<?xml version="1.0" encoding="UTF-8"?><!DOCTYPE article  PUBLIC "-//NLM//DTD Journal Publishing DTD v3.0 20080202//EN" "http://dtd.nlm.nih.gov/publishing/3.0/journalpublishing3.dtd"><article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" dtd-version="3.0" xml:lang="en" article-type="research article"><front><journal-meta><journal-id journal-id-type="publisher-id">JPEE</journal-id><journal-title-group><journal-title>Journal of Power and Energy Engineering</journal-title></journal-title-group><issn pub-type="epub">2327-588X</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/jpee.2017.511004</article-id><article-id pub-id-type="publisher-id">JPEE-80531</article-id><article-categories><subj-group subj-group-type="heading"><subject>Articles</subject></subj-group><subj-group subj-group-type="Discipline-v2"><subject>Engineering</subject></subj-group></article-categories><title-group><article-title>
 
 
  Prediction of Coal Bed Methane Recovery Rate and Its Improvement Measures in Dafosi Mine Field
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Dongmin</surname><given-names>Ma</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Chenyang</surname><given-names>Zhang</given-names></name><xref ref-type="aff" rid="aff2"><sup>2</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Chuantao</surname><given-names>Wang</given-names></name><xref ref-type="aff" rid="aff2"><sup>2</sup></xref><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Xiaoyan</surname><given-names>Tang</given-names></name><xref ref-type="aff" rid="aff2"><sup>2</sup></xref></contrib></contrib-group><aff id="aff1"><addr-line>National Energy Key Laboratory of Coal and CBM Simultaneous Extraction, Jincheng, China</addr-line></aff><aff id="aff2"><addr-line>College of Geology and Environment, Xi’an University of Science and Technology, Xi’an, China</addr-line></aff><author-notes><corresp id="cor1">* E-mail:<email>chant2012@163.com(CW)</email>;</corresp></author-notes><pub-date pub-type="epub"><day>17</day><month>11</month><year>2017</year></pub-date><volume>05</volume><issue>11</issue><fpage>37</fpage><lpage>49</lpage><history><date date-type="received"><day>11,</day>	<month>October</month>	<year>2017</year></date><date date-type="rev-recd"><day>21,</day>	<month>November</month>	<year>2017</year>	</date><date date-type="accepted"><day>24,</day>	<month>November</month>	<year>2017</year></date></history><permissions><copyright-statement>&#169; Copyright  2014 by authors and Scientific Research Publishing Inc. </copyright-statement><copyright-year>2014</copyright-year><license><license-p>This work is licensed under the Creative Commons Attribution International License (CC BY). http://creativecommons.org/licenses/by/4.0/</license-p></license></permissions><abstract><p>
 
 
  The recovery rate of coalbed methane (CBM) can reflect the mining situation and the residual gas in coal reservoir. It plays an important role in the calculation of the recoverable resources. This paper mainly uses isothermal adsorption curve method and hydraulic model method to predict recovery rate of CBM. The isothermal adsorption curve method considering desorption lag problem in the prediction process, which is more in line with the actual situation. In the hydraulic model method, the recovery rate of “V” type well is the largest in the early stage. But with the time going on, the recovery rate of multilateral horizontal well is greater than vertical well, “U” type well and “V” type well finally. The factors affecting CBM recovery rate include geological characteristics, development conditions and economic factors. The geological characteristics of coal reservoir are the main factors affecting CBM recovery rate, and corresponding measures can be adopted to improve the recovery rate.
 
</p></abstract><kwd-group><kwd>Recovery Rate</kwd><kwd> Isothermal Adsorption Curve Method</kwd><kwd> Hydraulic Model  Method</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>CBM recovery rate refers to an economic limit, can be produced by percentage of CBM from CBM reserves in the current engineering and technical conditions, can reflect the mining situation of CBM, and the residual gas in coal reservoir. The recoverable resources of CBM are obtained by multiplying the amount of geological resources by the recovery rate and it is an important basis for investment decision, implementation and adjustment of development plan.</p><p>The exploration and development of CBM has been explored and developed for more than 20 years in China. Basically, the two industrial development bases of Qinshui Basin and Ordos Basin have been formed. The development of the CBM industry in recent years, CBM development technology has made great progress, mainly in the deep coal seam fracturing, refracturing, layer fracturing and tectonic coal production measures [<xref ref-type="bibr" rid="scirp.80531-ref1">1</xref>] . These technologies have solved a series of problems, such as pulverized coal blockage. In fact, there are some factors restricting the development of CBM, including geological factors, mining technology factors, industrial policy factors and so on [<xref ref-type="bibr" rid="scirp.80531-ref2">2</xref>] . The structure of CBM reservoir formation is complex in China, and the effect of foreign mining technology is not satisfactory in the development and application of CBM. China’s mining technology also has some limitations, resulting in the backwardness of China’s CBM industry development.</p><p>In view of the low recovery rate of CBM in China, domestic scholars have also conducted relevant research, mainly in gas injection production. Zhao Jin [<xref ref-type="bibr" rid="scirp.80531-ref3">3</xref>] carried out numerical simulation of carbon dioxide injection method for enhancing CBM recovery rate. The results show that carbon dioxide injection can improve the production technology of CBM production and recovery, Shen Jian<sup> </sup> [<xref ref-type="bibr" rid="scirp.80531-ref4">4</xref>] carried out feasibility analysis about carbon dioxide injection, also got a similar conclusion. Zheng Yuzhu [<xref ref-type="bibr" rid="scirp.80531-ref5">5</xref>] has studied the factors that influence CBM recovery rate and it is considered that the geological characteristics, development conditions and economic factors of coal reservoir have important influence on recovery rate of CBM. At present the study about Dafosi mine field CBM exploitation has mainly carried on the pore characteristics, CBM workability and the occurrence characteristics of CBM. However, there is a lack of research on recovery rate, so it is necessary to study the recovery rate of CBM in Dafosi mine field.</p><p>At present, there are few researches on low rank coal recovery rate in China. When using the isothermal adsorption curve to predict recovery rate, it is considered that adsorption and desorption are reversible, and the desorption lag is not taken into consideration [<xref ref-type="bibr" rid="scirp.80531-ref6">6</xref>] [<xref ref-type="bibr" rid="scirp.80531-ref7">7</xref>] . This paper mainly uses the isothermal adsorption curve method and the hydraulic model method to predict the recovery rate in Dafosi mine field, the isothermal adsorption curve method considering desorption lag problem, provides a new idea for prediction of Dafosi mine field recovery rate.