Tangki Soda Kaustik NaOH F-503 Tangki Hidrazin F-517 Pompa Utilitas 1 L-501

diinjeksikan ke Deaerator Bentuk : Silinder tegak vertikal dengan head berbentuk torisperical . Kapasitas : 52.0742 m 3 jam Dimensi : Diameter shell D = 3.9624 m : Tinggi shell Hs = 3.9624 m : Tebal shell t s = 0.5000 in : Tebal head t h = 0.5000 in : Tinggi atap = 0.3304 m Tekanan Desain : 22.3972 psi Bahan Konstruksi : Carbon Steel SA-283 Grade C AISI tipe 316 Jumlah : 1 Buah

27. Pompa Utilitas 1 L-501

Alat : Pompa utilitas 1 Kode : L-501 Fungsi : Mengalirkan air dari sungai menuju bak sedimentasi. Jenis : Centrifugal Pump,single suction, single stage. Bahan Konstruksi : Stainless Steel austenitic AISI tipe 316 Kapasitas : 61.2864 galmenit Efisiensi Pompa : 65 Dimensi : NPS = 2 in : Sch. = 40 Power Motor : 0.7837 hp NPSH : 6.4120 m Jumlah : 1 Buah

28. Pompa Utilitas 2 L-502

Alat : Pompa Utilitas 2 Kode : L-502 Fungsi : Mengalirkan air dari bak sedimentasi menuju ke bak penggumpal. Jenis : Centrifugal Pump,single suction, single stage. Bahan Konstruksi : Stainless Steel austenitic AISI tipe 316 Kapasitas : 61.2864 galmenit Efisiensi Pompa : 65 Dimensi : NPS = 2 in : Sch. = 40 Power Motor : 0.7837 hp NPSH : 6.4120 m Jumlah : 1 Buah

29. Pompa Utilitas 3 L-503

Alat Pompa Utilitas 3 Kode L-503 Fungsi Mengalirkan alum dari tangki alum menuju ke bak penggumpal. Jenis Centrifugal Pump,single suction, single stage. Bahan Konstruksi Stainless Steel austenitic AISI tipe 316 Kapasitas : 0.0508 galmenit Efisiensi Pompa : 35 Dimensi : NPS = 18 in : Sch. = 40 Power Motor : 0.0010 hp NPSH : 0.0566 m Jumlah : 1 Buah

30. Pompa Utilitas 4 L-504

Alat : Pompa Utilitas 4 Kode : L-504 Fungsi : Mengalirkan soda kaustik dari tangki soda kaustik menuju ke anion exchanger dan bak penggumpal. Jenis : Centrifugal Pump,single suction, single stage. Bahan Konstruksi : Stainless Steel austenitic AISI tipe 316 Kapasitas : 0.2704 galmenit Efisiensi Pompa : 35 Dimensi : NPS = 18 in : Sch. = 40 Power Motor : 0.0049 hp NPSH : 0.1725 m Jumlah : 1 Buah

Dokumen yang terkait

PRELIMINARY DESIGN OF PROPYLENE GLYCOL PLANT FROM PROPYLENE OXIDE AND WATER USING ACID CATALYST Preliminary Design of Propylene Glycol Plant from Propylene Oxide and Water Using Acid Catalyst Capacity of 60,000 Tons/Year.

0 4 18

PRELIMINARY DESIGN OF PROPYLENE GLYCOL PLANT FROM PROPYLENE OXIDE AND WATER USING ACID CATALYST Preliminary Design of Propylene Glycol Plant from Propylene Oxide and Water Using Acid Catalyst Capacity of 60,000 Tons/Year.

0 2 14

CHAPTER I Preliminary Design of Propylene Glycol Plant from Propylene Oxide and Water Using Acid Catalyst Capacity of 60,000 Tons/Year.

0 2 9

PRELIMINARY DESIGN OF PROPYLENE GLYCOL PLANT FROM PROPYLENE OXIDE AND WATER USING ACID CATALYST Preliminary Design of Propylene Glycol Plant from Propylene Oxide and Water Using Acid Catalyst with Capacity of 50,000 Ton/Year.

0 4 15

PRELIMINARY DESIGN OF PROPYLENE GLYCOL PLANT FROM PROPYLENE OXIDE AND WATER USING ACID Preliminary Design of Propylene Glycol Plant from Propylene Oxide and Water Using Acid Catalyst with Capacity of 50,000 Ton/Year.

0 2 14

FINAL PROJECT PRELIMINARY DESIGN OF TERTIARY BUTYL ALCOHOL Preliminary Design of Tertiary Butyl Alcohol Plant from Isobutylene and Water, Capacity of 80,000 Tons/Year.

0 2 19

TITLE PAGEFINAL PROJECT Preliminary Design of Tertiary Butyl Alcohol Plant from Isobutylene and Water, Capacity of 80,000 Tons/Year.

0 2 16

INTRODUCTION Preliminary Design of Tertiary Butyl Alcohol Plant from Isobutylene and Water, Capacity of 80,000 Tons/Year.

0 2 9

INTRODUCTION Preliminary Design Of Chemical Plant The Production Of Linear Alkylbenzene From 1-Dodecene And Benzene With Capacity 20,000 Tons Per Year.

0 9 8

PRELIMINARY DESIGN OF CHEMICAL PLANT THE PRODUCTION OF LINEAR ALKYL BENZENE FROM 1-DODECENE AND Preliminary Design Of Chemical Plant The Production Of Linear Alkylbenzene From 1-Dodecene And Benzene With Capacity 20,000 Tons Per Year.

2 15 9