<?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">OJOGas</journal-id><journal-title-group><journal-title>Open Journal of Yangtze Oil and Gas</journal-title></journal-title-group><issn pub-type="epub">2473-1889</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/ojogas.2021.61001</article-id><article-id pub-id-type="publisher-id">OJOGas-106035</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>
 
 
  Study on the Plugging System of the Lower Ancient High Loss Zone in Changqing Gas Field
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Yan</surname><given-names>Gao</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>Zuwen</surname><given-names>Wang</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>Xiuli</surname><given-names>Shao</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Dichen</surname><given-names>Tan</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>Erping</surname><given-names>Liu</given-names></name><xref ref-type="aff" rid="aff3"><sup>3</sup></xref></contrib></contrib-group><aff id="aff2"><addr-line>Yangtze University, Jingzhou, China</addr-line></aff><aff id="aff1"><addr-line>Chuanqing Drilling Engineering Company Underground Operation Company, Xi’an, China</addr-line></aff><aff id="aff3"><addr-line>Liaohe Oil Safety and Environment Protection Technical Supervision Center, Panjin, China</addr-line></aff><pub-date pub-type="epub"><day>22</day><month>12</month><year>2020</year></pub-date><volume>06</volume><issue>01</issue><fpage>1</fpage><lpage>12</lpage><history><date date-type="received"><day>19,</day>	<month>October</month>	<year>2020</year></date><date date-type="rev-recd"><day>20,</day>	<month>December</month>	<year>2020</year>	</date><date date-type="accepted"><day>23,</day>	<month>December</month>	<year>2020</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>
 
 
  At present, in the workover operations of old gas wells in the Changqing Gas Field, due to years of exploitation in the production layer, pressure deficits, and general leakage during the well killing, the well must be plugged before the well can be killed. In particular, the fracture-cavity type fractures of the lower paleocarbonate reservoirs have serious leakage. Traditional plugging materials and traditional plugging materials and methods have some limitations in dealing with leakage problems. Therefore, a composite plugging system using polymer solution as the base carrier fluid, multi-particle size rigid particles, expandable particles and modified fibers is developed. Its formula is: water + 2% polyacrylamide + 0.1% N, N-methylene bisacrylamide polymer gel is the base carrier fluid; the formulation of the particle plugging agent was continuously optimized through the CDL-II high temperature and high pressure dynamic and static plugging ability to plug the core. The final formulation of the plugging agent is: 1) 20% rigid particles (5 mm, 1 mm, 0.5 mm CCP-3 ratio 4:2:1) + 1% 3 mm expanded particles SMK-1 + 1% 1 - 2 mm fiber SRXW-10; 2) 20% rigid particles (3 mm, 0.1 mm, 0.05 mm CCP-3 ratio 3:2:1) + 1% 3 mm expanded particles SMK-1 + 1% 1 - 2 mm fiber SRXW-10. The water swelling multiples of the granular plugging agent in salt water are all above 7 times, which meets the requirements of leak-proof plugging operations under high salinity; 3% HCl is selected as the gel breaker, and the plugging system has a gel breaking rate of 95%; through the water plugging and profile control experimental system, the sand-filled pipe is used to simulate the plugging effect under high temperature and high pressure, and the plugging system can be sealed for 5 days at a high temperature of 110&#176;C and a high pressure of 20 MPa to achieve a good plugging of the formation. It is expected that the developed plugging system has a good application prospect in future workover operations.