</p></sec><sec id="s2"><title>2. Prediction of CBM Recovery Rate in Dafosi Mine Field</title><sec id="s2_1"><title>2.1. Selection of Prediction Methods</title><p>The prediction methods of CBM recovery rate [<xref ref-type="bibr" rid="scirp.80531-ref8">8</xref>] [<xref ref-type="bibr" rid="scirp.80531-ref9">9</xref>] include numerical simulation method, analog method, isothermal adsorption curve method, desorption method and production decline method. The numerical simulation method is based on the CBM production mechanism, through the establishment of geological model and mathematical model, the use of computer to predict the recovery rate. The analog method is used to obtain the recovery rate by comparing with the area where the recovery rate has been obtained. The isothermal adsorption curve method is based on the adsorption of methane on coal in accordance with the Langmuir equation, through calculating the adsorption amount under the waste pressure, the recovery rate is obtained. CBM content is composed of three parts: stripping gas, lost gas and residual gas. Stripping gas and lost gas can be desorbed under natural conditions. The desorption method is used to calculate the recovery rate by calculating the rate of stripping gas and lost gas content. The production decline method is to calculate the recovery ratio through the original coalbed gas content and the abandoned content at the end of exploitation.</p><p>The analogy method requires a similar geological condition and has obtained CBM recovery rate areas for comparison. The production decline method is too simple and has low reliability. The prediction of CBM recovery rate by desorption method will be affected by related geological factors. So this paper uses the isothermal adsorption curve method and the hydraulic model method to predict recovery rate. The data of isothermal adsorption curve are easy to obtain, and the predicted recovery rate can be well consistent with the actual production at present stage. The hydraulic model method [<xref ref-type="bibr" rid="scirp.80531-ref10">10</xref>] [<xref ref-type="bibr" rid="scirp.80531-ref11">11</xref>] can well predict the future recovery rate, and has a good prediction and guidance for the future production of CBM. But the two methods have certain limitations, the isothermal adsorption curve method is mainly the determination method of waste pressure is not uniform, may cause the final result of deviation. The hydraulic model method has a long duration, so it is necessary to obtain a large amount of CBM drainage data for calculation.</p></sec><sec id="s2_2"><title>2.2. CBM Recovery Rate Prediction</title><sec id="s2_2_1"><title>2.2.1. Isothermal Adsorption Curve Method</title><p>The adsorption of methane on coal is suitable for the Langmuir equation, and the process is a reversible process, which provides a theoretical basis for the prediction of recovery rate by the isothermal adsorption curve method. According to the isothermal adsorption test of coal, with the increase of pressure, the ability of coal to absorb methane is enhanced. When a certain amount of methane is adsorbed on coal, the methane is desorbed and adsorption decreases as the pressure decreases. The formula of CBM recovery rate is expressed by the isothermal adsorption curve method:</p><disp-formula id="scirp.80531-formula9"><graphic  xlink:href="//html.scirp.org/file/4-1770410x2.png"  xlink:type="simple"/></disp-formula><p>η―CBM Recovery rate;</p><p>G―initial CBM content;</p><p>V<sub>u</sub>―adsorption capacity of CBM under obsolete pressure.</p><p>Samples were collected at site and balanced water experiments were carried out on the samples. After the sample preparation was completed, the methane adsorption/desorption experiments were carried out. Experiments were carried out by using AST-2000 type CBM adsorption/desorption experimental instrument, five experimental temperature points were set at 25˚C, 30˚C, 35˚C, 40˚C, 45˚C. The isothermal adsorption experiment is a repetitive process of prelum- equilibrium-prelum, and the isothermal desorption experiment is a repetitive process of depressurization-equilibrium-depressurization. Experimental equipment automatically collects the pressure, temperature and other experimental data.</p><p>The adsorption process was fitted by Langmuir equation [<xref ref-type="bibr" rid="scirp.80531-ref12">12</xref>] [<xref ref-type="bibr" rid="scirp.80531-ref13">13</xref>] [<xref ref-type="bibr" rid="scirp.80531-ref14">14</xref>] . The equation assumes that there is no adsorption molecule interaction in the surface phase, and the probability of each molecule adsorbed is the same, which is a single molecule layer adsorption model. The desorption equation [<xref ref-type="bibr" rid="scirp.80531-ref15">15</xref>] is used to fit the desorption process:</p><disp-formula id="scirp.80531-formula10"><graphic  xlink:href="//html.scirp.org/file/4-1770410x3.png"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.80531-formula11"><graphic  xlink:href="//html.scirp.org/file/4-1770410x4.png"  xlink:type="simple"/></disp-formula><p>V<sub>a</sub>―adsorption capacity of CBM under pressure P in adsorption process;</p><p>V<sub>b</sub>―adsorption capacity of CBM under pressure P during desorption;</p><p>a―saturated adsorption capacity of coal sample;</p><p>b―comprehensive parameters related to adsorption heat;</p><p>c―residual adsorption capacity.</p><p>The experimental results are shown in <xref ref-type="table" rid="table1">Table 1</xref> and <xref ref-type="fig" rid="fig1">Figure 1</xref>.</p><p>Experience of CBM development in the United States, under the better market conditions, it is feasible and economical to carry out the drainage of coalbed to achieve the overall depressurization of 85%. Therefore, the CBM recovery rate can be calculated by 15% of the original pressure of coalbed, and the calculation results are shown in <xref ref-type="table" rid="table2">Table 2</xref>.</p><p>In summary, recovery rate increases with the increase of temperature. When the desorption lag is not considered, the recovery rate is 36.41% to 50.43%. When the delayed desorption is taken into consideration, the recovery rate is only 9.40% to 25.39%.</p><table-wrap id="table1" ><label><xref ref-type="table" rid="table1">Table 1</xref></label><caption><title> Experimental results of adsorption/desorption of Dafosi NO.4 coalbed equilibrium water sample</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Temperature/˚C</th><th align="center" valign="middle"  colspan="3"  >Langmuir fitting</th><th align="center" valign="middle"  colspan="4"  >The desorption formula fitting</th></tr></thead><tr><td align="center" valign="middle" >a</td><td align="center" valign="middle" >b</td><td align="center" valign="middle" >R<sup>2</sup></td><td align="center" valign="middle" >a</td><td align="center" valign="middle" >b</td><td align="center" valign="middle" >c</td><td align="center" valign="middle" >R<sup>2</sup></td></tr><tr><td align="center" valign="middle" >25</td><td align="center" valign="middle" >11.563</td><td align="center" valign="middle" >0.448</td><td align="center" valign="middle" >0.992</td><td align="center" valign="middle" >8.623</td><td align="center" valign="middle" >0.701</td><td align="center" valign="middle" >0.949</td><td align="center" valign="middle" >0.996</td></tr><tr><td