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The Kvitebjørn medium rich gas condensate field in the Norwegian North Sea is characterized as a high pressure high temperature (HPHT) reservoir with 770.5 bar pressure and 150°C temperature at about 4000 m TVD MSL. Despite high temperature and depth, the average reservoir properties are reasonably good. The main reservoir is Brent Group of Middle Jurassic age which is extensively faulted. One of the main challenges is the drilling in depleted reservoir. The strategy to mitigate the problem has been to put the field on reduced production and/or to actively manage reservoir pressure by producing more from areas far away from the drilling locations. Advanced drilling technologies have also been developed to improve drillability. Several improved oil/gas recovery methods are currently under consideration, which include infill drilling, process capacity upgrading, low pressure-production and gas recycling. Infill drilling is challenging due to reservoir depletion. Capacity upgrading is to be implemented to expedite hydrocarbon recovery. Gas recycling has some potential for improved condensate recovery, but the project economy is poor. Low pressure production appears to be a very attractive option. A compressor concept has been selected based on thorough evaluation of space and weight limitations on the platform, possibility for future drilling and intervention operations, explosion hazard, tie-in of other prospects and future export facilities etc. Subsurface challenges include uncertainties related to well integrity and productivity, reservoir communication, reservoir volumes, etc. The purpose of this paper is to present the challenges related to development and management of this HPHT gas condensate reservoir, the strategies to overcome the challenges and the methods to improve gas and condensate recoveries from this field with special focus on the low pressure production and gas recycling. Introduction The HPHT Kvitebjørn Field is located in block 34/11 in the southeastern part of the Tampen Spur area of the Norwegian North Sea (Fig. 1). The field is currently owned 58.55% by StatoilHydro, 30% by Petoro, 6.45% by Enterprise Oil and 5% by Total. StatoilHydro is the operator. Block 34/11 was awarded in the 14th concession round in 1993. The field was discovered in 1994 by the exploration well 34/11–1 (Fig. 2), which encountered a gas condensate column of 175 m in the Brent Group. A gas-water-contact (GWC) at 4139 m TVD MSL was observed in this well. Another appraisal well (34/11–3T2) was drilled in 1996–97, which confirmed a gas condensate column of 160 m in the same formation. A plan for development and operation (PDO) of the field was approved by the authority in 2000. The main drilling program started in October 2003 and the production commenced on 26th of September 2004. The development plan consisted of a platform having a 20.7 MSm3/d production/processing capacity with three stage separation, one drilling rig and living quarters. The water depth at the Kvitebjørn platform is 190 m TVD MSL. The drainage strategy was chosen to be pressure depletion by 11 production wells.
The Kvitebjørn medium rich gas condensate field in the Norwegian North Sea is characterized as a high pressure high temperature (HPHT) reservoir with 770.5 bar pressure and 150°C temperature at about 4000 m TVD MSL. Despite high temperature and depth, the average reservoir properties are reasonably good. The main reservoir is Brent Group of Middle Jurassic age which is extensively faulted. One of the main challenges is the drilling in depleted reservoir. The strategy to mitigate the problem has been to put the field on reduced production and/or to actively manage reservoir pressure by producing more from areas far away from the drilling locations. Advanced drilling technologies have also been developed to improve drillability. Several improved oil/gas recovery methods are currently under consideration, which include infill drilling, process capacity upgrading, low pressure-production and gas recycling. Infill drilling is challenging due to reservoir depletion. Capacity upgrading is to be implemented to expedite hydrocarbon recovery. Gas recycling has some potential for improved condensate recovery, but the project economy is poor. Low pressure production appears to be a very attractive option. A compressor concept has been selected based on thorough evaluation of space and weight limitations on the platform, possibility for future drilling and intervention operations, explosion hazard, tie-in of other prospects and future export facilities etc. Subsurface challenges include uncertainties related to well integrity and productivity, reservoir communication, reservoir volumes, etc. The purpose of this paper is to present the challenges related to development and management of this HPHT gas condensate reservoir, the strategies to overcome the challenges and the methods to improve gas and condensate recoveries from this field with special focus on the low pressure production and gas recycling. Introduction The HPHT Kvitebjørn Field is located in block 34/11 in the southeastern part of the Tampen Spur area of the Norwegian North Sea (Fig. 1). The field is currently owned 58.55% by StatoilHydro, 30% by Petoro, 6.45% by Enterprise Oil and 5% by Total. StatoilHydro is the operator. Block 34/11 was awarded in the 14th concession round in 1993. The field was discovered in 1994 by the exploration well 34/11–1 (Fig. 2), which encountered a gas condensate column of 175 m in the Brent Group. A gas-water-contact (GWC) at 4139 m TVD MSL was observed in this well. Another appraisal well (34/11–3T2) was drilled in 1996–97, which confirmed a gas condensate column of 160 m in the same formation. A plan for development and operation (PDO) of the field was approved by the authority in 2000. The main drilling program started in October 2003 and the production commenced on 26th of September 2004. The development plan consisted of a platform having a 20.7 MSm3/d production/processing capacity with three stage separation, one drilling rig and living quarters. The water depth at the Kvitebjørn platform is 190 m TVD MSL. The drainage strategy was chosen to be pressure depletion by 11 production wells.
