Class I Operational Constraints Requiring Specialized Wellbore Hydraulic Modeling Tom Ortiz TCEQ A False Sense of Security? • Surface measurements are straightforward, but can we always use them to infer downhole well performance? • We will discuss two UIC rules for which specialized wellbore hydraulic modeling can shed light on gaps in the information provided by surface measurements – Positive annulus to tubing pressure differential – Tubing pressure measurement under vacuum Positive Pressure for Leak Prevention • “[A]nnulus pressure shall be at least 100 psi greater than…tubing pressure” (30 TAC §331.63(e)) • Pressure is measured at the surface, but gravity and friction affect pressure drop downhole 𝑓𝐷 ∆𝑃 = 𝜌𝑔𝐷 − 𝜌𝑉 2 2𝑑𝑖 • Positive annulus pressure is needed from surface to packer in order to prevent waste leakage Right is a schematic of an injection well that includes labels for the surface and bottomhole pressure differentials. The schematic also includes the surface, intermediate, and long-string casing, the injection packer, and the perforations Pannulus – Ptubing = 100 psi Here is an illustration of a typical wellbore. Surface pressure differential can be measured and controlled at the surface. However, below, down to the packer, gravity and friction interact, which can result in either a higher or lower pressure differential. Pannulus – Ptubing =? Base Case Here is an illustration of the same wellbore, with the base case inside casing diameter, packer depth, and inside tubing diameter all marked. 8.535 in ID Casing Tubing Packer Depth Injection Rate Annulus Specific Gravity Waste Specific Gravity 9⅝ in, 53.5 lb/ft, N-80 4 in, 9.5 lb/ft, N-80 6,000 ft. GL 200 gpm 1.0 1.1 Right is a schematic of an injection well that includes labels for the long string casing and tubing ID, as well as the depth of the packer • Casing • Tubing • Packer Depth • Injection Rate • Annulus Specific Gravity • Waste Specific Gravity 9⅝ in, 53.5 lb/ft, N-80 4 in, 9.5 lb/ft, N-80 6,000 ft. GL 6,000 ft GL 200 gpm 1.0 1.1 3.548 in ID Sensitivity Analysis – Injection Rate • • • Center is a graph with annulus pressure differential at 6000 ft (base case packer depth) on the y-axis in psi Injection rate is on the x-axis in gpm Frictional pressure drop increases with the square of velocity (injection rate). For example, decreasing injection rate from 200 to 150 gpm results in a 68 psi decrease in annulus pressure differential. Sensitivity Analysis – Specific Gravity • • • Center is a graph with annulus pressure differential at 6000 ft (base case packer depth) on the y-axis in psi Waste specific gravity is on the x-axis Hydrostatic pressure increases linearly with density. For example, increasing waste specific gravity from 1.1 to 1.2 results in a 244 psi decrease in annulus pressure differential Sensitivity Analysis – Packer Depth • • • Center is a graph with annulus pressure differential at packer depth on the yaxis in psi Packer depth is on the x-axis in ft Both frictional pressure drop and hydrostatic pressure vary linearly with depth. For example, setting the packer 1000 ft shallower results in a 16.5 psi increase in annulus pressure differential Sensitivity Analysis – Tubing Diameter • • • Center is a graph with annulus pressure differential at 6000 ft (base case packer depth) on the y-axis in psi Tubing inner diameter is on the x-axis in in The graph shows the limiting effects of tubing size on annulus pressure differential. Increasing tubing size beyond a threshold diameter will cause frictional pressure drop to become negligible. On the other hand, continuing to decrease tubing size will cause the injection tubing to act as a throttling device. If you had enough pumping power available, in extreme cases it could be possible to vaporize the waste stream, causing annulus pressure differential at the packer to approach the annulus fluid’s hydrostatic pressure. In this example, the annulus fluid has a hydrostatic pressure of 2600 psig at 6000 ft. Monitor Vacuum Well Pressure Downhole Right is a schematic of an injection well that includes labels for the surface and bottomhole tubing pressures. The schematic also includes the surface, intermediate, and long-string casing, the injection packer, and the perforations. The tubing