align="center" valign="middle" >30</td><td align="center" valign="middle" >11.566</td><td align="center" valign="middle" >0.396</td><td align="center" valign="middle" >0.990</td><td align="center" valign="middle" >8.341</td><td align="center" valign="middle" >0.619</td><td align="center" valign="middle" >0.994</td><td align="center" valign="middle" >0.997</td></tr><tr><td align="center" valign="middle" >35</td><td align="center" valign="middle" >11.079</td><td align="center" valign="middle" >0.382</td><td align="center" valign="middle" >0.993</td><td align="center" valign="middle" >8.040</td><td align="center" valign="middle" >0.597</td><td align="center" valign="middle" >0.973</td><td align="center" valign="middle" >0.998</td></tr><tr><td align="center" valign="middle" >40</td><td align="center" valign="middle" >10.725</td><td align="center" valign="middle" >0.374</td><td align="center" valign="middle" >0.993</td><td align="center" valign="middle" >7.698</td><td align="center" valign="middle" >0.543</td><td align="center" valign="middle" >1.039</td><td align="center" valign="middle" >0.999</td></tr><tr><td align="center" valign="middle" >45</td><td align="center" valign="middle" >10.238</td><td align="center" valign="middle" >0.382</td><td align="center" valign="middle" >0.993</td><td align="center" valign="middle" >7.380</td><td align="center" valign="middle" >0.568</td><td align="center" valign="middle" >1.009</td><td align="center" valign="middle" >0.998</td></tr></tbody></table></table-wrap><table-wrap id="table2" ><label><xref ref-type="table" rid="table2">Table 2</xref></label><caption><title> Recovery rate of Dafosi No. 4 coalbed equilibrium water sample</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Temperature</th><th align="center" valign="middle"  rowspan="2"  >V<sub>G</sub></th><th align="center" valign="middle"  rowspan="2"  >P<sub>O</sub></th><th align="center" valign="middle"  colspan="2"  >V<sub>u</sub></th><th align="center" valign="middle"  colspan="2"  >Recovery rate/%</th></tr></thead><tr><td align="center" valign="middle" >Langmuir</td><td align="center" valign="middle" >The desorption formula</td><td align="center" valign="middle" >Langmuir</td><td align="center" valign="middle" >The desorption formula</td></tr><tr><td align="center" valign="middle" >25˚C</td><td align="center" valign="middle" >3.89</td><td align="center" valign="middle" >0.6075</td><td align="center" valign="middle" >2.4737345</td><td align="center" valign="middle" >3.5244111</td><td align="center" valign="middle" >36.408</td><td align="center" valign="middle" >9.398</td></tr><tr><td align="center" valign="middle" >30˚C</td><td align="center" valign="middle" >3.89</td><td align="center" valign="middle" >0.6075</td><td align="center" valign="middle" >2.2428663</td><td align="center" valign="middle" >3.2734140</td><td align="center" valign="middle" >42.343</td><td align="center" valign="middle" >15.851</td></tr><tr><td align="center" valign="middle" >35˚C</td><td align="center" valign="middle" >3.89</td><td align="center" valign="middle" >0.6075</td><td align="center" valign="middle" >2.0867796</td><td align="center" valign="middle" >3.1128512</td><td align="center" valign="middle" >46.355</td><td align="center" valign="middle" >19.978</td></tr><tr><td align="center" valign="middle" >40˚C</td><td align="center" valign="middle" >3.89</td><td align="center" valign="middle" >0.6075</td><td align="center" valign="middle" >1.9856288</td><td align="center" valign="middle" >2.9484752</td><td align="center" valign="middle" >48.956</td><td align="center" valign="middle" >24.204</td></tr><tr><td align="center" valign="middle" >45˚C</td><td align="center" valign="middle" >3.89</td><td align="center" valign="middle" >0.6075</td><td align="center" valign="middle" >1.9283735</td><td align="center" valign="middle" >2.9022559</td><td align="center" valign="middle" >50.427</td><td align="center" valign="middle" >25.392</td></tr></tbody></table></table-wrap></sec><sec id="s2_2_2"><title>2.2.2. Hydraulic Model Method</title><p>The method is to approximate the drainage and production process of CBM well into the unsteady flow full pressure well pumping process, using the The is formula to calculate reservoir water conduction coefficient. The influence radius is calculated by Jacob formula during the process of production, a gas production model was established to calculate recovery rate.</p><p>1) Calculation of recovery rate in vertical well</p><p>Taking No. 1 well in Dafosi mine field as an example, the recovery rate of vertical well is calculated. During the stage of stable production of drainage, the coefficient of water conductivity was calculated by the The is formula, which was 0.0064584m<sup>2</sup>/d and the water supply of the aquifer was 0.001. The radius of influence is calculated by Jacob formula, the calculation result is shown in <xref ref-type="table" rid="table3">Table 3</xref> and the recovery curve is shown in <xref ref-type="fig" rid="fig2">Figure 2</xref>.</p><p>2) Calculation of recovery rate in “U” type well</p><p>Taking No. 2 well in Dafosi mine field as an example, the recovery rate of “U” type well is calculated. During the stage of stable production of drainage, the</p><table-wrap id="table3" ><label><xref ref-type="table" rid="table3">Table 3</xref></label><caption><title> Calculation results of recovery rate in vertical well</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Time/m</th><th align="center" valign="middle" >Bottomhole pressure P<sub>w</sub>/MPa</th><th align="center" valign="middle" >Influence radius R<sub>e</sub>/m</th><th align="center" valign="middle" >Desorption radius r/m</th><th align="center" valign="middle" >Theoretical cumulative gas production Q<sub>L</sub>/m<sup>3</sup>・t<sup>−1</sup></th><th align="center" valign="middle" >Actual cumulative gas production Q<sub>S</sub>/m<sup>3</sup>・t<sup>−1</sup></th><th align="center" valign="middle" >Recovery rate η/%</th></tr></thead><tr><td align="center" valign="middle" >1</td><td align="center" valign="middle" >0.831</td><td align="center" valign="middle" >20.074</td><td align="center" valign="middle" >11.52</td><td align="center" valign="middle" >139314.44</td><td align="center" valign="middle" >1647.08</td><td align="center" valign="middle" >1.18</td></tr><tr><td align="center" valign="middle" >6</td><td align="center" valign="middle" >0.472</td><td align="center" valign="middle" >49.171</td><td align="center" valign="middle" >27.55</td><td align="center" valign="middle" >1013071.66</td><td align="center" valign="middle" >137187.46</td><td align="center" valign="middle" >13.54</td></tr><tr><td align="center" valign="middle" >12</td><td align="center" valign="middle" >0.334</td><td align="center" valign="middle" >69.538</td><td align="center" valign="middle" >38.66</td><td align="center" valign="middle" >2171867.88</td><td align="center" valign="middle" >384884.42</td><td align="center" valign="middle" >17.72</td></tr><tr><td align="center" valign="middle" >18</td><td align="center" valign="middle" >0.253</td><td align="center" valign="middle" >85.167</td><td align="center" valign="middle" >47.14</td><td align="center" valign="middle" >3388736.99</td><td align="center" valign="middle" >719452.65</td><td align="center" valign="middle" >21.23</td></tr><tr><td align="center" valign="middle" >24</td><td