The paper reports a best-practices case study regarding the Casing-while-Drilling (CwD) installation of large outer-diameter (OD) tubulars—30-inch casing, specifically—in a troublesome zone in Campeche Bay, Mexico. The 30-in. CwD job was an industry first for this pipe size. The installation was an ambitious attempt to drill a 30-in. conductor in an area historically fraught with extreme wellbore instability and to produce better results than conventional drilling could deliver. Another objective was to push the 30-in. conductor to a depth that had been unattainable in previous instances of comparable lithology. Hammering was too disruptive for such a precarious formation, and conventional drilling, with its manual equipment and serial tripping, was too time-consuming, making well collapse probable. CwD, therefore, was the best option. The CwD process entailed a 30-in. Casing Running Tool (CRT) with hydraulic pick-up arms and a remotely operated Single Joint Elevator (SJE) handling the casing, the first joint bearing a 34-in. drillbit. In one run, the 30 × 34-in. conductor section was drilled, cased, and cemented at a total depth of 256m—78m reaching/jetting into seabed, 178m drilling. The job only took 9.52h, with an average Rate of Penetration (ROP) of 18.04m/h, and drill-time was reduced by 1.31d (26.3%) when compared to conventional drilling. And there were no stuck pipe issues, problems while tripping in the hole, or safety incidents. Successful completion of the well hinged on the CRT's multi-functionality and capacity for running large-OD tubulars. Filling, or pumping, the string while lowering served as a lubricator, evacuating cuttings more effectively and resolving the hole-cleaning inefficiencies experienced in adjacent wells. The improved running efficiencies were also realized due to the hydraulic arms enabling better control of pipe movement; more specifically, the operational benefits of superior handling of large-OD pipe were three-fold. First, rotation of the string enhanced the plaster/smear effect, strengthening the wellbore, averting lost circulation, and minimizing formation damage. Second, the large casing-to-wellbore diameter ratio created a gauged well, the smoother, more circular profile contributing to better well stability and requiring less cement. Third, a small, mono-bore annulus (between wellbore and casing) and consequent higher annular velocity facilitated cutting transport, prevented wellbore erosion, and resulted in hydraulic optimization while running 256m of conductor.
Studies have been undertaken to mathematically model the cryogenic wind-tunnel process, validate the model by the use of experimental data from the 0.3 m transonic cryogenic tunnel, and construct an interactive simulator of the cryogenic tunnel using the validated model. Additionally, this model has been used for designing closed-loop feedback control laws for regulation of temperature and pressure in the 0.3 m transonic cryogenic tunnel. The global mathematical model of the cryogenic tunnel that has been developed consists of coupled nonlinear differential governing equations based on an energy state concept of the physical cryogenic phenomena. Process equations and comparisons between actual and computer simulation predictions of tunnel response are given. Also included are the control laws and simulator and tunnel responses obtained using the feedback schemes for closed-loop control of temperature and pressure. These data show that the microprocessor-based proportional-integral control laws for pressure and temperature regulation have yielded very good closed-loop results. Nomenclature A -area, m 2 or percent of valve opening b = pressure loss coefficient c m = specific heat of metal, J/kg-K c p = specific heat of gas at constant pressure, J/kg-K c v = specific heat of gas at constant volume, J/kg-K D = dimensionality constant E = internal energy, J GN 2 = gaseous nitrogen K = gain LN 2 = liquid nitrogen rh = mass flow rate, kg/s M = Mach number TV = fan speed, rpm p = total pressure, atm Q = heat flow, J/s r = pressure ratio s = Laplacian mathematical operator t -time and time constant, s T = total temperature, K V = volume, m 3 W = mass, kg a. = cooling capacity of gaseous nitrogen, J/kg 0 = cooling capacity of liquid nitrogen, J/kg 0 = thermal mass, J/K T = transport time lag, s 77 = fan efficiency 7 = ratio of specific heats Subscripts a c F G L m = acoustic = tunnel circuit = fan = gas = liquid = metal
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