Page 369 - Sustainability in the Process Industry Integration and Optimization

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batch processes: carbon footprint (CFP) (Cont.):
increase in value of objective defined, 2
function, 160 PI application, 13
infeasible solution generated by and product life-cycle assessment,
MILP approach, 160 2–3
number produced of each carbon neutrality studies, 2
product, 280 Carbon Trust, 5
optimal solution generated by case studies/examples:
S-graph, 161 de-bottlenecking HI crude-oil
process optimization frameworks distillation system, 256–262
and scheduling of, 159–163 energy efficiency in other food/
S-graphs and, 160–161 drink industries, 268–271
BCCs. See Balanced Composite Curves energy recovery from FCC unit,
best available techniques (BAT), water 253–256
and, 107–108 heat pinch technology, 219–226
bilinear optimization problem, 27 heat/power integration in
binary variable, 27 buildings/building
biofuels, 3 complexes, 275–277
biorefineries, green: industrial applications and, 253–280
flowsheet of, 173 industrial utility systems synthesis,
solution network for workflow 271–275
synthesis problem, 172 minimizing water/wastewater in
synthesis of, 171–173 citrus juice plant, 262–268
BIS (Department for Business, optimal design of supply chain,
Innovation and Skills), 297 277–279
black box (steady-state model), 23–24 scheduling large-scale paint
blue water, virtual, 109 production system, 279–280
bounding function, role in solving total sites, 226–233
MIP, 32 utility placement, 238–246
branch and bound approach, for water pinch technology, 247–252
solving discrete problems, 31 CCs. See Composite Curves
budget-income-time pinch analysis: Center for Engineering and
CCs for project budget and income, Sustainable Development
132 Research, De La Salle
PI and, 131–133 University, 297
project budget and income with Centre for Advanced Process
time, 132 Decision-Making, Carnegie
Mellon University, 297
C C Centre for Process Integration,
University of Manchester, 8, 13,
Canadian Society for Chemical 297, 301, 305, 307
Engineering, 11 Centre for Process Integration and
CAPE (Computer Aided Process Intensification, European
Engineering), 11 Community Project, 298, 302,
capital costs: 305, 307
data extraction with operating and, Centre for Process Systems
290–292 Engineering, Imperial College
heat transfer area, total cost London, 298, 310
targeting and, 69–70 Centre for Technology Transfer in the
carbon dioxide emissions (CO ), 138– Process Industries, Bucharest, 298
2
139 CFP. See carbon footprint
costs related to, 2 Charles Parsons Institute, University
FC-based systems and, 9 of Limerick, 298, 302, 305, 308
FCs, gas turbines and, 4 CHEMCAD, 205–206
carbon footprint (CFP), 20 Chemical Engineering, Chemical
conclusions and further Equipment Design and
information, 319–320 Automation (CHISA), 296