PRA RENCANA PABRIK PEMBUATAN 1,3-BUTADIENA KAPASITAS 60.000 TON/TAHUN
Total View This Week0
Total View This Week0
Institusion
Universitas Sriwijaya
Author
NYIMAS ANNISA RIZKI LINDY (STUDENT ID : 03031181520004)
SITI AISYAH SHANAZ VITRIA RAMADHONA (STUDENT ID : 03031181520036)
Tuti Indah Sari (LECTURER ID : 0001027501)
SITI AISYAH SHANAZ VITRIA RAMADHONA (STUDENT ID : 03031181520036)
Tuti Indah Sari (LECTURER ID : 0001027501)
Subject
TP155-156 Chemical engineering
Datestamp
2019-08-19 07:08:19
Abstract :
This 1.3-Butadiene manufacturing plant with a capacity of 60,000 tons / year is planned to be established in 2024 in the Krakatau Steel Industrial Zone, Cilegon City, Banten Province with an area of ​​5.2 hectares. The process of making 1,3-Butadiene is a dehydration process of 2,3-Butanediol using a calcium phosphate hydroxyapatite catalyst in a multitube fixed bed reactor of 4 pieces. The reactor has operating conditions at the same temperature that is 365oC, while the sequential pressure is 2.2; 1.85; 1,5; and 1.21 bar, with the following reaction. C4H10O2 (g) ïƒ C4H8O (g) + H2O (g) 2,3-Butanadiol 3-Buten-2-Ol Water C4H8O (g) ïƒ C4H6 (g) + H2O (g) 3-Buten-2-Ol 1,3-Butadiene Water C4H10O2 (g) ïƒ C4H8O (g) + H2O (g) 2,3-Butanadiol Methyl Ethyl Ketone Water C4H10O2 (g) ïƒ C4H8O (g) + H2O (g) 2,3-Butanadiol 2-Methyl Propanal Water This plant is a type of Limited Liability Company (PT) with line and staff organization system and the number of employees is 152 people. Based on the results of an economic analysis, a 1,3-Butadiene manufacturing plant is worth setting up with the following details. a. Investment = US $ 115,973,048.01 b. Sales revenue per year = US $ 400,863,511.66 c. Cost of production per year = US $ 342,533,473.14 d. Net profit per year = US $ 52,181,932.38 e. Pay out time = 2.1 years f. Rate of return on investment = 37.72% g. Discounted cash flow = 55.82% h. Break even point = 34.17% i. Service life = 11 years
This 1.3-Butadiene manufacturing plant with a capacity of 60,000 tons / year is planned to be established in 2024 in the Krakatau Steel Industrial Zone, Cilegon City, Banten Province with an area of ​​5.2 hectares. The process of making 1,3-Butadiene is a dehydration process of 2,3-Butanediol using a calcium phosphate hydroxyapatite catalyst in a multitube fixed bed reactor of 4 pieces. The reactor has operating conditions at the same temperature that is 365oC, while the sequential pressure is 2.2; 1.85; 1,5; and 1.21 bar, with the following reaction. C4H10O2 (g) ïƒ C4H8O (g) + H2O (g) 2,3-Butanadiol 3-Buten-2-Ol Water C4H8O (g) ïƒ C4H6 (g) + H2O (g) 3-Buten-2-Ol 1,3-Butadiene Water C4H10O2 (g) ïƒ C4H8O (g) + H2O (g) 2,3-Butanadiol Methyl Ethyl Ketone Water C4H10O2 (g) ïƒ C4H8O (g) + H2O (g) 2,3-Butanadiol 2-Methyl Propanal Water This plant is a type of Limited Liability Company (PT) with line and staff organization system and the number of employees is 152 people. Based on the results of an economic analysis, a 1,3-Butadiene manufacturing plant is worth setting up with the following details. a. Investment = US $ 115,973,048.01 b. Sales revenue per year = US $ 400,863,511.66 c. Cost of production per year = US $ 342,533,473.14 d. Net profit per year = US $ 52,181,932.38 e. Pay out time = 2.1 years f. Rate of return on investment = 37.72% g. Discounted cash flow = 55.82% h. Break even point = 34.17% i. Service life = 11 years
File :
RAMA_24201_03031181520004_03031181520036.pdf
RAMA_24201_03031181520004_03031181520036_TURNITIN.pdf
RAMA_24201_03031181520004_03031181520036_0001027501_09.pdf
RAMA_24201_03031181520004_03031181520036_0001027501_10_ref.pdf
RAMA_24201_03031181520004_03031181520036_0001027501_11_lamp.pdf
RAMA_24201_03031181520004_03031181520036_0001027501_01_front_ref.pdf
RAMA_24201_03031181520004_03031181520036_0001027501_02.pdf
RAMA_24201_03031181520004_03031181520036_0001027501_03.pdf
RAMA_24201_03031181520004_03031181520036_0001027501_04.pdf
RAMA_24201_03031181520004_03031181520036_0001027501_05.pdf
RAMA_24201_03031181520004_03031181520036_0001027501_06.pdf
RAMA_24201_03031181520004_03031181520036_0001027501_07.pdf
RAMA_24201_03031181520004_03031181520036_0001027501_08.pdf
Download
book
BibTex
Latex, Jabref
cloud_download
Original Resource
url resource Institution
