LEADER 00000nam 2200385 4500
001 AAI3123778
005 20050228064437.5
008 050228s2004 eng d
035 (UnM)AAI3123778
040 UnM|cUnM
100 1 Maravelias, Christos T
245 10 Mixed-integer and constraint programming methods for the
scheduling of batch processes and the new product
development
300 169 p
500 Source: Dissertation Abstracts International, Volume: 65-
02, Section: B, page: 0886
500 Adviser: Ignacio E. Grossmann
502 Thesis (Ph.D.)--Carnegie Mellon University, 2004
520 This thesis deals with the development of optimization
models in order to address: (a) the scheduling of batch
plants, and (b) the simultaneous scheduling of tests and
design of batch plants that arise in the New Product
Development (NPD) of pharmaceutical and agrochemical
industries
520 To address the issue of developing computationally
effective methods for the scheduling of multipurpose batch
plants, three optimization approaches are proposed
520 A novel continuous-time MILP formulation is proposed, that
relies on the State Task Network (STN) and addresses the
general problem of batch scheduling, accounting for
resource (utility) constraints, variable batch sizes and
processing times, various storage policies (UIS/FIS/NIS/
ZW), batch mixing/splitting, and sequence-dependent
changeover times. The proposed model is significantly
faster than other continuous-time models and more general
than event-driven formulations being equally fast
520 A hybrid MILP/CP algorithm is proposed, where the original
scheduling problem is decomposed into a MILP master
problem and a CP subproblem. The decisions about the type
and number of tasks performed, as well as the assignment
of units to tasks are made by the MILP master problem,
while the CP subproblem checks the feasibility of a
specific assignment and generates integer cuts. To enhance
the performance of the algorithm, a graph-theoretic
preprocessing that determines time windows for the tasks
and equipment units and two new classes of integer cuts
are proposed. The proposed framework can be used for
various plant topologies and objective functions.
Numerical results show that for some classes of problems,
it is two to three orders of magnitude faster than
standalone MILP and CP models
520 In the second part of the thesis we present optimization
models for the solution of problems that arise in the New
Product Development of agrochemical and pharmaceutical
industries. (Abstract shortened by UMI.)
590 School code: 0041
590 DDC
650 4 Engineering, Chemical
650 4 Operations Research
650 4 Engineering, Industrial
690 0542
690 0796
690 0546
710 20 Carnegie Mellon University
773 0 |tDissertation Abstracts International|g65-02B
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