align="center" valign="middle" >0.195</td><td align="center" valign="middle" >98.342</td><td align="center" valign="middle" >54.27</td><td align="center" valign="middle" >4643938.07</td><td align="center" valign="middle" >1083731.93</td><td align="center" valign="middle" >23.34</td></tr><tr><td align="center" valign="middle" >30</td><td align="center" valign="middle" >0.151</td><td align="center" valign="middle" >109.95</td><td align="center" valign="middle" >60.55</td><td align="center" valign="middle" >5927941.83</td><td align="center" valign="middle" >1448421.36</td><td align="center" valign="middle" >24.43</td></tr><tr><td align="center" valign="middle" >36</td><td align="center" valign="middle" >0.114</td><td align="center" valign="middle" >120.44</td><td align="center" valign="middle" >66.21</td><td align="center" valign="middle" >7235075.67</td><td align="center" valign="middle" >1881095.72</td><td align="center" valign="middle" >26.00</td></tr><tr><td align="center" valign="middle" >42</td><td align="center" valign="middle" >0.112</td><td align="center" valign="middle" >130.09</td><td align="center" valign="middle" >71.40</td><td align="center" valign="middle" >8441543.77</td><td align="center" valign="middle" >2355419.48</td><td align="center" valign="middle" >27.90</td></tr><tr><td align="center" valign="middle" >48</td><td align="center" valign="middle" >0.110</td><td align="center" valign="middle" >139.08</td><td align="center" valign="middle" >76.24</td><td align="center" valign="middle" >9647428.96</td><td align="center" valign="middle" >2872174.28</td><td align="center" valign="middle" >29.77</td></tr><tr><td align="center" valign="middle" >54</td><td align="center" valign="middle" >0.108</td><td align="center" valign="middle" >147.51</td><td align="center" valign="middle" >80.77</td><td align="center" valign="middle" >10853852.19</td><td align="center" valign="middle" >3431360.12</td><td align="center" valign="middle" >31.61</td></tr><tr><td align="center" valign="middle" >60</td><td align="center" valign="middle" >0.107</td><td align="center" valign="middle" >155.49</td><td align="center" valign="middle" >85.06</td><td align="center" valign="middle" >12060957.68</td><td align="center" valign="middle" >4032977.00</td><td align="center" valign="middle" >33.44</td></tr><tr><td align="center" valign="middle" >66</td><td align="center" valign="middle" >0.105</td><td align="center" valign="middle" >163.08</td><td align="center" valign="middle" >87.61</td><td align="center" valign="middle" >13268867.60</td><td align="center" valign="middle" >4677024.92</td><td align="center" valign="middle" >35.25</td></tr><tr><td align="center" valign="middle" >72</td><td align="center" valign="middle" >0.103</td><td align="center" valign="middle" >170.33</td><td align="center" valign="middle" >91.22</td><td align="center" valign="middle" >14477686.91</td><td align="center" valign="middle" >5363503.88</td><td align="center" valign="middle" >37.05</td></tr><tr><td align="center" valign="middle" >78</td><td align="center" valign="middle" >0.101</td><td align="center" valign="middle" >177.29</td><td align="center" valign="middle" >94.67</td><td align="center" valign="middle" >15687506.82</td><td align="center" valign="middle" >6092413.88</td><td align="center" valign="middle" >38.84</td></tr><tr><td align="center" valign="middle" >84</td><td align="center" valign="middle" >0.099</td><td align="center" valign="middle" >183.98</td><td align="center" valign="middle" >97.98</td><td align="center" valign="middle" >16898407.42</td><td align="center" valign="middle" >6863754.92</td><td align="center" valign="middle" >40.62</td></tr></tbody></table></table-wrap><p>coefficient of water conductivity was calculated by the The is formula, which was 0.02689068m<sup>2</sup>/d and the water supply of the aquifer was 0.005. The radius of influence is calculated by Jacob formula, the calculation result is shown in <xref ref-type="table" rid="table4">Table 4</xref> and the recovery curve is shown in <xref ref-type="fig" rid="fig3">Figure 3</xref>.</p><p>3) Calculation of recovery rate in “V” type well</p><p>Taking No. 3 well in Dafosi mine field as an example, the recovery rate of “V” type well is calculated. During the stage of stable production of drainage, the coefficient of water conductivity was calculated by the Theis formula, which was</p><table-wrap id="table4" ><label><xref ref-type="table" rid="table4">Table 4</xref></label><caption><title> Calculation results of recovery rate in “U” type well</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Time/m</th><th align="center" valign="middle" >Bottomhole pressure P<sub>w</sub>/MPa</th><th align="center" valign="middle" >Influence radius R<sub>e</sub>/m</th><th align="center" valign="middle" >Desorption radius r/m</th><th align="center" valign="middle" >Theoretical cumulative gas production Q<sub>L</sub>/m<sup>3</sup>・t<sup>−1</sup></th><th align="center" valign="middle" >Actual cumulative gas production Q<sub>S</sub>/m<sup>3</sup>・t<sup>−1</sup></th><th align="center" valign="middle" >Recovery rate η/%</th></tr></thead><tr><td align="center" valign="middle" >1</td><td align="center" valign="middle" >1.552</td><td align="center" valign="middle" >16.84</td><td align="center" valign="middle" >7.08</td><td align="center" valign="middle" >54433.648</td><td align="center" valign="middle" >0</td><td align="center" valign="middle" >0.00</td></tr><tr><td align="center" valign="middle" >6</td><td align="center" valign="middle" >0.503</td><td align="center" valign="middle" >41.25</td><td align="center" valign="middle" >20.68</td><td align="center" valign="middle" >709580</td><td align="center" valign="middle" >33043.44</td><td align="center" valign="middle" >4.66</td></tr><tr><td align="center" valign="middle" >12</td><td align="center" valign="middle" >0.325</td><td align="center" valign="middle" >58.35</td><td align="center" valign="middle" >29.35</td><td align="center" valign="middle" >1551726.9</td><td align="center" valign="middle" >139273.06</td><td align="center" valign="middle" >8.98</td></tr><tr><td align="center" valign="middle" >18</td><td align="center" valign="middle" >0.252</td><td align="center" valign="middle" >71.46</td><td align="center" valign="middle" >35.82</td><td align="center" valign="middle" >2406545.1</td><td align="center" valign="middle" >282351.16</td><td align="center" valign="middle" >12.10</td></tr><tr><td align="center" valign="middle" >24</td><td align="center" valign="middle" >0.210</td><td align="center" valign="middle" >82.52</td><td align="center" valign="middle" >41.19</td><td align="center" valign="middle" >3266204.2</td><td align="center" valign="middle" >490164.24</td><td align="center" valign="middle" >15.01</td></tr><tr><td align="center" valign="middle" >30</td><td align="center" valign="middle" >0.183</td><td align="center" valign="middle" >92.26</td><td align="center" valign="middle" >45.86</td><td align="center" valign="middle" >4128091.3</td><td align="center" valign="middle" >694397.2</td><td align="center" valign="middle" >16.82</td></tr><tr><td align="center" valign="middle" >36</td><td align="center" valign="middle" >0.163</td><td align="center" valign="middle" >101.07</td><td align="center" valign="middle" >50.04</td><td align="center" valign="middle" >4991033.1</td><td