fluid column does not reach surface. • “[I]njection pressure at the wellhead shall…assure that…injection does not initiate…or propagate fractures” (30 TAC §331.63(c)) Ptubing = 0 psig • Under vacuum, a wellhead gauge will not provide usable tubing pressure measurements: the fluid column does not reach the surface • Injection interval fracture risk is, in that case, unknown unless tubing pressure is measured downhole Here again is an illustration of our example well. It shows a standing column of waste fluid in the tubing that does not reach the surface. Therefore, a wellhead tubing pressure gauge will always read zero. Ptubing = ? Permanent Downhole Gauges Right is a schematic of an injection well that includes labels for the surface and bottomhole tubing pressures. The schematic also includes the surface, intermediate, and long-string casing, the injection packer, and the perforations. The tubing fluid column does not reach surface. An expanded view of a downhole pressure gauge run on tubing is also included at center. • A downhole gauge mounted near the well’s completion can address the vacuum problem • Flowing bottomhole pressure must remain below injection interval fracture stress Electrical Cable (to surface) Downhole Pressure Gauge Injection Tubing Here is another illustration of our example well. This time, an offset illustration of the lowermost section of the injection tubing is also included to show placement of a permanent downhole pressure gauge and the connected electrical cable, which extends along the tubing to surface. Limit Flowing Bottomhole Pressure sh This is an illustration of a section of the reservoir immediately adjacent to the wellbore. The wellbore pressure is shown acting against the reservoir, and the horizontal rock matrix stress and reservoir pore pressure are shown as opposing the force of the wellbore pressure Pr Pw Center is a diagram of the portion of the reservoir adjacent to the well’s completion. Labels for horizontal matrix stress, pore pressure, and flowing bottomhole pressure are shown. Fracture stress = horizontal stress + formation pressure 𝑃𝑤 < 𝜎ℎ + 𝑃𝑟 Wellbore (flowing bottomhole) pressure must remain less than the sum of the horizontal rock matrix stress and reservoir pore pressure acting at that point in order to prevent fracturing Estimate Fracture Stress Right is a diagram of a portion of the reservoir with labels for overburden stress, pore pressure, and vertical stress, which together act to establish mechanical equilibrium Left is a diagram of a cylindrical bar that shows its original, unstressed dimensions, as well as its deformed dimensions after being subjected to axial stress Vertical stress = overburden stress – reservoir pressure Reservoir rock is compressed by overburden Pore pressure helps support overburden stress NOTE – If one assumes that the ratio of vertical to horizontal stress = 3, Poisson’s ratio = 0.25 𝜀ℎ 𝜇=− 𝜀𝑣 Here is an illustration of a cylindrical bar that has been vertically. stressed Vertical and horizontal strains are labeled 𝑃𝑓 = 𝜎ℎ + 𝑃𝑟 eh 𝑃𝑓 = 𝜎𝑣 ev sv sob Pr 𝜇 + 𝑃𝑟 1−𝜇 𝑃𝑓 = 𝜎𝑜𝑏 − 𝑃𝑟 Here is an illustration of the overburden, showing the relationship among overburden stress, reservoir pressure, and the magnitude of vertical reservoir stress below the overburden. 𝜇 + 𝑃𝑟 1−𝜇 sv Final Thoughts • Compliance with TCEQ UIC rules sometimes requires gathering different data or constructing different models • Considering these constraints early can assist with optimizing performance over the life of the well – Front end design, or workover? (Now or later?) – Maximize flow rate? Minimize construction cost? – Which is most economical? (Initial vs. total lifecycle?) Thanks for Your Attention Thomas Manuel Ortiz, Ph.D., P.E. Project Manager Texas Commission on Environmental Quality Office of Waste Radioactive Materials Division Underground Injection Control Permits Section +1-512-239-6406 [email protected] Nomenclature Roman d diameter (in) D depth (ft) f Darcy friction factor (-) P pressure (psig) V velocity (ft/s) Greek e strain (in/in) m Poisson’s ratio (-) r density (lb/gal) s stress (psi) Subscripts f fracture h horizontal i inner ob overburden r reservoir v vertical w wellbore
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