Alturkistani Sultan, Wang Haoyi, Gautam Ribhu, Sarathy S Mani
Physical Sciences and Engineering Division, King Abdullah University of Science and Technology (KAUST), CCRC, Thuwal, Jeddah 23955-6900, Saudi Arabia.
Physical Sciences and Engineering Division, King Abdullah University of Science and Technology (KAUST), KAUST Catalysis Center, Thuwal, Jeddah 23955-6900, Saudi Arabia.
ACS Omega. 2023 May 30;8(23):21223-21236. doi: 10.1021/acsomega.3c02350. eCollection 2023 Jun 13.
Oxidative coupling of methane (OCM) is a promising process for converting natural gas into high-value chemicals such as ethane and ethylene. The process, however, requires important improvements for commercialization. The foremost is increasing the process selectivity to C (CH + CH) at moderate to high levels of methane conversion. These developments are often addressed at the catalyst level. However, optimization of process conditions can lead to very important improvements. In this study, a high-throughput screening (HTS) instrument was utilized for LaO/CeO (3.3 mol % Ce) to generate a parametric data set within the temperature range of 600-800 °C, CH/O ratio between 3 and 13, pressure between 1 and 10 bar, and catalyst loading between 5 and 20 mg leading to space-time between 40 and 172 s. Statistical design of experiments (DoE) was applied to gain insights into the effect of operating parameters and to determine the optimal operating conditions for maximum production of ethane and ethylene. Rate-of-production analysis was used to shed light on the elementary reactions involved in different operating conditions. The data obtained from HTS experiments established quadratic equations relating the studied process variables and output responses. The quadratic equations can be used to predict and optimize the OCM process. The results demonstrated that the CH/O ratio and operating temperatures are key for controlling the process performance. Operating at higher temperatures with high CH/O ratios increased the selectivity to C and minimized CO (CO + CO) at moderate conversion levels. In addition to process optimization, DoE results also allowed the flexibility of manipulating the performance of OCM reaction products. A C selectivity of 61% and a methane conversion of 18% were found to be optimum at 800 °C, a CH/O ratio of 7, and a pressure of 1 bar.
甲烷氧化偶联(OCM)是一种将天然气转化为乙烷和乙烯等高价值化学品的很有前景的工艺。然而,该工艺要实现商业化还需要重大改进。首要的是在中等到高甲烷转化率水平下提高该工艺对C₂(C₂H₄ + C₂H₆)的选择性。这些改进通常在催化剂层面进行探讨。然而,工艺条件的优化也能带来非常重要的改进。在本研究中,使用了一台高通量筛选(HTS)仪器对La₂O₃/CeO₂(3.3摩尔% Ce)进行研究,以在600 - 800℃的温度范围内、CH₄/O₂比在3至13之间、压力在1至10巴之间以及催化剂负载量在5至20毫克之间生成一组参数数据集,从而得到40至172秒的时空。应用实验设计(DoE)来深入了解操作参数的影响,并确定乙烷和乙烯最大产量的最佳操作条件。通过生产速率分析来揭示不同操作条件下所涉及的基元反应。从HTS实验获得的数据建立了将所研究的工艺变量与输出响应相关联的二次方程。这些二次方程可用于预测和优化OCM工艺。结果表明,CH₄/O₂比和操作温度是控制工艺性能的关键。在较高温度和高CH₄/O₂比下操作可提高对C₂的选择性,并在中等转化率水平下使CO₂(CO₂ + CO)最小化。除了工艺优化外,DoE结果还允许灵活调控OCM反应产物的性能。发现在800℃、CH₄/O₂比为7和压力为1巴时,C₂选择性为61%且甲烷转化率为18%是最佳的。