align="center" valign="middle" >896396.69</td><td align="center" valign="middle" >17.96</td></tr><tr><td align="center" valign="middle" >42</td><td align="center" valign="middle" >0.148</td><td align="center" valign="middle" >109.17</td><td align="center" valign="middle" >53.86</td><td align="center" valign="middle" >5854416.5</td><td align="center" valign="middle" >1215320.84</td><td align="center" valign="middle" >20.76</td></tr><tr><td align="center" valign="middle" >48</td><td align="center" valign="middle" >0.136</td><td align="center" valign="middle" >116.71</td><td align="center" valign="middle" >57.39</td><td align="center" valign="middle" >6717891.5</td><td align="center" valign="middle" >1531593.44</td><td align="center" valign="middle" >22.80</td></tr><tr><td align="center" valign="middle" >54</td><td align="center" valign="middle" >0.126</td><td align="center" valign="middle" >123.79</td><td align="center" valign="middle" >60.69</td><td align="center" valign="middle" >7581245.5</td><td align="center" valign="middle" >1882333.16</td><td align="center" valign="middle" >24.83</td></tr><tr><td align="center" valign="middle" >60</td><td align="center" valign="middle" >0.118</td><td align="center" valign="middle" >130.49</td><td align="center" valign="middle" >63.80</td><td align="center" valign="middle" >8444344.8</td><td align="center" valign="middle" >2267540.00</td><td align="center" valign="middle" >26.85</td></tr><tr><td align="center" valign="middle" >66</td><td align="center" valign="middle" >0.111</td><td align="center" valign="middle" >136.86</td><td align="center" valign="middle" >66.74</td><td align="center" valign="middle" >9307103.3</td><td align="center" valign="middle" >2687213.96</td><td align="center" valign="middle" >28.87</td></tr><tr><td align="center" valign="middle" >72</td><td align="center" valign="middle" >0.105</td><td align="center" valign="middle" >142.94</td><td align="center" valign="middle" >69.54</td><td align="center" valign="middle" >10169464.7</td><td align="center" valign="middle" >3141355.04</td><td align="center" valign="middle" >30.89</td></tr><tr><td align="center" valign="middle" >78</td><td align="center" valign="middle" >0.100</td><td align="center" valign="middle" >148.78</td><td align="center" valign="middle" >72.22</td><td align="center" valign="middle" >11031392.7</td><td align="center" valign="middle" >3629963.24</td><td align="center" valign="middle" >32.91</td></tr><tr><td align="center" valign="middle" >84</td><td align="center" valign="middle" >0.096</td><td align="center" valign="middle" >154.40</td><td align="center" valign="middle" >74.79</td><td align="center" valign="middle" >11892863.9</td><td align="center" valign="middle" >4153038.56</td><td align="center" valign="middle" >34.92</td></tr></tbody></table></table-wrap><p>0.034841 m<sup>2</sup>/d and the water supply of the aquifer was 0.014102. The radius of influence is calculated by Jacob formula, the calculation result is shown in <xref ref-type="table" rid="table5">Table 5</xref> and the recovery curve is shown in <xref ref-type="fig" rid="fig4">Figure 4</xref>.</p><p>4) Calculation of recovery rate in multilateral horizontal well</p><p>Taking No. 4 well in Dafosi mine field as an example, the recovery rate of</p><table-wrap id="table5" ><label><xref ref-type="table" rid="table5">Table 5</xref></label><caption><title> Calculation results of recovery rate in “V” type well</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Time/m</th><th align="center" valign="middle" >Bottomhole pressure P<sub>w</sub>/MPa</th><th align="center" valign="middle" >Influence radius R<sub>e</sub>/m</th><th align="center" valign="middle" >Desorption radius r/m</th><th align="center" valign="middle" >Theoretical cumulative gas production Q<sub>L</sub>/m<sup>3</sup>・t<sup>−1</sup></th><th align="center" valign="middle" >Actual cumulative gas production Q<sub>S</sub>/m<sup>3</sup>・t<sup>−1</sup></th><th align="center" valign="middle" >Recovery rate η/%</th></tr></thead><tr><td align="center" valign="middle" >1</td><td align="center" valign="middle" >1.581</td><td align="center" valign="middle" >14.62</td><td align="center" valign="middle" >6.19</td><td align="center" valign="middle" >40532.34</td><td align="center" valign="middle" >0.00</td><td align="center" valign="middle" >0.00</td></tr><tr><td align="center" valign="middle" >6</td><td align="center" valign="middle" >0.545</td><td align="center" valign="middle" >35.81</td><td align="center" valign="middle" >18.03</td><td align="center" valign="middle" >525074.04</td><td align="center" valign="middle" >18306.78</td><td align="center" valign="middle" >3.49</td></tr><tr><td align="center" valign="middle" >12</td><td align="center" valign="middle" >0.152</td><td align="center" valign="middle" >50.64</td><td align="center" valign="middle" >26.57</td><td align="center" valign="middle" >1288303.46</td><td align="center" valign="middle" >81114.54</td><td align="center" valign="middle" >6.30</td></tr><tr><td align="center" valign="middle" >18</td><td align="center" valign="middle" >0.123</td><td align="center" valign="middle" >62.02</td><td align="center" valign="middle" >32.17</td><td align="center" valign="middle" >1950411.93</td><td align="center" valign="middle" >115318.03</td><td align="center" valign="middle" >6.91</td></tr><tr><td align="center" valign="middle" >24</td><td align="center" valign="middle" >0.122</td><td align="center" valign="middle" >71.61</td><td align="center" valign="middle" >36.72</td><td align="center" valign="middle" >2591424.48</td><td align="center" valign="middle" >455720.23</td><td align="center" valign="middle" >17.59</td></tr><tr><td align="center" valign="middle" >30</td><td align="center" valign="middle" >0.121</td><td align="center" valign="middle" >80.06</td><td align="center" valign="middle" >40.70</td><td align="center" valign="middle" >3230203.71</td><td align="center" valign="middle" >764080.55</td><td align="center" valign="middle" >23.65</td></tr><tr><td align="center" valign="middle" >36</td><td align="center" valign="middle" >0.120</td><td align="center" valign="middle" >87.71</td><td align="center" valign="middle" >44.26</td><td align="center" valign="middle" >3867264.08</td><td align="center" valign="middle" >1095565.18</td><td align="center" valign="middle" >28.33</td></tr><tr><td align="center" valign="middle" >42</td><td align="center" valign="middle" >0.119</td><td align="center" valign="middle" >94.73</td><td align="center" valign="middle" >47.52</td><td align="center" valign="middle" >4502960.87</td><td align="center" valign="middle" >1491565.18</td><td align="center" valign="middle" >33.12</td></tr><tr><td align="center" valign="middle" >48</td><td align="center" valign="middle" >0.117</td><td align="center" valign="middle" >101.27</td><td align="center" valign="middle" >50.55</td><td align="center" valign="middle" >5140260.34</td><td align="center" valign="middle" >1887565.18</td><td align="center" valign="middle" >36.72</td></tr><tr><td align="center" valign="middle" >54</td><td align="center" valign="middle" >0.116</td><td align="center" valign="middle" >107.42</td><td align="center" valign="middle" >53.37</td><td align="center" valign="middle" >5774300.88</td><td align="center" valign="middle" >2283565.18</td><td align="center" valign="middle" >39.55</td></tr><tr><td