 
</p></abstract><kwd-group><kwd>Lower Ancient High Loss Layer</kwd><kwd> Plugging Gel</kwd><kwd> Particle Plugging Agent</kwd><kwd> Gel Breaking Performance</kwd><kwd> Plugging Performance</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>The Changqing Gas Field is a typical gas field with “low permeability, low pressure and low abundance”. After long-term mining, the formation pressure coefficient dropped to about 0.5 [<xref ref-type="bibr" rid="scirp.106035-ref1">1</xref>] [<xref ref-type="bibr" rid="scirp.106035-ref2">2</xref>] [<xref ref-type="bibr" rid="scirp.106035-ref3">3</xref>]. In order for the oil and gas wells in the Changqing block to resume normal production, it is necessary to restore the formation force coefficient through workover operations. At present, in workover operations, due to years of mining, pressure deficits, and common losses during well killing, the well must be plugged before killing, especially the fractures of the lower paleocarbonate reservoir, where the leakage is more serious [<xref ref-type="bibr" rid="scirp.106035-ref4">4</xref>] [<xref ref-type="bibr" rid="scirp.106035-ref5">5</xref>] [<xref ref-type="bibr" rid="scirp.106035-ref6">6</xref>]. In the process of workover operations, traditional plugging materials and methods are prone to poor plugging effect, repeated leakage or flowback difficulties when dealing with leakage problems, and plugging the pay zone, affecting productivity after workover, etc. [<xref ref-type="bibr" rid="scirp.106035-ref7">7</xref>]. This research relies on the Yangtze University Oilfield Chemistry Laboratory and project team members to develop a composite plugging system that uses polymer solutions, multi-particle size temporary plugging particles, and modified fibers to realize the effective plugging of perforation holes.</p></sec><sec id="s2"><title>2. Development of Plugging Gel</title><p>The polymer commonly used in oil fields is polyacrylamide, which can be cross-linked with inorganic or organic cross-linking agents [<xref ref-type="bibr" rid="scirp.106035-ref8">8</xref>]. Common inorganic crosslinking agents have poor temperature resistance and cannot withstand the high temperature and high pressure environment of the formation, so organic crosslinking agents are selected for crosslinking. This article selects polyacrylamide (concentration of 2%); cross-linking agents are polyamine organics (called MTA), N,N-methylenebisacrylamide (BIS) and phenol, all at a concentration of 0.1%. To evaluate the gelation of the crosslinking agent at 120˚C, a high-temperature roller heating furnace is used, which only heats and does not roll, which can better simulate the underground plugging process [<xref ref-type="bibr" rid="scirp.106035-ref9">9</xref>]. The gelation status of the crosslinking agent at 120˚C is evaluated, as shown in <xref ref-type="table" rid="table1">Table 1</xref>.</p><p>It can be seen from <xref ref-type="table" rid="table1">Table 1</xref> that polyacrylamide can be gelled in the case of three crosslinking agents. Because phenol pollutes the environment, and the pumpability of MTA is a bit worse than that of BIS as a crosslinking agent, it is finally determined that water + polyacrylamide HPAM + BIS (N, N-methylene) Bisacrylamide) system.</p><table-wrap id="table1" ><label><xref ref-type="table" rid="table1">Table 1</xref></label><caption><title> Gelation status of polyacrylamide and crosslinking agent</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Crosslinking agent</th><th align="center" valign="middle" >Gel forming</th><th align="center" valign="middle" >Pumpable</th></tr></thead><tr><td align="center" valign="middle" >Phenol</td><td align="center" valign="middle" >Gelled</td><td align="center" valign="middle" >Easy</td></tr><tr><td align="center" valign="middle" >Phenol</td><td align="center" valign="middle" >Gelled</td><td align="center" valign="middle" >Easy</td></tr><tr><td align="center" valign="middle" >MTA</td><td align="center" valign="middle" >Gelled</td><td align="center" valign="middle" >Harder</td></tr><tr><td align="center" valign="middle" >MTA</td><td align="center" valign="middle" >Gelled</td><td align="center" valign="middle" >Harder</td></tr><tr><td align="center" valign="middle" >BIS</td><td align="center" valign="middle" >Gelled</td><td align="center" valign="middle" >Easy</td></tr><tr><td align="center" valign="middle" >BIS</td><td align="center" valign="middle" >Gelled</td><td align="center" valign="middle" >Easy</td></tr></tbody></table></table-wrap>Determination of Plugging Gel Formulation<p>The system formula is initially set as 2% polyacrylamide + 0.1% BIS, and the experimental temperature was 100˚C - 120˚C. Use single factor analysis to determine the optimal increase.