 
| Set CHEMIMP | |
|---|---|
| Source: | David Bogle, Imperial College, London | 
| Discipline: | Chemical engineering | 
| Accession: | August 1982 | 
Five matrices extracted from runs of the chemical engineering package SPEED UP. In each case, the matrix is the initial Jacobian approximation for a sparse nonlinear equation modeling a chemical process system.
Unsymmetric with many zeros on the diagonal. Some of the entries actually have the value zero. This happens when a procedure is used in which all outputs are incorrectly assumed to be a function of all inputs.
 These matrices can be significantly reduced by block triangularization methods.
![[impcol_a Icon]](impcol_a_tiny.gif) IMPCOL A  (real unsymmetric, 207  by 207, 572 entries), Heat exchanger network
 IMPCOL A  (real unsymmetric, 207  by 207, 572 entries), Heat exchanger network
![[impcol_b Icon]](impcol_b_tiny.gif) IMPCOL B  (real unsymmetric, 59  by 59, 312 entries), Cavett's process
 IMPCOL B  (real unsymmetric, 59  by 59, 312 entries), Cavett's process
![[impcol_c Icon]](impcol_c_tiny.gif) IMPCOL C  (real unsymmetric, 137  by 137, 411 entries), Ethylene plant model
 IMPCOL C  (real unsymmetric, 137  by 137, 411 entries), Ethylene plant model
![[impcol_d Icon]](impcol_d_tiny.gif) IMPCOL D  (real unsymmetric, 425  by 425, 1339 entries), Nitric acid plant model
 IMPCOL D  (real unsymmetric, 425  by 425, 1339 entries), Nitric acid plant model
![[impcol_e Icon]](impcol_e_tiny.gif) IMPCOL E  (real unsymmetric, 225  by 225, 1308 entries), Hydrocarbon separation problem
 IMPCOL E  (real unsymmetric, 225  by 225, 1308 entries), Hydrocarbon separation problem
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