align="center" valign="middle" >60</td><td align="center" valign="middle" >0.115</td><td align="center" valign="middle" >113.23</td><td align="center" valign="middle" >56.03</td><td align="center" valign="middle" >6407599.99</td><td align="center" valign="middle" >2679565.18</td><td align="center" valign="middle" >41.82</td></tr><tr><td align="center" valign="middle" >66</td><td align="center" valign="middle" >0.113</td><td align="center" valign="middle" >118.75</td><td align="center" valign="middle" >58.56</td><td align="center" valign="middle" >7044038.23</td><td align="center" valign="middle" >3075565.18</td><td align="center" valign="middle" >43.66</td></tr><tr><td align="center" valign="middle" >72</td><td align="center" valign="middle" >0.112</td><td align="center" valign="middle" >124.03</td><td align="center" valign="middle" >60.96</td><td align="center" valign="middle" >7676571.78</td><td align="center" valign="middle" >3471565.18</td><td align="center" valign="middle" >45.22</td></tr><tr><td align="center" valign="middle" >78</td><td align="center" valign="middle" >0.111</td><td align="center" valign="middle" >129.10</td><td align="center" valign="middle" >63.26</td><td align="center" valign="middle" >8308693.21</td><td align="center" valign="middle" >3867565.18</td><td align="center" valign="middle" >46.55</td></tr><tr><td align="center" valign="middle" >84</td><td align="center" valign="middle" >0.110</td><td align="center" valign="middle" >133.97</td><td align="center" valign="middle" >65.47</td><td align="center" valign="middle" >8940480.57</td><td align="center" valign="middle" >4263565.18</td><td align="center" valign="middle" >47.69</td></tr></tbody></table></table-wrap><p>multilateral horizontal well is calculated. The radius of influence based on the front vertical well, and the horizontal section is 1500 m. The radius of influence are shown in <xref ref-type="table" rid="table6">Table 6</xref>, and the recovery curve is shown in <xref ref-type="fig" rid="fig5">Figure 5</xref>.</p></sec><sec id="s2_2_3"><title>2.2.3. Prediction Analysis</title><p>In the foregoing, the isothermal adsorption curve method and the hydraulic</p><table-wrap id="table6" ><label><xref ref-type="table" rid="table6">Table 6</xref></label><caption><title> Calculation results of recovery rate in multilateral horizontal well</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Time/m</th><th align="center" valign="middle" >Bottomhole pressure P<sub>w</sub>/MPa</th><th align="center" valign="middle" >Influence radius R<sub>e</sub>/m</th><th align="center" valign="middle" >Desorption radius r/m</th><th align="center" valign="middle" >Theoretical cumulative gas production Q<sub>L</sub>/m<sup>3</sup>・t<sup>−1</sup></th><th align="center" valign="middle" >Actual cumulative gas production Q<sub>S</sub>/m<sup>3</sup>・t<sup>−1</sup></th><th align="center" valign="middle" >Recovery rate η/%</th></tr></thead><tr><td align="center" valign="middle" >1</td><td align="center" valign="middle" >2.906</td><td align="center" valign="middle" >124.33</td><td align="center" valign="middle" >3.45</td><td align="center" valign="middle" >28201.15</td><td align="center" valign="middle" >0.00</td><td align="center" valign="middle" >0.00</td></tr><tr><td align="center" valign="middle" >6</td><td align="center" valign="middle" >2.305</td><td align="center" valign="middle" >198.23</td><td align="center" valign="middle" >42.47</td><td align="center" valign="middle" >1177436.25</td><td align="center" valign="middle" >0.00</td><td align="center" valign="middle" >0.00</td></tr><tr><td align="center" valign="middle" >12</td><td align="center" valign="middle" >1.524</td><td align="center" valign="middle" >238.72</td><td align="center" valign="middle" >88.90</td><td align="center" valign="middle" >8001914.60</td><td align="center" valign="middle" >1500.77</td><td align="center" valign="middle" >0.02</td></tr><tr><td align="center" valign="middle" >18</td><td align="center" valign="middle" >1.007</td><td align="center" valign="middle" >266.70</td><td align="center" valign="middle" >121.99</td><td align="center" valign="middle" >17811923.66</td><td align="center" valign="middle" >241334.18</td><td align="center" valign="middle" >1.35</td></tr><tr><td align="center" valign="middle" >24</td><td align="center" valign="middle" >0.666</td><td align="center" valign="middle" >288.84</td><td align="center" valign="middle" >145.91</td><td align="center" valign="middle" >27815843.73</td><td align="center" valign="middle" >1415691.28</td><td align="center" valign="middle" >5.09</td></tr><tr><td align="center" valign="middle" >30</td><td align="center" valign="middle" >0.440</td><td align="center" valign="middle" >307.49</td><td align="center" valign="middle" >163.89</td><td align="center" valign="middle" >36989249.73</td><td align="center" valign="middle" >3661554.51</td><td align="center" valign="middle" >9.90</td></tr><tr><td align="center" valign="middle" >36</td><td align="center" valign="middle" >0.291</td><td align="center" valign="middle" >323.79</td><td align="center" valign="middle" >141.93</td><td align="center" valign="middle" >45106632.79</td><td align="center" valign="middle" >6672425.60</td><td align="center" valign="middle" >14.79</td></tr><tr><td align="center" valign="middle" >42</td><td align="center" valign="middle" >0.192</td><td align="center" valign="middle" >338.37</td><td align="center" valign="middle" >150.94</td><td align="center" valign="middle" >52234816.44</td><td align="center" valign="middle" >10238308.40</td><td align="center" valign="middle" >19.60</td></tr><tr><td align="center" valign="middle" >48</td><td align="center" valign="middle" >0.127</td><td align="center" valign="middle" >351.64</td><td align="center" valign="middle" >158.48</td><td align="center" valign="middle" >58527918.45</td><td align="center" valign="middle" >14600518.40</td><td align="center" valign="middle" >24.95</td></tr><tr><td align="center" valign="middle" >54</td><td align="center" valign="middle" >0.084</td><td align="center" valign="middle" >363.86</td><td align="center" valign="middle" >164.97</td><td align="center" valign="middle" >64148329.28</td><td align="center" valign="middle" >19759055.60</td><td align="center" valign="middle" >30.80</td></tr><tr><td align="center" valign="middle" >60</td><td align="center" valign="middle" >0.056</td><td align="center" valign="middle" >375.23</td><td align="center" valign="middle" >170.67</td><td align="center" valign="middle" >69238930.34</td><td align="center" valign="middle" >25713920.00</td><td align="center" valign="middle" >37.14</td></tr><tr><td align="center" valign="middle" >66</td><td align="center" valign="middle" >0.037</td><td align="center" valign="middle" >385.89</td><td align="center" valign="middle" >175.77</td><td align="center" valign="middle" >73916137.79</td><td align="center" valign="middle" >32465111.60</td><td align="center" valign="middle" >43.92</td></tr><tr><td align="center" valign="middle" >72</td><td align="center" valign="middle" >0.024</td><td align="center" valign="middle" >395.93</td><td align="center" valign="middle" >180.43</td><td align="center" valign="middle" >78271072.6</td><td align="center" valign="middle" >40012630.40</td><td align="center" valign="middle" >51.12</td></tr><tr><td align="center" valign="middle" >78</td><td align="center" valign="middle" >0.016</td><td align="center" valign="middle" >405.46</td><td align="center" valign="middle" >184.72</td><td align="center" valign="middle" >82373453.24</td><td align="center" valign="middle" >48356476.40</td><td align="center" valign="middle" >58.70</td></tr><tr><td align="center" valign="middle" >84</td><td align="center" valign="middle" >0.011</td><td align="center" valign="middle" >414.53</td><td align="center" valign="middle" >188.72</td><td align="center" valign="middle" >86275944.36</td><td align="center" valign="middle" >57496649.60</td><td align="center" valign="middle" >66.64</td></tr></tbody></table></table-wrap><p>model method are adopted respectively for the recovery efficiency of vertical well. The isothermal adsorption curve method is based on the adsorption/de- sorption experiment to calculate recovery rate. The hydraulic model rule is based on the original production data and establishes the hydraulic model to calculate recovery rate. Compared with the two methods, the hydraulic model method is more practical.