It was shown in an earlier work by us that entropy generation and energy (hot utility or cold utility) consumption of isothermal, isobaric reactor networks depend only on the network's inlet and outlet stream compositions and flow rates and are not dependent on the reactor network structure, as long as the universe of realizable reactor units and network outlet mixing units are either all endothermic interacting with a single hot reservoir, or all exothermic interacting with a single cold reservoir, respectively. It is shown that when the universe of realizable reactor/mixer units, of isothermal, isobaric, continuous stirred tank reactor networks, consists of both endothermic units interacting with a single hot reservoir and exothermic units interacting with a single cold reservoir, the network's net (hot minus cold) utility consumption depends only on the network's inlet and outlet stream compositions and flow rates (and does not depend on the network's structure). In contrast, the network's entropy generation depends on the network's inlet and outlet stream compositions and flow rates, and the network's hot utility (or cold utility) consumption. The latter, in general, depends on the network structure, thus making entropy generation also, in general, depend on network structure. Thus, the synthesis of isothermal, isobaric reactor networks, with fixed inlet and outlet stream specifications, is equivalent to the synthesis of minimum hot (or cold) utility consuming such networks. The Infinite DimEnsionAl State-space conceptual framework is used for the problem's mathematical formulation, which is then used to rigorously establish the above equivalence. A case study involving Trambouze kinetics demonstrates the findings. sible reactor units include units of both the exothermic and endothermic type. The IDEAS framework decomposes a reactor network into an operator, OP network, where the reactor unit operations occur, and a distribution, DN network, where the flow operations (mixing, splitting, recycling, and bypass) occur. IDEAS has been successfully applied to numerous globally optimal process network synthesis problems, such as mass exchange network synthesis, 8 complex distillation network synthesis, 9-11 power cycle synthesis, 12 reactor network synthesis, 13,14 reactive distillation network synthesis, 15 separation network synthesis, 16 attainable region construction, 17-20 and batch attainable region construction. 21 The rest of the article is structured as follows: CSTR models using a mass basis and a molar basis are presented, the applicability of IDEAS to the entropy generation and energy consumption quantification problem is demonstrated, and the resulting IDEAS mathematical formulation is presented. Next, properties of the entropy generation and net energy consumption functions are rigorously established in a theorem, which establishes the net energy consumption function's dependence on only network inlet and outlet information, and the entropy generation function's dependence on both network inlet and ou...