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Prarancangan Pabrik Polistirena Dengan Proses Polimerisasi Larutan Kapasitas 70.000 Ton/Tahun

机译:年产7万吨聚合工艺聚苯乙烯装置的设计。

摘要

Polystyrene is a thermoplastic polymer using raw materials of styrene monomer with assisted solvent ethyl benzene and benzoyl peroxide initiator. Particularly High Impact polystyrene has a number of uses as household appliances, food wrapping, insulation, and furniture. Needs of polystyrene in Indonesia is quite high from 2006-2015 are likely to experience increased. Polystyrene plant capacity of 70.000 tonnes/year operation for 330 days. In the manufacture of polystyrene comparison between raw materials, solvents of 1:0,05492. The reaction that occurs in the manufacture of polystyrene that is an exothermic reaction using reactor CSTR (Continous Stirred Tank Reactor) because the converted liquid-liquid. Operating conditions are maintained at a temperature of 90°C (isothermal) and a pressure of 1 atm. Polystyrene plant with a capacity of 70.000 tonnes/year using the raw materials of styrene monomer of 12.575,8271 kg/h ethyl benzene of the impurities with 50,5053 kg/h ethyl benzene solvent, to of 690,6644 kg/h with the impurities of toluene and benzene respectively amounted to 0,0691 kg and 0,6222 kg/h, and benzoyl peroxide initiator of 20,5071 kg/h. In the manufacture of polystyrene requires supporting units namely air, steam, electric, and compressed air. For the needs of water obtained from the River as much as 3.249,4677 kg/h. Steam needs as much as 659,3500 kg/h of boiler with diesel fuel as much as 0,0607 m3/hour. Electricity needs as much as 335,6026 kW obtained from PLN and as a backup generator that has a capacity of 1.000 kW using fuel as much as 0,1145 m3/hour. Compressed air needs as much 71.064 m3/hour. This direnacanakan the factory located in Serang, Banten, with a land area of 14,800 m2 and employs 128 people. Economic analysis of polystyrene plant is in need of fixed capital amounted to Rp 297.722.649.279 and Rp 148.745.508.634 of working capital. While profit before tax of Rp. 131.171.167.310/year. Profit after tax of Rp 101.378.375.483/year. This feasibility analysis it can be concluded that the Percent Return On Investment (ROI) of 45,40% before tax and after tax of 34,05%. Pay Out Time (POT) before tax of 1,80 years and after tax of 2,27 years. Break Even Point (BEP) of 41,48% capacity and Shut Down Point (SDP) of 27,30% capacity. Discounted Cash Flow (DCF) for 31,75%. Based on the analysis of the feasibility of the polystyrene plant is quite interesting and worth to be established.
机译:聚苯乙烯是一种热塑性聚合物,使用苯乙烯单体的原料以及辅助溶剂乙苯和过氧化苯甲酰引发剂。特别是高抗冲聚苯乙烯有许多用途,如家用电器,食品包装,隔热材料和家具。从2006年至2015年,印度尼西亚对聚苯乙烯的需求可能会增加。聚苯乙烯工厂的产能为7万吨/年,运营330天。在制造聚苯乙烯的原料之间进行比较,溶剂为1:05492。在聚苯乙烯生产中发生的反应是使用反应器CSTR(连续搅拌釜反应器)的放热反应,因为已转化为液-液。操作条件保持在90°C(等温)的温度和1个大气压的压力下。聚苯乙烯装置的年产能为70.000吨/年,使用的苯乙烯单体原料的杂质为12.575,8271 kg / h乙苯和50,5053 kg / h乙苯溶剂,至690,6644 kg / h。甲苯和苯的杂质含量分别为0,0691 kg和0,6222 kg / h,过氧化苯甲酰引发剂为20,5071 kg / h。在聚苯乙烯的制造中,需要支撑单元,即空气,蒸汽,电和压缩空气。对于从河流获得的水的需求量高达3.249,4677公斤/小时。蒸汽需要高达659,3500 kg / h的锅炉,而柴油则需要高达0,0607 m3 / h。从PLN获得的电力需要多达335,6026 kW,而作为备用发电机(使用1.01立方米/小时的燃料,容量为1.000 kW)。压缩空气每小时需要71.064立方米。这个direnacanakan工厂位于万丹Serang,占地面积14800平方米,拥有128名员工。聚苯乙烯工厂的经济分析需要的固定资本为Rp 297.722.649.279和Rp 148.745.508.634。而税前利润为Rp。 131.171.167.310/年。税后利润为Rp 101.378.375.483/年。通过此可行性分析,可以得出税前和税后的投资回报率(ROI)为45.40%,税后为34.05%。税前1,80年和税后2,27年的还款时间(POT)。收支平衡点(BEP)的容量为41.48%,关机点(SDP)的容量为27.30%。贴现现金流量(DCF)为31.75%。基于对聚苯乙烯装置可行性的分析是很有趣的,值得建立。

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