Gas-to-Methanol Production at Lower Operating Conditions: Techno-economic Analysis of SMR, ATR, and DMR

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Abstract

Methanol production is basically through the traditional methods of Steam Methane Reforming (SMR), Auto-Thermal Reforming (ATR), and Dry Methane Reforming (DMR). However, the process is usually energy intensive, up to 100 bar and 1000oC, leading to high associated and operating costs. This study investigates the techno-economic feasibility of methanol synthesis at lower temperatures and pressures, based on the equilibrium expression presented by Turton, et al. Three (3) methanol production routes were investigated; The Steam Methane Reforming (SMR), the Auto-Thermal Reforming (ATR), and the Dry Methane Reforming (DMR). The peculiarity in each production option was simulated using Aspen HYSYS v11 software. The process parameters were rigorously optimized using the optimizer tool in Aspen HYSYS V11, in order to achieve the most economical yield while meeting the acceptable quality benchmark for the product. The initial simulations were carried out using values from the upper end of the operating ranges as stated in literatures. While monitoring the product yield and quality, the process operating parameters which essentially are the pressures and temperatures point to point through the flow schemes, were reduced to either the lower end of the operating ranges or even much lower provided, an optimum product yield rate and quality was obtained as output. The involved process equipment was sized on a preliminary level in order to estimate the plant cost using the same feed rate of 100MMscf/d of natural gas for all three cases. The simulation results showed that methanol synthesis was optimized at 40o C and 15 bar. a. Furthermore, the ATR option gave the most methanol throughput at 5128.8 MTPD, the SMR option produced 4802.4 MTPD, while the DMR had the least output at 3434.4 MTPD. All three cases proved profitable, with a payback period ranging between 4.82 to 6.52 years. Despite requiring the most capital investment of USD2.136 billion, the ATR option is the most viable technology for this production scale and the quickest to pay back invested capital (4.82 years). As such, it is the most recommended option.
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低操作条件下的气制甲醇生产:SMR、ATR和DMR的技术经济分析
甲醇生产基本上是通过传统的蒸汽甲烷重整(SMR)、自动热重整(ATR)和干式甲烷重整(DMR)方法进行的。然而,该过程通常是能源密集型的,高达100巴和1000摄氏度,导致高相关和运营成本。本研究在Turton等人提出的平衡表达式的基础上,探讨了在较低温度和压力下合成甲醇的技术经济可行性。考察了3条甲醇生产路线;蒸汽甲烷重整(SMR)、自动热重整(ATR)和干式甲烷重整(DMR)。使用Aspen HYSYS v11软件模拟每个生产选项的特性。利用Aspen HYSYS V11中的优化工具对工艺参数进行了严格优化,以实现最经济的产量,同时满足产品可接受的质量基准。最初的模拟是使用文献中规定的操作范围上端的值进行的。在监测产品收率和质量的同时,工艺操作参数(本质上是通过流动方案点对点的压力和温度)被降低到操作范围的下端,甚至更低,以获得最佳的产品收率和质量作为输出。所涉及的工艺设备在初步水平上进行了评估,以便在所有三种情况下使用相同的进给量为100万立方英尺/天的天然气来估计工厂成本。模拟结果表明,在40℃、15 bar条件下,甲醇的合成是最优的。a.此外,ATR选项的甲醇产量最高,为5128.8 MTPD, SMR选项的甲醇产量为4802.4 MTPD,而DMR的产量最低,为3434.4 MTPD。这三个案例都证明是有利可图的,投资回收期在4.82年至6.52年之间。尽管需要21.36亿美元的资本投资,但ATR选项是该生产规模最可行的技术,也是最快收回投资的技术(4.82年)。因此,它是最推荐的选项。
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