scholarly journals Numerical simulation of hydraulic fracturing in coal seam for enhancing underground gas drainage

2018 ◽  
Vol 37 (1) ◽  
pp. 166-193 ◽  
Author(s):  
Chaojun Fan ◽  
Sheng Li ◽  
Mingkun Luo ◽  
Zhenhua Yang ◽  
Tianwei Lan

Hydraulic fracturing is an efficiency approach to improve underground gas drainage. Although the interaction of fluid and coal has been comprehensively investigated in fracturing process and gas drainage process, fewer scholars have combined these two processes together and taken the gas–water two-phase flow into account, which brought a large deviation for design of hydraulic fracturing enhancing underground gas drainage. In this paper, we proposed a fully coupled hydraulic stress damage mathematical model considering gas–water two-phase flow, which can be used to simulate the whole process of hydraulic fracturing enhancing underground gas drainage. The coal seam is simplified as a dual-porosity single-permeability elastic media with elastic modulus reduce and permeability increase when encountered damage. The permeability and porosity serving as the coupling term is a function of stress, water/gas pressure, gas ad/desorption, and damage value. The proposed model was first verified by showing that the modeled gas flux agrees with the field data. The evolution laws of permeability and gas pressure during hydraulic fracturing enhancing underground gas drainage were studied and several influence factors were analyzed by accomplishing a series of simulations. Gas drainage can be effectively enhanced only when the hydraulic fracturing induced damage zone is breakthrough at drainage hole. After the coal seam is effectively fractured, the gas flux has a decline–incline–decline tendency with increasing of drainage time. The breakthrough time of damage zone increases linearly with coal seam elastic modulus, increases exponentially with vertical stress and borehole spacing, and decreases exponentially with injecting pressure.

Micromachines ◽  
2021 ◽  
Vol 12 (5) ◽  
pp. 510
Author(s):  
Yan Huang ◽  
Bifen Shu ◽  
Shengnan Zhou ◽  
Qi Shi

In this paper, two-phase pressure drop data were obtained for boiling in horizontal rectangular microchannels with a hydraulic diameter of 0.55 mm for R-134a over mass velocities from 790 to 1122, heat fluxes from 0 to 31.08 kW/m2 and vapor qualities from 0 to 0.25. The experimental results show that the Chisholm parameter in the separated flow model relies heavily on the vapor quality, especially in the low vapor quality region (from 0 to 0.1), where the two-phase flow pattern is mainly bubbly and slug flow. Then, the measured pressure drop data are compared with those from six separated flow models. Based on the comparison result, the superficial gas flux is introduced in this paper to consider the comprehensive influence of mass velocity and vapor quality on two-phase flow pressure drop, and a new equation for the Chisholm parameter in the separated flow model is proposed as a function of the superficial gas flux . The mean absolute error (MAE ) of the new flow correlation is 16.82%, which is significantly lower than the other correlations. Moreover, the applicability of the new expression has been verified by the experimental data in other literatures.


Author(s):  
Sujin Yeom ◽  
Seung S. Lee ◽  
Sang Yong Lee

This paper presents a micro-fluidic device which generates micro-bubbles, ranging from 70μm to 160μm in diameter, and two-phase flow characteristics in the device were tested. The device is composed of three sub-channels: a centered gas channel (10μm×50μm) and two liquid channels (both with 85μm×50μm) on each side of the gas channel. Micro-bubbles are generated by co-flow of gas and liquid at the exit of the gas channel when the drag force becomes larger than the surface tension force as bubbles grow. Methanol and a gas mixture of CO2 and N2 were used as the working fluid. Since the flow rate of gas was very small, the gas momentum effect was considered negligible. Thus, in the present case, the controlling parameters were the liquid superficial velocity and the inlet pressure of the gas. A high speed camera was used to record two-phase flow patterns and micro-bubbles of the device. To confine the ranges of the micro-bubbles generation, two-phase flow patterns in the device is observed at first. Four different flow patterns were observed: annular, annular-slug, slug, and bubbly flow. In bubbly flows, uniform-sized micro-bubbles were generated, and the operating ranges of the liquid superficial velocity and the gas pressure were below 0.132 m/s and 0.7 bar, respectively. Diameters of the micro-bubbles appeared smaller with the higher superficial liquid velocity and/or with a lower gas pressure. Experimental results showed that, with the gas pressure lower than a certain level, the sizes of micro-bubbles were almost insensitive to the gas pressure. In such a ranges, the micro-bubble diameters could be estimated from a drag coefficient correlation, CDw = 31330/Re3, which is different from the correlations for macro-channels due to a larger wall effect with the micro-channels. In the latter part of the paper, as a potential of application of the micro-bubble generator to gas analysis, dissolution behavior of the gas components into the liquid flow was examined. The result shows that the micro-bubble generator can be adopted as a component of miniaturized gas analyzers if a proper improvement could be made in controlling the bubble sizes effectively.


