In this study, the simultaneous production of ammonia and methyl formate (MF) in a thermally coupled reactor has been investigated. Since the ammonia synthesis reaction is associated with heat release, and the production of MF is an endothermic reaction, the ammonia production reaction supplies the heat required for MF's reaction in the proposed reactor. To justify the suggested model's accuracy, the results are verified with the same condition's experimental data. This reactor's benefits include the elimination of ammonia synthesis inter-stage coolers, and reduced energy consumption. Also, exchanged heat causes significant improvements in both equilibrium reactions and enhanced process performance. On the other hand, by the novel configuration reactor, the methanol dehydrogenation reaction's hydrogen supplied about 21.57% of the required hydrogen in ammonia production feed. Eventually, the effect of input parameters on reactor performance investigates by using the sensitivity analysis and optimization process. It also found that about 34.66% of required hydrogen in ammonia synthesis feeds by methanol dehydrogenation reaction in optimum conditions supplied.

在这项研究中，研究了在热耦合反应器中同时生产氨和甲酸甲酯 (MF)。由于氨合成反应与放热有关，并且MF的产生是吸热反应，因此氨产生反应提供了所提出的反应器中MF反应所需的热量。为了证明建议模型的准确性，使用相同条件的实验数据验证结果。该反应器的优点包括消除氨合成级间冷却器和降低能耗。此外，热交换会显着改善平衡反应和增强工艺性能。另一方面，通过新型配置的反应器，甲醇脱氢反应的氢气供应量约为21。氨生产原料中所需氢气的 57%。最后，通过使用敏感性分析和优化过程来研究输入参数对反应器性能的影响。还发现通过甲醇脱氢反应在最佳条件下提供氨合成原料中所需氢气的约34.66%。