</p><p>According to the calculation results of different well types, compared the recovery rate and the comparison results are shown in <xref ref-type="table" rid="table7">Table 7</xref>. It can be found that the recovery rate of “V” type well is the largest in the early stage (3 years), followed by vertical well and “U” type well, and finally the multilateral horizontal well. After 5 years, the recovery rate of “V” type well is still the largest, followed by multilateral horizontal well and vertical well, and finally “U” type well. With the development of production, the recovery rate of multilateral horizontal well is greater than the other three kinds of wells finally.</p></sec></sec></sec><sec id="s3"><title>3. Analysis of Factors Affecting Recovery Rate</title><p>The factors affecting CBM recovery rate include geological characteristics, development conditions and economic factors [<xref ref-type="bibr" rid="scirp.80531-ref16">16</xref>] . The geological characteristics of coal reservoir are the main factors affecting CBM recovery rate, including coal rank, depth, adsorption characteristics, permeability and gas content [<xref ref-type="bibr" rid="scirp.80531-ref17">17</xref>] . The effect of gas content on recovery rate is due to the presence of waste pressure. When the waste pressure is determined, for coalbed with the same adsorption capacity, residual adsorption capacity is determined, so when the gas content is higher, the recovery rate of CBM is higher. When the adsorption capacity is different and the gas content is uniform, residual adsorption capacity is higher, the recovery rate of CBM is lower. The permeability is mainly rely on the changing nature of the coalbed to change the recovery rate, in the case of low permeability, desorption-diffusion-percolation can’t be formed in a large range, resulting in low gas production and the recovery rate is not up to the expected result. The influence factors of coal rank, depth and reservoir pressure affect the adsorption characteristics, permeability and other physical properties of coal under the combined action, and have a certain influence on recovery rate of CBM.</p><table-wrap id="table7" ><label><xref ref-type="table" rid="table7">Table 7</xref></label><caption><title> Contrast of recovery rate</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >CBM well type</th><th align="center" valign="middle" >Production time/y</th><th align="center" valign="middle" >Recovery rate/%</th></tr></thead><tr><td align="center" valign="middle"  rowspan="3"  >Vertical well</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >26.00</td></tr><tr><td align="center" valign="middle" >5</td><td align="center" valign="middle" >33.44</td></tr><tr><td align="center" valign="middle" >7</td><td align="center" valign="middle" >40.62</td></tr><tr><td align="center" valign="middle"  rowspan="3"  >“U” type well</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >17.96</td></tr><tr><td align="center" valign="middle" >5</td><td align="center" valign="middle" >27.19</td></tr><tr><td align="center" valign="middle" >7</td><td align="center" valign="middle" >34.92</td></tr><tr><td align="center" valign="middle"  rowspan="3"  >“V” type well</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >28.33</td></tr><tr><td align="center" valign="middle" >5</td><td align="center" valign="middle" >41.82</td></tr><tr><td align="center" valign="middle" >7</td><td align="center" valign="middle" >47.69</td></tr><tr><td align="center" valign="middle"  rowspan="3"  >Multilateral horizontal well</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >14.79</td></tr><tr><td align="center" valign="middle" >5</td><td align="center" valign="middle" >37.14</td></tr><tr><td align="center" valign="middle" >7</td><td align="center" valign="middle" >66.64</td></tr></tbody></table></table-wrap></sec><sec id="s4"><title>4. Measures for improving CBM Recovery Rate in Dafosi Mine Field</title><p>According to the factors affecting CBM recovery rate, the corresponding measures can be taken to improve recovery rate, mainly in permeability, adsorption capacity and development conditions [<xref ref-type="bibr" rid="scirp.80531-ref18">18</xref>] [<xref ref-type="bibr" rid="scirp.80531-ref19">19</xref>] [<xref ref-type="bibr" rid="scirp.80531-ref20">20</xref>] [<xref ref-type="bibr" rid="scirp.80531-ref21">21</xref>] .</p><p>CBM reservoir has the characteristics of low pressure, low permeability and low saturation. The gas exists mainly in the adsorbed state, and its output is a complex process of desorption-diffusion-percolation. China’s coalbed is low pressure and less saturated, which is the reason China’s CBM overall recovery rate is not large. Through artificial modification of physical properties of coal reservoir, recovery rate of CBM can be improved, and the main methods are hydraulic fracturing and gas injection production.</p><p>After hydraulic fracturing, coalbed interior will appear a plurality of extending far crack. In the process of drainage and depressurization, the range of pressure reduction can be increased, thus making it more desorption of CBM, increasing gas production of CBM well. Gas injection production technology mainly uses coal to adsorb CO<sub>2</sub> stronger, and displaces CH<sub>4</sub> in the void of coal matrix. By injecting CO<sub>2</sub> and other gas into coal reservoir and coal reservoir saturation will be increased, the desorption rate of CBM will be accelerated.</p><p>Drilling technology can also increase CBM recovery rate, mainly in multilateral horizontal well drilling technology. The resistance of fluid in horizontal well is relatively small, the branch hole and coalbed cleat intersect each other, so that the cleat and fracture of coalbed are more unblocked, and the desorption range of CBM is increased. The permeability of Dafosi mine field coal reservoir is good, the hardness of coalbed is large, and the discharge area of CBM well is large. During the development of multilateral horizontal well, the discharge area of each branch can be disturbed in a short time, so that CBM between the branches can be fully desorbed and migrated to the wellbore.