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During the last few years, production of liquid hydrocarbons has been reported from the gas-condensate window of the Eagle Ford, Barnett, Niobrara and Marcellus shale plays in the US. This paper presents a new Material Balance Equation (MBE) for estimation of Original Gas in Place (OGIP) and Original Condensate in Place (OCIP) in shale gas condensate reservoirs. This material balance methodology allows estimating the critical time for implementing gas injection in those cases where condensate buildup represents a problem. Additionally, the proposed MBE considers the effects of free, adsorbed and dissolved gas condensate production, and also takes into-account the stress-dependency of porosity and permeability. An extension of the methodology is implemented for estimating the optimum time for hydraulically re-fracturing shale condensate reservoirs. The new MBE applies to shale gas condensate reservoirs by incorporating a two-phase gas deviation factor (Z2) and total cumulative gas production (Gpt) that includes both gas and condensate. If a crossplot of P/Z2 (pressure/Z2) vs. Gpt is prepared for a conventional gas condensate reservoir, a single straight line is obtained. However, when the single-phase gas compressibility factor (Z) is used, a deviation from the linear behavior is observed once the reservoir pressure falls below the gas dew-point. This methodology is applied in this study to unconventional shale gas condensate. Since there are three characteristic stages of production in a shale gas reservoir (production of free, adsorbed and dissolved gas), the location of the aforementioned deviation will provide a hint of the production stage that will be affected by condensate buildup. For example, if the deviation point is located in the region where production of free gas is predominant, then the production due to desorption mechanisms will be negatively impacted because condensation will have already occurred in the reservoir, resulting on reduction of effective permeability to gas. This methodology allows then estimating the critical time for implementing gas injection on the basis of the total cumulative gas production. Results are presented as crossplots of 1) P/Z2 vs. Gpt, 2) Gpt vs. time and 3) gas rate vs. time. It is concluded that estimation of the critical time for implementing gas injection is useful for improving the performance of those shale gas condensate reservoirs where condensate buildup represents a threat that can negatively impact the gas production rate. The novelty of this work resides on the fact that the combined effect of free, adsorbed and dissolved gas production mechanisms on stress-sensitive shale gas condensate reservoirs has not been considered previously in the literature for estimation of OGIP and OCIP using an analytical MBE.
During the last few years, production of liquid hydrocarbons has been reported from the gas-condensate window of the Eagle Ford, Barnett, Niobrara and Marcellus shale plays in the US. This paper presents a new Material Balance Equation (MBE) for estimation of Original Gas in Place (OGIP) and Original Condensate in Place (OCIP) in shale gas condensate reservoirs. This material balance methodology allows estimating the critical time for implementing gas injection in those cases where condensate buildup represents a problem. Additionally, the proposed MBE considers the effects of free, adsorbed and dissolved gas condensate production, and also takes into-account the stress-dependency of porosity and permeability. An extension of the methodology is implemented for estimating the optimum time for hydraulically re-fracturing shale condensate reservoirs. The new MBE applies to shale gas condensate reservoirs by incorporating a two-phase gas deviation factor (Z2) and total cumulative gas production (Gpt) that includes both gas and condensate. If a crossplot of P/Z2 (pressure/Z2) vs. Gpt is prepared for a conventional gas condensate reservoir, a single straight line is obtained. However, when the single-phase gas compressibility factor (Z) is used, a deviation from the linear behavior is observed once the reservoir pressure falls below the gas dew-point. This methodology is applied in this study to unconventional shale gas condensate. Since there are three characteristic stages of production in a shale gas reservoir (production of free, adsorbed and dissolved gas), the location of the aforementioned deviation will provide a hint of the production stage that will be affected by condensate buildup. For example, if the deviation point is located in the region where production of free gas is predominant, then the production due to desorption mechanisms will be negatively impacted because condensation will have already occurred in the reservoir, resulting on reduction of effective permeability to gas. This methodology allows then estimating the critical time for implementing gas injection on the basis of the total cumulative gas production. Results are presented as crossplots of 1) P/Z2 vs. Gpt, 2) Gpt vs. time and 3) gas rate vs. time. It is concluded that estimation of the critical time for implementing gas injection is useful for improving the performance of those shale gas condensate reservoirs where condensate buildup represents a threat that can negatively impact the gas production rate. The novelty of this work resides on the fact that the combined effect of free, adsorbed and dissolved gas production mechanisms on stress-sensitive shale gas condensate reservoirs has not been considered previously in the literature for estimation of OGIP and OCIP using an analytical MBE.
