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XiaolinQu, M.S., Lal K. Almas: The water requirement and profitability analysis of corn using irrigation
management approaches including evapotranspiration and weather data
In order to show the impact of a change in the price of fuel to the cost, a range
of fuel price from $2/mcf to $7/mcf is applied in the calculation of cost. In the
calculation of FULC, natural gas is used since it is the predominate source of
energy for pumping irrigation water in the Texas Panhandle area. The fuel cost
(FULC) is equal to the product of the amount of fuel used (NG) multiplied by the
price of the fuel (PNG)(Equation 2) (Colette et al. 2004).
FULC = NG*P NG (2)
Where NG is the amount of natural gas used in million cubic feet (mcf), P NG is
the price of natural gas ($). The amount of natural gas needed (NG) to pump one
acre-inch of water differs among irrigation systems (Equation 3) (Almas, 2000).
2
NG= 0.0038*L+ 0.0088*PSI – 0.000007623* PSI*L – 0.0000033*L (3)
Where L is the system lift in feet and PSI is the system pressure per square inch
The NG, LMR, LC and AIC are known constants for a given irrigation system
(Almas et al, 2000). For example, the total cost function for a typical Low
Elevation Spray Application (LESA) system with a 350 foot system lift can be
expressed as Equation 4. And Equation 4 is the cost function being used in this
study to analyze the optimum problem across the three water approaches.
TC= FC+ (1.018*P NG +4.04 + 0.56+1.06)*W= FC+ (1.018*P NG + 5.66)*W (4)
Where W represents the water approaches including total available water,
irrigation application and PPET. Marginal Factor Cost (MFC) represents the
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