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ABSTRACT

The main energy sources in Indonesia generally still rely on fossil fuels, such as petroleum, coal and natural gas. Biofuel is a solution that can be applied as a substitute for fossil fuels. This research was conducted by simulating the biofuel production process and calculating the amount of carbon dioxide emissions produced. This simulation is done by modeling the hydroprocessing process using Unisim R390.1 by optimizing the operating conditions for each raw material. The Hydrotreatment process was varied at a pressure of 1-5 MPa and a temperature of 250oC - 350oC. shows that palm oil is the most effective in producing bioavtur at a temperature of 300oC and a pressure of 3 MPa, while nyamplung oil is the most effective for producing renewable diesel at a temperature of 300oC and a pressure of 3 MPa. The calculation of the number of emissions from the carbon dioxide life cycle shows that to produce 1 kg of biofuel, 3.82 x 103 kg of CO2 is produced"

"Pemenuhan kebutuhan bahan bakar dilakukan dengan aktivitas impor bahan bakar yang menyebabkan defisit pada current account. Indonesia juga berkomitmen untuk ikut serta dalam pembatasan kenaikan suhu rata-rata global di Conference of Parties (COP) 21 dengan menurunkan emisi karbon sebesar 29% dengan usaha sendiri. Produksi Renewable diesel menggunakan teknologi hydrotreatment dengan bahan baku 100% bio-oil dan co-processing dengan bahan baku 50% bio-oil. Kapasitas produksi pada simulasi ini yaitu teknologi hydrotreatment sebesar 1,9 juta ton pertahun dan co-processing 633.600 ton pertahun dengan by-products LPG 297.840 ton pertahun, naphta 316.800 ton pertahun, dan bensin 617.700 ton pertahun. Biaya investasi atau CAPEX hydrotreatment dan co-processing masing-masing 1.198.000.000 USD dan 2.159.290.000 USD. Biaya operasional atau OPEX hydrotreatment dan co-processing masing-masing 1.612.800.000 USD dan 1.097.000.000 USD. NPV selama 25 tahun sebesar USD 18.779.951.443 dan USD 19.268.377.636. Internal rate of return hydrotreatment dan co-processing masing-masing 42% dan 32%. Biaya pokok produksi hydrotreatment dan co-processing masing-masing 68 USD/MJ dan 54 USD/MJ. Teknologi hydrotreatment dengan bahan baku 100% bio-oil lebih sensitif terhadap parameter bahan baku dan harga produk, sedangkan teknologi co-processing lebih sensitive terhadap parameter biaya operasional. Pelaksanaan produksi renewable diesel perlu memperhatikan sensitivitas parameter-parameter tersebut.

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Fulfillment of fuel needs is carried out with fuel import activities that cause a current account deficit. Indonesia is also committed to participating in limiting global average temperature increases at Conference of Parties (COP) 21 by reducing carbon emissions by 29% on its own. Renewable diesel production using hydrotreatment technology with 100% bio-oil raw material and co-processing with 50% bio-oil raw material. The production capacity of hydrotreatment is 1.9 million tons per year and co-processing 633.600 tons per year with by-products LPG 297.840 tons per year, naphta 316.800 tons per year, and gasoline 617.700 tons per year. Investment costs or CAPEX hydrotreatment and co-processing are 1.198.000.000 USD and 2.159.290.000 USD, respectively. Operational costs or OPEX of hydrotreatment and co-processing are 1.612.800.000 USD and 1.097.000.000 USD, respectively. NPV for 25 years amounted to USD 18.779.951.443 and USD 19.268.377.636. Internal rate of return hydrotreatment and co-processing are 42% and 32%, respectively. The levelized cost of energy of hydrotreatment and co-processing are 68 USD/MJ and 54 USD/MJ, respectively. Hydrotreatment technology with 100% bio-oil raw material is more sensitive to raw material parameters and product prices, while co-processing technology is more sensitive to operational cost parameters. The implementation of renewable diesel production needs to consider the sensitivity of these parameters.

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