Summary During the last few years, production of liquid hydrocarbons has been reported from the gas-condensate window of the Eagle Ford, Barnett, Niobrara, and Marcellus shale plays in the US. This paper presents a new material-balance equation (MBE) for estimation of original gas in place (OGIP) and original condensate in place (OCIP) in shale-gas-condensate reservoirs. This material-balance methodology allows estimating the critical time for implementing gas injection in those cases in which condensate buildup represents a problem. In addition, the proposed MBE considers the effects of free, adsorbed, and dissolved gas-condensate production, and also takes into account the stress-dependency of porosity and permeability. An extension of the methodology is implemented for estimating the optimum time for hydraulically refracturing shale-condensate reservoirs. The new MBE applies to shale-gas-condensate reservoirs by incorporating a two-phase gas-deviation factor (Z2) and total cumulative gas production (Gpt) that includes both gas and condensate. If a crossplot of P/Z2 (pressure/Z2) vs. Gpt is prepared for a conventional gas-condensate reservoir, a single straight line is obtained. However, when the single-phase gas-compressibility factor (Z) is used, a deviation from the linear behavior is observed after the reservoir pressure falls below the gas dewpoint. This methodology is applied in this study to unconventional shale-gas condensate. Because there are three characteristic stages of production in a shale-gas reservoir (production of free, adsorbed, and dissolved gas), the location of the aforementioned deviation will provide a hint of the production stage that will be affected by condensate buildup. For example, if the deviation point is in the region where production of free gas is predominant, then the production caused by desorption mechanisms will be negatively affected because condensation will have already occurred in the reservoir, resulting in reduction of effective permeability to gas. This methodology then allows estimating the critical time for implementing gas injection on the basis of the total cumulative gas production. The method also permits estimating the optimum time for refracturing. The refracturing can be of a normal size for a given shale (similar to the original fracturing job), or it can be a superfrac job. Results are presented as crossplots of (1) P/Z2 vs. Gpt, (2) Gpt vs. time, and (3) gas rate vs. time. It is concluded that estimation of the critical time for implementing gas injection is useful for improving the performance of those shale-gas-condensate reservoirs in which condensate buildup represents a threat that can negatively affect the gas-production rate. The novelty of this work resides on the fact that the combined effect of free, adsorbed, and dissolved gas-production mechanisms on stress-sensitive shale-gas-condensate reservoirs had not been considered previously in the literature for estimation of OGIP, OCIP, and reservoir performance with an analytical MBE. The inclusion of gas injection and refracturing had not been considered either.
Selecting a good fracturing candidate that can maximize the complex fracture network in advance is beneficial for enhancing the fracturing effectiveness and the economic development of shale gas reservoirs. Brittleness is generally used to evaluate the capability of complex fracture networks by using critical mechanical parameters, but these parameters must be acquired from well logs and time-consuming triaxial core-scale mechanical tests. However, considering the physical and chemical instability of shales, standard-sized core plugs are difficult to obtain in some zones of interest. Thus, the analysis of drill cuttings by the combination of SEM/EDS (scanning electron microscopy-energy dispersive spectrometer) analyses and grid nanoindentation was used to replace conventional standard measurements on high-quality sized cores. A significant advantage of this technique is that drill cuttings can be collected from most wells. Furthermore, in contrast to traditional tests, the petrophysical and mechanical properties of shales can be characterized simultaneously. Thus, a comprehensive brittleness model can be established based on the mineral brittleness and mechanical brittleness. Experimental results demonstrate that the integration of grid nanoindentation and the deconvolution technique can provide reliable estimations of the homogenized Young's modulus and Poisson's ratio, while EDS mapping can provide accurate mineral compositions of the indentation area. The method is successfully applied to evaluate the brittleness of a shale gas well in a shale gas field in China, which demonstrates that this method is a fast and cost-efficient way to evaluate the brittleness of shale gas formations with a small volume of rock samples.
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