</p></sec><sec id="s5"><title>5. Conclusions</title><p>1) In the isothermal adsorption method, the desorption hysteresis is well solved by the desorption formula, and the calculated recovery rate is lower than that calculated by Langmuir equation, which is in line with the actual situation. The recovery rate of “V” type well is the biggest in the early stage of hydraulic model, but with the development of production, the recovery rate of multilateral horizontal well is greater than the other three kinds of wells finally.</p><p>2) The factors affecting CBM recovery rate include geological characteristics, development conditions and economic factors. The geological characteristics of coal reservoir are the main factors affecting CBM recovery rate, including coal rank, depth, adsorption characteristics, permeability and gas content.</p><p>3) Through the hydraulic fracturing and gas injection production, the physical properties of coal reservoir can be improved to improve recovery rate, and drilling technology, such as multilateral horizontal well drilling technology, can be used to improve recovery rate of CBM.</p></sec><sec id="s6"><title>Cite this paper</title><p>Ma, D.M., Zhang, C.Y., Wang, C.T. and Tang, X.Y. (2017) Prediction of Coal Bed Methane Recovery Rate and Its Improvement Measures in Dafosi Mine Field. Journal of Power and Energy Engineering, 5, 37-49. https://doi.org/10.4236/jpee.2017.511004</p></sec></body><back><ref-list><title>References</title><ref id="scirp.80531-ref1"><label>1</label><mixed-citation publication-type="other" xlink:type="simple">Ye, J.P. and Lu, X.X. (2016) Development Status and Technical Progress of China Coalbed Methane Industry. Coal Science and Technology, 44, 24-28.</mixed-citation></ref><ref id="scirp.80531-ref2"><label>2</label><mixed-citation publication-type="other" xlink:type="simple">Huang, S.C., Liu, W.G. and Zhao, G.Q. (2009) Coalbed Methane Development and Utilization in China: Status and Future Development. China Coal, 35, 5-10.</mixed-citation></ref><ref id="scirp.80531-ref3"><label>3</label><mixed-citation publication-type="other" xlink:type="simple">Zhao, J., Zhang, S.A., Zhan, F.W., et al. (2012) Numerical Simulation Study on Carbon Dioxide Injection to Enhance CBM Recovery. Natural Gas and Oil, 30, 67-70.</mixed-citation></ref><ref id="scirp.80531-ref4"><label>4</label><mixed-citation publication-type="other" xlink:type="simple">Shen, J., Qin, Y., Zhang, C.J., et al. (2016) Feasibility of Enhanced Coalbed Methane Recovery by CO2 Sequestration into Deep Coalbed of Qinshui Basin. Journal of China Coal Society, 41, 156-161.</mixed-citation></ref><ref id="scirp.80531-ref5"><label>5</label><mixed-citation publication-type="other" xlink:type="simple">Zheng, Y.Z. and Han, B.S. (2005) Affecting Factors and Estimating Methods of Recovery Percent of Coalbed Gas. Natural Gas Industry, 25, 120-123.</mixed-citation></ref><ref id="scirp.80531-ref6"><label>6</label><mixed-citation publication-type="other" xlink:type="simple">Ma, D.M. (2008) Research on the Adsorption and Desorption Mechanism of Coalbed Methane. Xi’an University of Science and Technology, Xi’an.</mixed-citation></ref><ref id="scirp.80531-ref7"><label>7</label><mixed-citation publication-type="other" xlink:type="simple">Qiao, J.W. (2009) Research on the Low Rank Coal of Pore Characteristics and Desorption Laws. Xi’an University of Science and Technology, Xi’an.</mixed-citation></ref><ref id="scirp.80531-ref8"><label>8</label><mixed-citation publication-type="other" xlink:type="simple">Zhang, P.H., Li, G.H. and Li, J.W. (2006) The Review on the Predictive Methodology of Coalbed Methane Recovery Efficiency. Coal Geology &amp; Exploration, 34, 26-30.</mixed-citation></ref><ref id="scirp.80531-ref9"><label>9</label><mixed-citation publication-type="other" xlink:type="simple">Zhou, S.Z. and Zhang, W.Z. (2011) The Current Methods for Estimating Recovery Rate of CBM and the Existing Problems in China. China Coalbed Methane, 8, 9-12.</mixed-citation></ref><ref id="scirp.80531-ref10"><label>10</label><mixed-citation publication-type="other" xlink:type="simple">Liu, S.G., Yuan, W.F., Zhang, X.L., et al. (2013) The Production Curve and Recovery Rate of Coalbed Methane Well in Panzhuang Block. Journal of China Coal Society, 38, 164-167.</mixed-citation></ref><ref id="scirp.80531-ref11"><label>11</label><mixed-citation publication-type="other" xlink:type="simple">Liu, C.J. and Tan, X. (2009) Study on the CBM Recovery Rate in Tiefa Coal Basin. Chinese Journal of Coal, 35, 5-8.</mixed-citation></ref><ref id="scirp.80531-ref12"><label>12</label><mixed-citation publication-type="other" xlink:type="simple">Busch, A., Genst Erblum, Y. and Kross, B.M. (2003) Methaneand CO2 Sorption and Desorption Measurements on Dry Argonnepremium Coals: Pure Components and Mixture. International Journal of Coal Geology, 55, 205-224. https://doi.org/10.1016/S0166-5162(03)00113-7</mixed-citation></ref><ref id="scirp.80531-ref13"><label>13</label><mixed-citation publication-type="other" xlink:type="simple">Parityum, H. (1993) Study of Coal Sorption Isotherms Using a Multicomponents Gas Mixture. Proceedings of the 1993 International Coal Methane Symposium, Birmingham, 151-160.</mixed-citation></ref><ref id="scirp.80531-ref14"><label>14</label><mixed-citation publication-type="other" xlink:type="simple">Greaveskh and Owenlb, M. (1993) Multicomponent Gas Adsorption-Desorption Behavior of Coal. Proceedings of the 1993 International Coalbed Methane Symposium, 197-205.</mixed-citation></ref><ref id="scirp.80531-ref15"><label>15</label><mixed-citation publication-type="other" xlink:type="simple">Ma, D.M., Zhang, S.A. and Lin, Y.B. (2011) Isothermal Adsorption and Desorption Experiment of Coal and Experimental Results Accuracy Fitting. Journal of China Coal Society, 36, 477-480.</mixed-citation></ref><ref id="scirp.80531-ref16"><label>16</label><mixed-citation publication-type="other" xlink:type="simple">Wu, X.P. and Zhang, Q. (2014) Study on Influence of Development Mode and Stimulation Technique on the Recovery of Coalbed Methane. China Coalbed Methane, 11, 20-24.</mixed-citation></ref><ref id="scirp.80531-ref17"><label>17</label><mixed-citation publication-type="other" xlink:type="simple">Xu, L.J. and Xian, X.F. (2005) Study on Status of CBM Reserves and Improvement of CMM Recovery. China Coalbed Methane, 2, 19-22.</mixed-citation></ref><ref id="scirp.80531-ref18"><label>18</label><mixed-citation publication-type="other" xlink:type="simple">Rao, M.Y., Zhang, S.A. and Shang, C.S. (2007) Analysis on Key Techniques to Improve CBM Recovery in China. China Coalbed Methane, 4, 12-16.</mixed-citation></ref><ref id="scirp.80531-ref19"><label>19</label><mixed-citation publication-type="other" xlink:type="simple">Xu, C.H., Zhao, G.J., Long, S.X., et al. (2010) Analysis on New Technologies to Enhance CBM Recovery. China Petroleum Exploration, 3, 51-54.</mixed-citation></ref><ref id="scirp.80531-ref20"><label>20</label><mixed-citation publication-type="other" xlink:type="simple">Zhang, C.J., Shen, J., Qin, Y., et al. (2016) Technology of CO2 Injection Affected to Improve Coalbed Methane Recovery and CO2 Sealed Storage. Coal Science and Technology, 44, 205-210.</mixed-citation></ref><ref id="scirp.80531-ref21"><label>21</label><mixed-citation publication-type="other" xlink:type="simple">Xu, X. and Liang, M. (2016) Method of Improving CBM Recovery Rate and Technologies Research Progress. China Coalbed Methane, 13, 3-6.</mixed-citation></ref></ref-list></back></article>