| Symbols used | ||
| A | - | binary variable |
| a | - | coefficient in the matrix |
| AL × I | - | matrix of input data |
| AH | [m2] | surface of the heater |
| AC | [m2] | surface of the cooler |
| AEX | [m2] | surface of the heat exchanger |
| B | - | binary variable |
| CF | [kW・K−1] | heat flow |
| CP | [J・(kg・K)−1] | heat capacity |
| C | [EUR・kg−1], [EUR・(GJ)−1] | price of raw materials, products and UC |
| ddv | [%] | tax |
| E | [kWh・a−1] | energy productivity |
| H | [kJ・mol−1] | standard reaction enthalpy |
| I0 | [kEUR] | investment of process units |
| k | - | mass conversion |
| kH | [kW・(K・m2)−1] | heat transfer coefficient of the heater |
| kC | [kW・(K・m2)−1] | heat transfer coefficient of the cooler |
| kEX | [kW・(K・m2)−1] | heat transfer coefficient of the heat exchanger |
| M | [kg・kmol−1] | molar mass |
| MB | [m2], [m3], [kW] [kEUR・a−1] | the big-M |
| qm | [kg・h−1] | mass flow |
| QC | [kW] | consumption of cold UC |
| Rm | [kJ・(kmol・k)−1] | general gas constant |
| RH | [kW・k−1] | consumption of hot UC |
| P | [bar] | pressure |
| P | [kW] | power |
| UC | [kWh・a−1] | consumption of utility |
| t | [h], [a] | time |
| T | [˚C], [˚K], | temperature |
| V | [m3] | volume |
| Z | - | binary variable |
| Z | [kEUR・a−1] | maximized annual profit |
| X | - | molar yield |
| y | - | binary variable |
| yI × I | - | matrix of binary variables |
| AMORT | [kEUR・a−1] | cost of amortization of process units |
| odh | [kEUR・a−1] | expenses |
| O PER | [kEUR・a−1] | additional operating costs |
| prod | [kEUR・a−1] | income of the sale of products |
| prod_steam | [kEUR・a−1] | sale of medium pressure steam |
| prih | [kEUR・a−1] | incomes |
| PROF | [kEUR・a−1] | annual profit |
| raw | [kEUR・a−1] | cost of raw materials |
| TAXE | [kEUR・a−1] | emission taxes |