1988 ◽  
Vol 14 (1) ◽  
pp. 107-111 ◽  
Author(s):  
Yoshishige Hayashi ◽  
Eiji Hirai ◽  
Yasuhide Nakano ◽  
Masakatsu Urairi

1984 ◽  
Vol 24 (02) ◽  
pp. 141-152 ◽  
Author(s):  
A. Settari ◽  
H.S. Price

Abstract Computer-based numerical simulation can be used as a tool for analysis of fracturing treatments and prediction of postfracturing well performance. The physical problem studied involves fracture mechanics, fluid flow, and heat transfer both in the fracture and in the reservoir. The numerical model predicts fracture extension, length, and width; proppant transport and settlement; fracture closure; cleanup, and postfracturing performance under different producing conditions. The number of physical features that are customarily neglected in fracture designs have been incorporated in the present model. These include stress-sensitive reservoir properties, proper two-phase calculation of leakoff and cleanup, stress-dependent fracture permeability and temperature- and time-dependent fracturing fluid rheology. The utility and a priori predictive capability of the model is illustrated with two examples of fracturing jobs. The first example is a marginal gas well stimulated by a medium-size gelled-water fracturing job. The second example is a massive foam fracture in the Elmworth basin. In both cases, the simulator predicted results that are in good agreement with the observed productivity. Introduction Fracturing technology has been developing rapidly in recent years. Both the size and sophistication of field treatments have increased dramatically. The development of low-permeability gas reserves is especially dependent on successful and economical application of fracturing technology. The low-permeability gas sands often have permeability below 1 ud and discontinuous (lenticular) or dual porosity structure. A number of very large treatments have been performed with varied results. Compared with the rapid development of field technology, design and analysis of massive hydraulic fracturing (MHF) treatments have involved traditional methods based on correlations and crude approximations. Design methods used by service companies and industry concentrate on the prediction of fracture shape and proppant placement, and as such do not predict accurately deliverability after the fracturing job. Such methods cannot be used for design optimization, which must be based on accurate long-term production forecasts. In addition, the various aspects of the process are, of necessity, treated separately. Typically, fracture extension, leakoff, fracturing fluid heatup, and cleanup all are determined independently using simplifying assumptions about their mutual influence. The need for production-forecasting tools has been recognized by reservoir engineers who developed analytical and numerical techniques for predicting the deliverability of fractured wells. The most advanced approaches of this type involve conventional finite-difference reservoir simulation techniques and are used for optimization of treatment size. The common weakness of analyses of this type is that the fracture is treated as static and many of the variables controlling deliverability (such as fracture length, conductivity, propped length, and height) must be entered and are typically obtained by the design methods discussed previously. Also, the influence of the fracturing job on the reservoir (such as damage by the fluid) cannot be properly accounted for. The need for tools that would model the entire process in a more rigorous fashion is obvious. Most of the information on the fracturing operations in the field must be obtained indirectly, and production testing yields the basic and most important data. A meaningful tool for analysis of treatments must therefore correctly model the interaction between the fracturing operation and the postfracture behavior. This paper describes development and field application of a comprehensive simulator that treats in an integrated fashion all important aspects of the problem. The correctness of our approach has been confirmed by validation against field data, showing excellent agreement. Our model still simplifies treatment of fracture containment, and ongoing development is directed toward enhancements that will allow a priori optimization of treatments including containment. General Description of the Simulator Although the model is general and can be used in other applications, this paper addresses only those features of interest in fracturing treatments. The relevant geometry is shown in Fig. 1. The model simulates two-dimensional (2D), compressible, two-phase flow and heat transfer simultaneously with initiation and propagation of a vertical hydraulic fracture. Once the fracture exists, appropriate equations of two-phase flow and heat transfer in the fracture also are solved. SPEJ P. 141^


2021 ◽  
Vol 377 ◽  
pp. 55-69
Author(s):  
Bin Zhou ◽  
Jiang Xu ◽  
Fazhi Yan ◽  
Shoujian Peng ◽  
Yabin Gao ◽  
...  

Energies ◽  
2019 ◽  
Vol 12 (4) ◽  
pp. 735 ◽  
Author(s):  
Grzegorz Ligus ◽  
Daniel Zając ◽  
Maciej Masiukiewicz ◽  
Stanisław Anweiler

This paper presents experimental studies on the optimization of two-phase fluid flow in an airlift pump. Airlift pumps, also known as mammoth pumps, are devices applied for vertical transport of liquids with the use of gas. Their operating principle involves the existence of a density gradient. This paper reports the results of experimental studies into the hydrodynamic effects of the airlift pump. The studies involved optical imaging of two-phase gas-liquid flow in a riser pipe. The visualization was performed with high-speed visualization techniques. The studies used a transparent model of airlift pump with a rectangular cross-section of the riser. The assessment of the airlift pump operation is based on the image grey-level analysis to provide the identification of two-phase flow regimes. The scope of the study also involved the determination of void fraction and pressure drops. The tests were carried out in a channel with dimensions 35 × 20 × 2045 mm with the gas flux range 0.2–15.0 m3/h. For the assessment of the two-phase flow pattern Probability Density Function (PDF) was applied. On the basis of the obtained results, a new method for selecting the optimum operating regime of airlift pump was derived. This method provides the finding of stability and efficiency of liquid transport. It can also be applied to determine the correlation between the total lifting efficiency and the required gas flux for proper operation of the airlift pump.


2020 ◽  
Vol 34 (4) ◽  
pp. 4273-4288 ◽  
Author(s):  
Guanglei Cui ◽  
Yuling Tan ◽  
Tianyu Chen ◽  
Xia-Ting Feng ◽  
Derek Elsworth ◽  
...  

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