</p><p>1) Determination of polyacrylamide concentration</p><p>The concentration of polyacrylamide is 1.5%, 2%, 2.5%, the concentration of BIS is 0.1%, the experimental temperature is 100˚C - 120˚C, and the gel formation is shown in <xref ref-type="table" rid="table2">Table 2</xref>.</p><table-wrap id="table2" ><label><xref ref-type="table" rid="table2">Table 2</xref></label><caption><title> The effect of different concentrations of polyacrylamide on gel formation</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Concentration</th><th align="center" valign="middle"  colspan="3"  >Gel time (h)</th><th align="center" valign="middle"  rowspan="2"  >Initial viscosity (mPa∙s)</th></tr></thead><tr><td align="center" valign="middle" >100˚C</td><td align="center" valign="middle" >110˚C</td><td align="center" valign="middle" >120˚C</td></tr><tr><td align="center" valign="middle" >1.5%</td><td align="center" valign="middle" >6</td><td align="center" valign="middle" >4</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >3000</td></tr><tr><td align="center" valign="middle" >2.0%</td><td align="center" valign="middle" >4</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >5500</td></tr><tr><td align="center" valign="middle" >2.5%</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >1</td><td align="center" valign="middle" >8850</td></tr></tbody></table></table-wrap><p><xref ref-type="fig" rid="fig1">Figure 1</xref> shows the gelation of different concentrations of polyacrylamide at 100˚C. Comprehensive <xref ref-type="table" rid="table2">Table 2</xref> and <xref ref-type="fig" rid="fig1">Figure 1</xref> show that the viscosity and elasticity of 1.5% are much worse than that of 2% and 2.5%, and the gel time is longer., The blocking ability is poor; the performance difference between 2% and 2.5% is not much, but the initial viscosity when the concentration reaches 2.5% is 8550 mPa∙s, and the initial pumpability is too poor, so the initial pumpability and gel time are integrated And the elasticity after gelation, confirm that the polyacrylamide concentration is 2%.</p><p>2) Determination of BIS concentration</p><p>The concentration of BIS is 0.05%, 0.1%, 0.15%, the concentration of polyacrylamide is 2%, the experiment temperature is 100˚C - 120˚C, and the gel formation is shown in <xref ref-type="table" rid="table3">Table 3</xref>.</p><table-wrap id="table3" ><label><xref ref-type="table" rid="table3">Table 3</xref></label><caption><title> Gelation data of different concentrations of BIS</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Concentration</th><th align="center" valign="middle"  colspan="3"  >Gel time(h)</th><th align="center" valign="middle"  rowspan="2"  >Initial viscosity (mPa∙s)</th></tr></thead><tr><td align="center" valign="middle" >100˚C</td><td align="center" valign="middle" >110˚C</td><td align="center" valign="middle" >120˚C</td></tr><tr><td align="center" valign="middle" >0.05%</td><td align="center" valign="middle" >5</td><td align="center" valign="middle" >4</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >5780</td></tr><tr><td align="center" valign="middle" >0.10%</td><td align="center" valign="middle" >4</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >5500</td></tr><tr><td align="center" valign="middle" >0.15%</td><td align="center" valign="middle" >3</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >1</td><td align="center" valign="middle" >5650</td></tr></tbody></table></table-wrap><p>From <xref ref-type="table" rid="table3">Table 3</xref> data and observation of <xref ref-type="fig" rid="fig2">Figure 2</xref> it can be seen that the 0.05% concentration of BIS has a long time to gel, and the strength after gelation is low, and the blocking ability is poor; although the 0.15% concentration of BIS has less gel time, but due to excessive Cross-linking has poor stability. Therefore, combining the stability of gel formation, gel time and strength after gel formation, the concentration of BIS is determined to be 0.1%.