Nitric acid plant with raw materials of sulphuric acid and sodium nitrate with a capacity 65.000 tons/year is planned to be established in 2020 in Karawang, West Java. The sodium nitrate is imported from Chile and the sulphuric acid is from PT Indonesian Acid Industry. The nitric acid production uses continuous stirred tank reactor (CSTR). The reaction is exothermic, non adiabatic, and irreversible, carried out at temperature of 150°C and pressure of 1 atm. The plant is categorized as low risk process due to the friendly operating conditions. The process of nitric acid production is initiated with reacting sulphuric acid and sodium nitrate in the reactor. The vapor product of reactor is condensed by a partial condenser and is purified in distillation tower to produce nitric acid with purity of 98%, while the liquid product, called niter cake, is stored as side product. Based on the capacity, the production of nitric acid is 8,207.0707 kgs/hour. To support the process, utilities are required including 264,779.5449 kgs/hour of cooling water, 19,772.5449 kgs/hour of steam. Which is obtained from boiler consuming fuel oil as much as 1,473.8109 L/hour, and electricity supplied from PLN and generator set. The water source is taken from Kalimalang river,. The economic analysis gives the profit before tax is Rp113,168,435,407/year, and Rp84,876,326,556/year after tax. The percent Return on Investment (ROI) before tax is 34.52% and 25.89% after tax. The Pay Out Time (POT) before tax is 2.25 years and 2.79 years after tax. The Break Event Point (BEP), the Shut Down Point (SDP), and the Internal Rate of Return (IRR) are 47.80, 25.11%, and 40.27%, respectively. The above economic analysis concludes that the plant is feasible to set.
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机译:计划于2020年在西爪哇省卡拉旺建立年产65,000吨/年硫酸和硝酸钠原料的硝酸厂。硝酸钠从智利进口,硫酸从PT Indonesian Acid Industry进口。硝酸生产使用连续搅拌釜反应器(CSTR)。该反应是放热的,非绝热的且不可逆的,在150℃的温度和1atm的压力下进行。由于友好的操作条件,该工厂被归类为低风险过程。硝酸的生产过程通过在反应器中使硫酸和硝酸钠反应而开始。反应器的蒸气产物通过部分冷凝器冷凝,并在蒸馏塔中进行纯化,以产生纯度为98%的硝酸,而液体产物称为硝化饼,则作为副产物存储。根据产能,硝酸产量为8,207.0707公斤/小时。为了支持该过程,需要公用设施,包括264,779.5449公斤/小时的冷却水,19,772.5449公斤/小时的蒸汽。锅炉耗油量高达每小时1,473.8109升,而PLN和发电机组则提供电力。水源取自卡里玛琅河。经济分析得出,税前利润为Rp113,168,435,407 /年,税后利润为Rp84,876,326,556 /年。税前投资回报率(ROI)为34.52%,税后为25.89%。税前支付时间(POT)为2.25年和税后2.79年。中断事件点(BEP),关闭点(SDP)和内部收益率(IRR)分别为47.80、25.11%和40.27%。以上经济分析认为该装置可行。
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