Design Problem, a horizontal separator for the following operating conditions. Gas rate: 15 MMSCFD Gas specific gravity: 0.6 Oil rate: 4,000 bbl/day Oil gravity: 40 API Operating pressure: 1000 psi Operating temperature: 60F Retention time: 3min Droplet size removal: 120 µm d Liquid Leff 20 24 30 36 42 46 Gas Leff Liss Hg=0.013 CP Pg=3.708 lb/ft³ Po=53.03 lb/ft³ Z=0.84 SR

Design Problem, a horizontal separator for the following operating conditions. Gas rate: 15 MMSCFD Gas specific gravity: 0.6 Oil rate: 4,000 bbl/day Oil gravity: 40 API Operating pressure: 1000 psi Operating temperature: 60F Retention time: 3min Droplet size removal: 120 µm d Liquid Leff 20 24 30 36 42 46 Gas Leff Liss Hg=0.013 CP Pg=3.708 lb/ft³ Po=53.03 lb/ft³ Z=0.84 SR

Structural Analysis

6th Edition

ISBN:9781337630931

Author:KASSIMALI, Aslam.

Publisher:KASSIMALI, Aslam.

Chapter2: Loads On Structures

Section: Chapter Questions

Problem 1P

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Using method of separation
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Please upload your full solution to the following problem. Determine the dosage and daily consumption of powdered activated carbon (PAC) required for trichloroethylene (TCE) removal given the following design specifications: 6 SUL Influent concentration = 1 mg/L TCE Carbon type: Calgon Filtrasorb 400 (12 x 40 mesh); pb = 450 g/L Freundlich parameters for TCE • Freundlich capacity parameter K = 55.9 (mg/g)(L/mg)¹/n • Freundlich intensity parameter 1/n = 0.48 Treatment objective = 0.005 mg/L TCE Flow rate = 378.5 L/min (100 gal/min) Assume that no other solutes compete with TCE for adsorption onto the PAC, and that the PAC is saturated at the treatment objective.