Chemical hydrostatic backpressure reduction methodology to flow fluids through disposal wells
To control hydrostatic backpressure of disposal wells connected to a disposal plant surface network, density of water to be injected from a water disposal plant system into disposal wells formed in a subterranean zone, a density of a hydrostatic backpressure-modifying additive to modify a density of the water, a target total injection flow rate of the water, and a vertical depth of a portion of the subterranean zone through which the water is to be injected are identified. Injected water flow rate upstream of an injection point into the multiple disposal wells, wellhead injection pressure needed to achieve the target total injection flow rate and a total injection rate are periodically received. Based on these parameters, dosage rate of the additive to maintain the target total injection flow rate is periodically determined. An additive quantity is injected into the water and periodically modified based on the periodically determined dosage rate.
1. A method comprising:
identifying, by a computer system, injection water density of water (ρ w ) to be injected from a water disposal plant system at a surface into a plurality of disposal wells included in the water disposal plant system and formed in a subterranean zone;
identifying, by the computer system, a density (ρ 0 ) of a hydrostatic backpressure-modifying additive, the additive configured to modify a density of the water to be injected;
identifying, by the computer system, a target total injection flow rate of the water to be injected;
identifying, by the computer system, a vertical depth (D v ) of a portion of the subterranean zone through which the water is to be injected;
while the water is being injected into the plurality of disposal wells:
periodically receiving, by the computer system, injected water flow rate (q w ) upstream of an injection point into the plurality of disposal wells, wellhead injection pressure (ΔP ad ) needed to achieve the target total injection flow rate and a total injection rate (q t ),
periodically determining, by the computer system, a dosage rate (q 0 ) of the additive to maintain the target total injection flow rate using the total injection rate (q t ), the wellhead injection pressure (ΔP ad ), the vertical depth (D v ), the injection water density (ρ w ) and the density (ρ 0 ) of the additive, and
periodically modifying a quantity of the additive injected into the water based on the periodically determined dosage rate.
2. The method of claim 1 , wherein the dosage rate (q 0 ) of the additive is determined using the following formula:
q
o
=
q
t
[
144
Δ
P
ad
D
v
+
ρ
w
-
ρ
w
q
w
q
t
]
ρ
o
.
3. The method of claim 2 , further comprising developing the formula by computationally modeling, using the computer system, fluid flow through the plurality of disposal wells.
4. The method of claim 3 , wherein computationally modeling the fluid flow through the plurality of disposal wells comprises generating, by the computer system and for each disposal well, a respective inflow performance curve.
5. The method of claim 1 , wherein the additive is ethylenediaminetetraacetic acid (EDTA) 30% weight solution.
6. The method of claim 1 , wherein the additive is potassium dihydrogen phosphate (KH 2 PO 4 ) 80% weight solution.
7. The method of claim 1 , wherein modifying a quantity of the additive injected into the water comprises opening or closing a valve of a flow control system to flow or stop a flow of the additive into the water.