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Prarancangan Pabrik Metanol Dari Batubara Dengan Proses Gasifikasi Kapasitas Produksi 100.000 Ton/Tahun

机译:年产100,000吨气化煤制甲醇装置的设计。

摘要

Methanol plant with raw material from gas synthesis of coal capacity 100.000 ton/years operated 330 days per years. Methanol manufactured process using fixed bed reactor. Reaction on fixed bed reactor occur gas phase, and exothermic, with operation condition non adiabatic at temperatur 2000C and pressure 48 atm. This industry include kind of high risk because operate above atmospheric pressure.udCoal demand as much as 12.626,262 kg/hours. The product is methanol as much as 9.097,242 kg/hours. Utility process include water supply from river (Kapuas, West Kalimantan), steam supply from boiler with diesel fuel, electricity needs supplied by PLN and 1 generator set 500 kW as stand-by with diesel fuel. This plant is established in Rasau, West Kalimantan, Indonesia, on 2025, with land area 28.575 m2 and employees 159 people.udThe results of the economic analysis of the obtained methanol plant pradesign fixed capital investment (FCI) of Rp 149.619.846.137 and working capital (WC) Rp 88.799.730.394. Feasibility analysis results obtained from the return on investment (ROI) before tax after tax 44,82% and 31,37%. Pay Out Time (POT) before and after- tax 1,82 and 2,42 of years. Break Even Point (BEP) 42,05%, Shut Down Point (SDP) of 22,65% and a Discounted Cash Flow (DCF) of 30,28%. The results of the economic analysis concluded that the methanol plant from coal with gasification process capacity of 100.000 ton/year is feasible to set.
机译:以天然气合成气为原料的甲醇装置以10万吨/年的产能运行,每年运行330天。甲醇采用固定床反应器制造。在固定床反应器上的反应发生在气相中,并且放热,在2000℃的温度和48 atm的压力下,操作条件为非绝热的。该行业包括高风险行业,因为它是在高于大气压的条件下运行的。 ud煤炭需求高达12.626,262公斤/小时。该产品的甲醇含量高达9.097,242公斤/小时。公用事业过程包括:从河流(卡普阿斯,西加里曼丹)供水,从锅炉供应柴油燃料的蒸汽,PLN和1台发电机组500 kW备用柴油发电机组的电力需求。该工厂建于2025年,位于印度尼西亚西加里曼丹西部的拉绍,占地面积28.575平方米,员工159人。 ud获得的甲醇工厂的经济分析结果为pradesign固定资本投资(FCI)Rp 149.619.846.137和营运资金(Rp)88.799.730.394。从税后税前投资回报率(ROI)获得的可行性分析结果为44,82%和31,37%。税前和税后的1,82年和2,42年的支付时间(POT)。收支平衡点(BEP)为42.55%,停机点(SDP)为22.65%,折现现金流(DCF)为30.28%。经济分析结果表明,煤气化工艺能力为100.000吨/年的煤制甲醇装置是可行的。

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