*basic / V*non-basic)

  9. Extended Basic Configuration Extensible Basic Configuration If the same product is desired at two purities • Same number of columns • Same number of distillation/bottom • 1 more stream for product

  10. Mathematical Framework for Searching Basic Configurations • Search for all basic configurations (with external constraints) , and eliminate all non-basic configurations • Incorporate design constraints

  11. Mathematical Framework for Searching Basic Configurations • A Configuration-A Directed Graph • Nodes-Streams • Edges-Columns

  12. Constraints • Material balance • 1 distillation and 1 bottom for each collumn • Basicity ----------------------------------------------------------- • External Constraints • Thermally Coupled Configurations

  13. Examples • ABC • xABCAB + xABCA = xABCDABC • xABCBC + xABCC = xABCDABC • Sum (xout * Componentsout) ≥ Sum (xin) * Componentsnode • xABCDA + 2xABCDAB + 3xABCDABC + 3xABCDBCD + 2xABCDCD + xABCDD ≥ 4 • xBC->B + xBCD->B ≤ 1

  14. Examples • ABCD-AB/BCD • XABCD-BCD=1 • XABCD-CD=1 • B distillate • XAB-B=0 • Thermally Coupled Configurations • Let y be the variable represents the backward flow of each non-product edge • y≤x

  15. Practice structure = 2 3 4 5 5 6 7 8 8 9 8 9 9 10 • x(1,:)=[0.25 0.25 0.25 0.25]; • x(2,:)=[0.25 0.1591 0.075885 0]; • x(3,:)=[0 0.090901 0.17411 0.25]; • x(4,:)=[0.25 0.081123 0 0]; • x(5,:)=[0 0.077977 0.075885 0]; • x(6,:)=[0 0.090901 0.082905 0]; • x(7,:)=[0 0 0.091209 0.25]; • x(8,:)=[0.25 0 0 0]; • x(9,:)=[0 0.081123 0 0]; • x(10,:)=[0 0.16888 0 0]; • x(11,:)=[0 0 0.15879 0]; • x(12,:)=[0 0 0.091209 0]; • x(13,:)=[0 0 0 0.25];

  16. Conclusion • Basic and non-basic configurations • Performance and extensibility of basic configurations • Mathematical framework for searching basic configurations • Practices

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