Abstract
Proper design of surface facilities in a gas injection project is of great importance from both engineering and economic points of views. A process engineer frequently deals with standards, protocols and codes in designing facilities available in the literature. In this chapter, engineering facets and basic designs of gas injection surface facilities including pipeline, compressor, intercooler and separator were introduced and discussed. A step by step procedure for initial design of different facilities were shown, and the fundamental concepts and equations for design of each facility were presented, supporting with case studies in each section so as to ensure the design effectiveness. All of the case studies were extracted from the field data, and thus, predicting these data with reliable agreement proves the proper design of facilities.
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Notes
- 1.
The data for this case study are extracted from field data of a gas pipeline in Iran.
- 2.
The data for this case study are taken from a gas compressor station in Iran.
- 3.
The design data for this case study are taken from a gas compressor station in Iran.
- 4.
The design data for this case study are taken from a petrochemical plant in Iran.
Abbreviations
- Q:
-
Gas flow-rate, standard ft3/day [SCFD] or m3/day
- f:
-
Dimensionless friction factor
- P:
-
Pressure, Psia or KPa
- G:
-
Gas gravity (air = 1.0)
- T:
-
Temperature, R or K
- L:
-
Pipe segment length, miles or Km
- Z:
-
Gas compressibility factor at average gas temperature, dimensionless
- D:
-
Pipe inside diameter, in or mm
- E:
-
Pipeline efficiency
- H:
-
Elevation, ft or m
- µ:
-
Gas viscosity, lb/ft.s and poise
- ε:
-
Absolute pipe roughness, in
- γ:
-
Adiabatic or isentropic exponent, ratio of specific heats of gas, Cp/Cv
- Re:
-
Reynolds number
- Cp:
-
Specific heats of gas at constant pressure
- Cv:
-
Specific heats of gas at constant volume
- Wa:
-
Adiabatic work, ft.lb/lf of gas or J/Kg of gas
- HP:
-
Compressor horsepower
- M:
-
Gas mass flow-rate, lb/min
- ΔH:
-
Compressor head, ft.lb/lb
- η:
-
Compressor efficiency, %
- Z:
-
Compressibility of gas at suction condition, dimensionless
- ηa:
-
Compressor adiabatic (isentropic) efficiency
- \({\dot{m}}_{g}\) :
-
Gas mass flow-rate, lbm/hr or Kg/hr
- \({\dot{m}}_{a}\) :
-
Air mass flow-rate per fan, lbm/hr or Kg/hr
- NFan:
-
Number of fans
- t:
-
Ambient air temperature, °F or K
- N:
-
Fan speed under simulation conditions, RPM
- Nd:
-
Fan speed under cooler design conditions, RPM
- q:
-
Heat transfer rate, BTU/hr or W
- U:
-
Overall heat transfer coefficient, BTU/hr.ft2.°F or W/m2.K
- A:
-
Heat transfer area, ft2 or m2
- LMTD :
-
Log mean temperature difference, °F or K
- F:
-
Temperature correction factor
- h:
-
Inside (gas-side) heat transfer coefficient based on tube outside surface area
- \({r}_{f}\) :
-
Combined fouling resistance, hr.ft2.°F /BTU or m2/K.W
- \({r}_{m}\) :
-
Metal resistance, hr.ft2.°F /BTU or m2/K.W
- \({N}_{Bay}\) :
-
Number of bays under simulation conditions
- \({F}_{t}\) :
-
Temperature correction factor
- \({u}_{t}\) :
-
Settling velocity, m/s
- \({\rho }_{v}\) :
-
Vapor phase density, Kg/m3
- \({\rho }_{L}\) :
-
Liquid phase density, Kg/m3
- \({D}_{V}\) :
-
Minimum vessel diameter, m
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Azin, R., Banafi, A. (2022). Design of Subsurface and Surface Facilities for Gas Injection. In: Azin, R., Izadpanahi, A. (eds) Fundamentals and Practical Aspects of Gas Injection. Petroleum Engineering. Springer, Cham. https://doi.org/10.1007/978-3-030-77200-0_7
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