</p><p>Through the above experimental research, it is finally determined that the final formulation of the plugging gel is water + 2% polyacrylamide + 0.1% BIS. The test temperature range of the plugging gel is 100˚C ~ 120˚C and the stability of the gel can still be maintained, so the temperature resistance of the system is ≥100˚C.</p></sec><sec id="s3"><title>3. Determination of Particle Plugging Agent</title><p>The experimental instrument is a CDL-II high temperature and high pressure dynamic and static plugging experimental device. Through the indoor artificial core (12 mm aperture), the advection pump uses a flow rate of 5 - 10 mL/min to displace the plugging system with plugging agent to make it pass For man-made fractured cores, the pressure is maintained for 10 minutes, the filter loss is less than 20 ml as the standard, and the experimental temperature is 110˚C. The formulation of the granular plugging agent is continuously optimized through the plugging ability of the core [<xref ref-type="bibr" rid="scirp.106035-ref10">10</xref>].</p><sec id="s3_1"><title>3.1. Determination of Rigid Particle Plugging Agent</title><sec id="s3_1_1"><title>3.1.1. Determination of Particle Size Gradation</title><p>CCP-3 is a rigid particle plugging agent, using 3 kinds of particle combinations, with 5 mm particles as the main body and 3 mm particles as the main body respectively, and the other two suitable particle size gradations are preferred. After investigation, the following combinations of particles were made.</p><p>1) Take 5 mm particles as the main body:</p><p>a) 5 mm + 2 mm + 1 mm; b) 5 mm + 2 mm + 0.5 mm; c) 5 mm + 1 mm + 0.5 mm;</p><p>2) With 3 mm particles as the main body:</p><p>a) 3 mm + 0.5 mm + 0.1 mm; b) 3 mm + 0.5 mm + 0.05 mm; c) 3 mm + 0.1 mm + 0.05 mm</p><p>The ratio of the three particles in the two formulations is 2:1:1, the particle concentration is 10%, and the plugging gel is used as the base carrier liquid to investigate the pressure resistance and plugging performance of the plugging agent with different particle size gradations. In order to determine the optimal particle size gradation, the experimental results are shown in <xref ref-type="table" rid="table4">Table 4</xref> and <xref ref-type="table" rid="table5">Table 5</xref>.</p><table-wrap id="table4" ><label><xref ref-type="table" rid="table4">Table 4</xref></label><caption><title> Evaluation of the plugging performance of CCP-3 with 5 mm particles as the main body in different particle size gradations</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Displacement pressure (MPa)</th><th align="center" valign="middle"  colspan="3"  >Different particle size gradation</th></tr></thead><tr><td align="center" valign="middle" >(1)</td><td align="center" valign="middle" >(2)</td><td align="center" valign="middle" >(3)</td></tr><tr><td align="center" valign="middle" >1.5</td><td align="center" valign="middle" >11 mL</td><td align="center" valign="middle" >10 mL</td><td align="center" valign="middle" >8 mL</td></tr><tr><td align="center" valign="middle" >3.0</td><td align="center" valign="middle" >12 mL</td><td align="center" valign="middle" >11 mL</td><td align="center" valign="middle" >9 mL</td></tr><tr><td align="center" valign="middle" >5.0</td><td align="center" valign="middle" >14 mL</td><td align="center" valign="middle" >13 mL</td><td align="center" valign="middle" >10 mL</td></tr><tr><td align="center" valign="middle" >7.5</td><td align="center" valign="middle" >16 mL</td><td align="center" valign="middle" >15 mL</td><td align="center" valign="middle" >12 mL</td></tr><tr><td align="center" valign="middle" >10.0</td><td align="center" valign="middle" >18 mL</td><td align="center" valign="middle" >16 mL</td><td align="center" valign="middle" >13 mL</td></tr><tr><td align="center" valign="middle" >12.0</td><td align="center" valign="middle" >27 mL</td><td align="center" valign="middle" >25 mL</td><td align="center" valign="middle" >20 mL</td></tr></tbody></table></table-wrap><table-wrap id="table5" ><label><xref ref-type="table" rid="table5">Table 5</xref></label><caption><title> Evaluation of the plugging performance of CCP-3 with 3 mm particles as the main body in different particle size gradations</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Displacement