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Prarancangan Pabrik Fatty Alcohol Ethoxylate Dari Fatty Alcohol Dan Etilen Oksida Kapasitas 52.000 Ton/Tahun

机译:由脂肪醇和环氧乙烷生产52,000吨/年的脂肪醇乙氧基化装置设计。

摘要

Surfactant industry needs increased with the growth of development in Indonesia. The increases od surfactant needed will increase the need for Fatty Alcohol ethoxylate (FAE), which is one of the ingredients in the manufacture of surfactants. Besides being used industrial surfactants, FAE is also used as an ingredient in cosmetics, pharmaceuticals and textiles. To fulfill domestic needs and their export opportunities that are still open, FAE factory is designed with a capacity of 50.000 tons/year. This factory will be established in Cilegon, Banten at 2020. ududRaw material for manufacturing FAE is fatty alcohol and ethylene oxide and potassium hydroxide (KOH) as catalyst. The process step is divided to 3 steps, there are activation catalyst, manufacturing product in reactor and purification product. First step, mixing fatty alcohol and KOH catalyst 0,5% weight of fatty alcohol at temperature of 180 °C in 30 minutes in the mixer. In this process, activation catalyst is happened. Second step, the solution is fed to bubble reactor and reacted with ethylene oxide at temperature of 180 °C and pressure 2 atm, this reaction is called ethoxylation. The conversion as long as manufacturing product in reactor is 84,43%. Last step, the product will be refined at distillation column, so the conversion will increase into 99,8%.ududFrom economic analysis shows Percent Return On Investment before tax = 41,37 %; Percent Return On Investment after tax = 31,03%, Pay Out Time before tax = 1,95 years; Pay Out Time after tax = 2,44 years. Break Even Point (BEP) = 41,84%; Shut Down Point (SDP) = 20,75%, Discounted Cash Flow (DCF) = 38,64%. The conclusion from this economic analysis is the factory is feasible to established.
机译:随着印度尼西亚的发展,对表面活性剂行业的需求也增加了。表面活性剂需求的增加将增加对脂肪醇乙氧基化物(FAE)的需求,脂肪醇乙氧基化物是制造表面活性剂的成分之一。除了用作工业表面活性剂外,FAE还用作化妆品,药​​品和纺织品的成分。为了满足仍需满足的国内需求及其出口机会,FAE工厂的设计产能为5万吨/年。该工厂将于2020年在万丹的Cilegon建立。 ud ud用于制造FAE的原料是脂肪醇,环氧乙烷和氢氧化钾(KOH)作为催化剂。工艺步骤分为三个步骤,分别是活化催化剂,反应器中的生产产物和纯化产物。第一步,在混合器中于30分钟内在180°C的温度下混合脂肪醇和KOH催化剂0.5%的脂肪醇。在此过程中,发生了活化催化剂。第二步,将溶液进料到鼓泡反应器中,并在180°C的温度和2 atm的压力下与环氧乙烷反应,该反应称为乙氧基化。只要反应器中的制造产品的转化率为84.43%。下一步,将在蒸馏塔中对产品进行精制,因此转化率将提高到99.8%。 ud ud经济分析显示,税前投资回报率= 41.37%;税后投资回报率= 31,03%,税前支付时间= 1,95年;税后支付时间= 2,44年。收支平衡点(BEP)= 41.84%;停机点(SDP)= 20.75%,折现现金流(DCF)= 38.64%。这项经济分析的结论是工厂是可行的。

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