Persen Removal TINJAUAN PUSTAKA

II.3. Persen Removal

Unit Pengolahan Removal Sumber I. Pre Teatment - Screening 20 – 35 SS Syed R.Qasim, WWTP Planning, Design, and Operation, hal 156

II. Primary Treatment

- Grit Chamber ≤ 100 Pasir ReynoldRichard, Unit Operations Processes in Env.Engineering, 2nd edition, hal 152 - Bak Equalisasi 10 – 20 BOD 23 – 47 SS ReynoldRichard, Unit Operations Processes in Env.Engineering, 2nd edition, hal 158 - Flotasi 1. Disolved Air Flotation 70 – 85 Oil 50 – 85 SS 20 – 70 BOD 10 – 60 COD Cavaseno, Industrial Wastewater and Solid Waste Engineering, hal.14 Hak Cipta © milik UPN Veteran Jatim : Dilarang mengutip sebagian atau seluruh karya tulis ini tanpa mencantumkan dan menyebutkan sumber. Unit Pengolahan Removal Sumber 2. Floculation - Flotation 97 Oil 75 Solid 80 BOD 80 COD Cavaseno, Industrial Wastewater and Solid Waste Engineering, hal.14 - Bak pengendap I 50 – 70 SS 25 – 40 BOD Metcalf Eddy, WWET Disposal, and Reuse 4th edition, hal 396 - Netralisasi pH 6,5 – 9 ReynoldRichard, Unit Operations Processes in Env.Engineering, 2nd edition, hal 161 - Koagulasi - Flokulasi 58 BOD 63 COD 33 TSS 93 Cr Eckenfelder, Jr., Industrial Water Pollution Control, 3th edition, hal 156 Hak Cipta © milik UPN Veteran Jatim : Dilarang mengutip sebagian atau seluruh karya tulis ini tanpa mencantumkan dan menyebutkan sumber. Unit Pengolahan Removal Sumber III. Secondary Treatment III.1. Aerob a. Activated Sludge 80 – 99 BOD 50 – 95 COD 60 – 85 SS 80 – 99 Oil 95 – 99 Phenol 33 – 99 NH 3 97 – 100 H 2 S Cavaseno, Industrial Wastewater and Solid Waste Engineering, hal.15 1. Konvensional 85 – 95 BOD ReynoldRichard, Unit Operations Processes in Env.Engineering, 2nd edition, hal 429 2. Non Konvensional - Step Aeration 85 – 95 BOD ReynoldRichard, Unit Operations Processes in Env.Engineering, 2nd edition, hal 429 - Tapered Aeration 85 – 95 BOD - Contact Stabilization 80 – 90 BOD - Pure Oxygen 85 – 95 BOD - High Rate Aeration 75 – 90 BOD - Extended Aeration 75 – 95 BOD Hak Cipta © milik UPN Veteran Jatim : Dilarang mengutip sebagian atau seluruh karya tulis ini tanpa mencantumkan dan menyebutkan sumber. Unit Pengolahan Removal Sumber - Oxydation Ditch 75 – 95 BOD ReynoldRichard, Unit Operations Processes in Env.Engineering, 2nd edition, hal 445 b. Aerated Lagoon 75 – 95 BOD 60 – 85 COD 40 – 65 SS 70 – 90 Oil 90 – 99 Phenol 95 – 100 H 2 S Cavaseno, Industrial Wastewater and Solid Waste Engineering, hal.16 III.2. An Aerob a. UASB 90 – 95 COD Metcalf Eddy, WWET Disposal, and Reuse 4th edition, hal 1007 b. An Aerobic Lagoon 80 – 90 COD Metcalf Eddy, WWET Disposal, and Reuse 4th edition, hal 1026 c. Fluidized Bed Reactor 90 COD Metcalf Eddy, WWET Disposal, and Reuse 4th edition, hal 1022 Hak Cipta © milik UPN Veteran Jatim : Dilarang mengutip sebagian atau seluruh karya tulis ini tanpa mencantumkan dan menyebutkan sumber. Unit Pengolahan Removal Sumber d. Fixed Bed Reactor ≤ 90 COD Metcalf Eddy, WWET Disposal, and Reuse 4th edition, hal 1019 III.3. Bio Film a. Trickling Filter 1. Low Rate TF 2. Intermediate Rate TF 3. High Rate TF 4. Super Rate TF 90 – 95 BOD 85 – 90 BOD 85 – 90 BOD 60 – 80 BOD ReynoldRichard, Unit Operations Processes in Env.Engineering, 2nd edition, hal 527 b. RBC s.d. 90 BOD Metcalf Eddy, WWET Disposal, and Reuse 4th edition, hal 937

II.4. Profil Hidrolis