pressure (MPa)</th><th align="center" valign="middle"  colspan="3"  >Different particle size gradation</th></tr></thead><tr><td align="center" valign="middle" >(1)</td><td align="center" valign="middle" >(2)</td><td align="center" valign="middle" >(3)</td></tr><tr><td align="center" valign="middle" >1.5</td><td align="center" valign="middle" >12 mL</td><td align="center" valign="middle" >11 mL</td><td align="center" valign="middle" >9 mL</td></tr><tr><td align="center" valign="middle" >3.0</td><td align="center" valign="middle" >13 mL</td><td align="center" valign="middle" >12 mL</td><td align="center" valign="middle" >10 mL</td></tr><tr><td align="center" valign="middle" >5.0</td><td align="center" valign="middle" >14 mL</td><td align="center" valign="middle" >13 mL</td><td align="center" valign="middle" >11 mL</td></tr><tr><td align="center" valign="middle" >7.5</td><td align="center" valign="middle" >17 mL</td><td align="center" valign="middle" >15 mL</td><td align="center" valign="middle" >13 mL</td></tr><tr><td align="center" valign="middle" >10.0</td><td align="center" valign="middle" >18 mL</td><td align="center" valign="middle" >17 mL</td><td align="center" valign="middle" >15 mL</td></tr><tr><td align="center" valign="middle" >12.0</td><td align="center" valign="middle" >26 mL</td><td align="center" valign="middle" >25 mL</td><td align="center" valign="middle" >21 mL</td></tr></tbody></table></table-wrap><p>According to <xref ref-type="table" rid="table4">Table 4</xref> and <xref ref-type="table" rid="table5">Table 5</xref>, the optimal particle size combination with 5 mm particles as the main body is determined, which is 5 mm + 1 mm + 0.5 mm; the optimal particle size combination with 3 mm particles as the main body, is 3 mm + 0.1 mm + 0.05 mm, which can withstand a pressure of 10 MPa.</p></sec><sec id="s3_1_2"><title>3.1.2. Determination of the Ratio of Large and Small Particles</title><p>Add 10% of the particle plugging agent to the plugging gel to investigate the compression resistance and plugging performance of the particles in different proportions. The experimental results are shown in <xref ref-type="table" rid="table6">Table 6</xref> and <xref ref-type="table" rid="table7">Table 7</xref>.</p><table-wrap id="table6" ><label><xref ref-type="table" rid="table6">Table 6</xref></label><caption><title> Evaluation of the plugging performance of CCP-3 with 5 mm particles as the main body under different proportions</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Displacement pressure (MPa)</th><th align="center" valign="middle"  colspan="4"  >The ratio of three kinds of particles</th></tr></thead><tr><td align="center" valign="middle" >4:1:1</td><td align="center" valign="middle" >4:1:2</td><td align="center" valign="middle" >4:2:1</td><td align="center" valign="middle" >2:1:1</td></tr><tr><td align="center" valign="middle" >1.5</td><td align="center" valign="middle" >10 mL</td><td align="center" valign="middle" >9 mL</td><td align="center" valign="middle" >8 mL</td><td align="center" valign="middle" >9 mL</td></tr><tr><td align="center" valign="middle" >3.0</td><td align="center" valign="middle" >11 mL</td><td align="center" valign="middle" >10 mL</td><td align="center" valign="middle" >8 mL</td><td align="center" valign="middle" >9 mL</td></tr><tr><td align="center" valign="middle" >5.0</td><td align="center" valign="middle" >13 mL</td><td align="center" valign="middle" >12 mL</td><td align="center" valign="middle" >9 mL</td><td align="center" valign="middle" >10 mL</td></tr><tr><td align="center" valign="middle" >7.5</td><td align="center" valign="middle" >15 mL</td><td align="center" valign="middle" >14 mL</td><td align="center" valign="middle" >9 mL</td><td align="center" valign="middle" >11 mL</td></tr><tr><td align="center" valign="middle" >10.0</td><td align="center" valign="middle" >16 mL</td><td align="center" valign="middle" >17 mL</td><td align="center" valign="middle" >12 mL</td><td align="center" valign="middle" >13.5 mL</td></tr><tr><td align="center" valign="middle" >12.5</td><td align="center" valign="middle" >25 mL</td><td align="center" valign="middle" >23 mL</td><td align="center" valign="middle" >21 mL</td><td align="center" valign="middle" >22 mL</td></tr></tbody></table></table-wrap><table-wrap id="table7" ><label><xref