(52d) Practical Process Integration Retrofit Part 4. Handling Large Projects
AIChE Spring Meeting and Global Congress on Process Safety
2012
2012 Spring Meeting & 8th Global Congress on Process Safety
15th Topical on Refinery Processing
Heat Integration Retrofit Tutorial
Tuesday, April 3, 2012 - 10:15am to 10:45am
Practical Process Integration Retrofit
Part 4. Dealing with Large
Projects
G.T.Polley
The ?Cross-Pinch Method? is
suitable for use in identify retrofits when the number of streams is small (the
example used in the demonstration of this method had seven streams, Polley
[2011]). However, ?Pinch Technology? is based on the assumptions that capital
cost expenditure is controlled by the cost of heat exchangers and factors such
as network operability can initially be ignored. With small projects
operability considerations are easily undertaken by an experienced process
engineer as the revamp is developed. With large projects this is difficult. The
evaluation of the capital cost of a revamp can often be dominated by the cost
of piping a modification to ?civils?. With small sized projects an experienced
process engineer can incorporate a consideration of these factors as a network
structure is developed. With large projects this is not possible.
The solution to this problem
is to decompose large networks into a number of smaller self contained
networks.
References
Tjoe T.N. & Linnhoff B.
?Using pinch technology for process retrofit?, Chem.Engng., 1986 April 28,
pp47-60
Ahmad S. & Linnhoff B.
?Supertargeting: Different process structures for different economics?, ASME
J.En.Res.Tech., 1989, 111(3), 131-136
Tjoe T.N. Ph.D. Thesis 1986,
UMIST, UK
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