The gas compression units in the processing plant are used for various purposes. Compression of the associated gas is designed to adjust for the different operating pressures. In addition, the injection of CO2 into oil reservoirs is used for enhanced oil recovery (EOR) and/or reduction of environmental impact. These systems utilize dozens of megawatts of electrical energy and intercooling for each compression stage. Therefore, the equipment used is energy-intensive and not thermodynamically efficient. An Organic Rankine Cycle (ORC) technology produces electrical energy from heat sources with low to medium temperature levels (90°C -150°C). In the present work, a model of an ORC integrated with the intercoolers of the compression units is used to simulate the energy conversion of the system. Next, various working fluids, such as R123, nbutane, n-pentane, hexane, and n-heptane, are considered. The results show a possibility of net power generation by R123 ORC of up to 40 MW. Furthermore, only an increase of 0.95% in the CO2 molar fraction of the flue gas leads to an increase of 1.29E8 kJ/h in the cooling demands of the CO2 removal and compression units. Moreover, the presented increase in cooling demands creates the possibility of net power generation of up to 41 MW by ORC. Furthermore, in terms of footprint, this integrated system can be implemented in onshore structures and with some modifications in the condenser in offshore plants. Finally, this integrated system reduces environmental impacts by generating power from waste heat sources.