MSCFD definition
Examples of MSCFD in a sentence
Pipeline Pressure ( PSIG ) Pipeline Capacity ( MSCFD ) @700 psig @ 25 psig For page 10 A-D see Chart 4.1 Metering Flow Diagram under separate PDF file from Autocad.
Total Contained Ethane in Stripper Off-Gas (FOEB/D) = Total Stripper Off-Gas from Naphtha Hydrotreater 1344 (MSCF/D) * Mole Fraction Ethane * 0.0800 (LB/SCF) * 22,169 (BTU/LB) / 1000 / 6.0 (MMBTU/FOEB) Total Unfinished Naphtha = The Total Unfinished Naphtha from AVU 146 as defined in Exhibit A-3.
Total Contained Methane in Stripper Off-Gas (FOEB/D) = Total Stripper Off-Gas from Naphtha Hydrotreater 1344 (MSCF/D) * Mole Fraction Methane * 0.0425 (LB/SCF) * 23,840 (BTU/LB) / 1000 / 6.0 (MMBTU/FOEB) Total Unfinished Naphtha = The Total Unfinished Naphtha from AVU 146 as defined in Exhibit A-3.
Total Contained H2S in Stripper Off-Gas (FOEB/D) = Total Stripper Off-Gas from Naphtha Hydrotreater 1344 (MSCF/D) * Mole Fraction H2S * 0.0907 (LB/SCF) * 7,105 (BTU/LB) / 1000 / 6.0 (MMBTU/FOEB) Total Unfinished Naphtha = The Total Unfinished Naphtha from AVU 146 as defined in Exhibit A-3.
Total Contained Pentane and Heavier In Stripper Off-Gas (B/D) = Total Stripper Off-Gas from HCU 942 (MSCF/D) * Mole Fraction Pentane and Heavier * 0.1980 (LB/SCF) / 221.0 (LB/BBL) * 1000 Heavy Gas Oil from AVU 146 to HCU 942 = Heavy Gas Oil from AVU 146 & Light Cycle Oil to HCU 942 - Light Cycle Oil to HCU 942 The above equations are based on the following deemed quantities.
Total Contained Hydrogen in Stripper Off-Gas (FOEB/D) = Total Stripper Off-Gas from Naphtha Hydrotreater 1344 (MSCF/D) * Mole Fraction Hydrogen * 0.0053 (LB/SCF) * 60,950 (BTU/LB) / 1000 / 6.0 (MMBTU/FOEB) EXHIBIT A-25 Total Unfinished Naphtha = The Total Unfinished Naphtha from AVU 146 as defined in Exhibit A-3.
Total Contained Pentane and Heavier In Stripper Off-Gas (B/D) = Total Stripper Off-Gas from Naphtha Hydrotreater 1344 (MSCF/D) * Mole Fraction Pentane and Heavier * 0.1980 (LB/SCF) / 221.0 (LB/BBL) * 1000 The above equations are based on the following deemed quantities.
H2 Supply Costs = (Metered MSCFD * H2 Price)* 365 day/yr + (** Kwh/MSCFD * Metered MSCFD * $/Kwh*24)*365 + LVT Comp Maintenance A stream of hydrogen is purged from the LVT and is amine treated and sent to the refinery’s PSA system to remove light ends, before being recycled to the hydrogen makeup system.
MMBO Million standard barrels of oil or condensate MSCFD Thousand standard cubic feet (of gas) per day MMSCFD Million standard cubic feet (of gas) per day TCF Trillion Cubic Feet BBO Billion standard barrels of oil or condensate BCF Billion Cubic Feet of gas at standard temperature and pressure conditions Bbls Barrels of oil or condensate BOPD Barrels of oil per day BS&W Base, sediment and water contaminants in oil BOE Barrels of Oil Equivalent.
Hydrogen compression costs are calculated per MSCFD using the GPSA Engineering Data Book, Section 4, assuming a **% efficiency.