Formation evaluation can become complex when the invading mud-filtrate properties are unusual, variable or unknown like in sodium potassium (Na/K) formate water base mud (WBM) environments. In these situations, computed reservoir properties are adversely affected and become strongly dependent on the formation invasion status. The Permian age reservoir discussed in this paper, consists of highly unconsolidated heterogeneous sandstone sequences, saturated with condensate rich gas. From a drilling engineering perspective, the shales are often unstable, requiring high mud overbalance to maintain hole stability in wells with high inclinations, which resulted in recurrent differential sticking incidents. The use of formate based drilling fluids in this field, gained acceptance over time, primarily to minimize drilling problems. The downside of formate muds, however, is that log data interpretation encounters serious challenges because of the uncertain petrophysical properties of the mud, affecting log measurements in two ways. The first are those effects related to the mud present inside the borehole and surrounding the tool, or so-called environmental effects. The second are those related to the invading mud-filtrate present inside the formation, resulting in pessimistic porosity, mineralogy and permeability estimates. This paper shows how Na/K formate WBM filtrate effects can be identified and eliminated using Logging-While-Drilling (LWD) time-lapse data acquisition and analysis to provide time-independent logs in a manner that renders the logs immune to various mud-filtrate effects. These logs, together with a corresponding new petrophysical model, make it possible to do away with the mud-filtrate petrophysical properties, and to solve for porosity, mineralogy and fluid saturations from standalone nuclear measurements, irrespective of the formation invasion status. Moreover, the results demonstrate how valuable LWD time-lapse data acquisition can be, and that data acquired while drilling – especially resistivity data in this instance – are important to validate this novel formation evaluation interpretation approach.
Xanthan gum is a non-damaging viscosifier and fluid loss control agent commonly included in reservoir drill-in, completion and workover fluid formulations. One of the key benefits offered by xanthan in these applications is that it is not an especially robust polysaccharide and under downhole conditions it will eventually self-break through molecular collapse and/or depolymerisation reactions. With only a temporary presence in the filter cake and formation invaded by filtrate, xanthan can never pose a serious or permanent threat to oil and gas production but clearly it would be good to be able to control and manage the rate at which it degrades. The rate at which xanthan degrades downhole is a function of the temperature, the presence of oxidants and the ionic environment. The purpose of the experimental program described in this paper was to measure the rate of natural self-breaking of xanthan under different temperature conditions when dissolved in various water and brine systems containing formate and halide ions. A simulated North Sea formation water and a low-sulfate seawater were included in the test program. The samples were dynamically and statically aged for periods up to 12 months, and their degree of natural self-breaking was tracked by viscosity measurements. Several other classes of polysaccharide were tested in the program, either alone or in combination with xanthan. The tests confirmed that at temperatures in the range 124–170°C (255–338°F) xanthan and the other polysaccharides all degraded over time and the resulting "broken" fluids had low viscosities. It was found that the self-breaking rate varied hugely with brine type and concentration. Concentrated formate brines, rich in antioxidants and high molar concentrations of water-structure making ions, allowed steady rates of polymer breaking over weeks and months while the same polysaccharides dissolved in brines containing significant amounts of sodium bromide degraded very quickly. These results suggested that clear brine systems of any density within the compatibility limits of the blended components could be engineered to self-break within a set period of time by blending formate and sodium bromide brines in appropriate ratios. Degradation tests at 124°C (255°F) of xanthan in a typical North Sea formation water and a low-sulphate seawater, showed very rapid self-degradation, resulting in hardly any remaining viscosity after only 4 days of ageing. It seems likely that xanthan gum and other polysaccharides that are stabilized in formate brines, will lose their viscosity rapidly if contacted by formation water or well injection water. In fact, an overflush of the filter cake and near wellbore formation with any low salinity fluid would make an effective breaker system for xanthan in the applicable temperature range. The learning points from this study offer a solution to the problem of filtrate retention as an artifact in laboratory coreflood tests of viscosified brine-based fluids. Not exposing the fluid to the reservoir temperature for a realistic time period between invasion and drawdown may leave some viscosified brine in the pore space and in the filtercake, that is hard to remove during the standard drawdown time. Such retained filtrate has an adverse effect on the core's water saturation and thereby on the effective permeability to hydrocarbons.
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