ref-type="table" rid="table7">Table 7</xref></label><caption><title> Plugging performance evaluation of CCP-3 with 3mm particles as the main body under different ratios</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Displacement pressure (MPa)</th><th align="center" valign="middle"  colspan="4"  >The ratio of three kinds of particles</th></tr></thead><tr><td align="center" valign="middle" >3:1:1</td><td align="center" valign="middle" >3:1:2</td><td align="center" valign="middle" >3:2:1</td><td align="center" valign="middle" >3:2:2</td></tr><tr><td align="center" valign="middle" >1.5</td><td align="center" valign="middle" >10 mL</td><td align="center" valign="middle" >8 mL</td><td align="center" valign="middle" >7 mL</td><td align="center" valign="middle" >9.5 mL</td></tr><tr><td align="center" valign="middle" >3.0</td><td align="center" valign="middle" >12 mL</td><td align="center" valign="middle" >11 mL</td><td align="center" valign="middle" >9 mL</td><td align="center" valign="middle" >12 mL</td></tr><tr><td align="center" valign="middle" >5.0</td><td align="center" valign="middle" >13 mL</td><td align="center" valign="middle" >12 mL</td><td align="center" valign="middle" >11 mL</td><td align="center" valign="middle" >12.5 mL</td></tr><tr><td align="center" valign="middle" >7.5</td><td align="center" valign="middle" >15 mL</td><td align="center" valign="middle" >14 mL</td><td align="center" valign="middle" >12 mL</td><td align="center" valign="middle" >14 mL</td></tr><tr><td align="center" valign="middle" >10.0</td><td align="center" valign="middle" >17 mL</td><td align="center" valign="middle" >15 mL</td><td align="center" valign="middle" >14 mL</td><td align="center" valign="middle" >16 mL</td></tr><tr><td align="center" valign="middle" >12.5</td><td align="center" valign="middle" >24 mL</td><td align="center" valign="middle" >21 mL</td><td align="center" valign="middle" >20 mL</td><td align="center" valign="middle" >22 mL</td></tr></tbody></table></table-wrap><p>According to <xref ref-type="table" rid="table6">Table 6</xref> and <xref ref-type="table" rid="table7">Table 7</xref>, the optimal particle size ratio with 5 mm particles as the main body is determined, which is 4:2:1; the optimal particle size ratio with 3 mm particles as the main body, is 3:2:1, which can bear Pressure of 10 MPa.</p></sec><sec id="s3_1_3"><title>3.1.3. Determination of the Concentration of Rigid Particles</title><p>According to the above ratio, the plugging performance of different dosages under the two formulas was evaluated. The plugging experiment data are as follows:</p><p>According to <xref ref-type="table" rid="table8">Table 8</xref> and <xref ref-type="table" rid="table9">Table 9</xref>, the optimal dosage of the two formulations is 20%, and the pressure can reach 10.0 MPa, and there is no obvious leakage.</p><table-wrap id="table8" ><label><xref ref-type="table" rid="table8">Table 8</xref></label><caption><title> The plugging effect of CCP-3 with 5 mm particles as the main body under different dosages</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Displacement pressure (MPa)</th><th align="center" valign="middle"  colspan="3"  >CCP-3 for large and small particles</th></tr></thead><tr><td align="center" valign="middle" >10%</td><td align="center" valign="middle" >20%</td><td align="center" valign="middle" >30%</td></tr><tr><td align="center" valign="middle" >1.5</td><td align="center" valign="middle" >8 mL</td><td align="center" valign="middle" >7 mL</td><td align="center" valign="middle" >8 mL</td></tr><tr><td align="center" valign="middle" >3.0</td><td align="center" valign="middle" >9 mL</td><td align="center" valign="middle" >7 mL</td><td align="center" valign="middle" >9 mL</td></tr><tr><td align="center" valign="middle" >5.0</td><td align="center" valign="middle" >11 mL</td><td align="center" valign="middle" >7.5 mL</td><td align="center" valign="middle" >10 mL</td></tr><tr><td align="center" valign="middle" >7.5</td><td align="center" valign="middle" >14 mL</td><td align="center" valign="middle" >9 mL</td><td align="center" valign="middle" >13 mL</td></tr><tr><td align="center" valign="middle" >10.0</td><td align="center" valign="middle" >15.5 mL</td><td align="center" valign="middle" >10 mL</td><td align="center" valign="middle" >15 mL</td></tr><tr><td align="center" valign="middle" >12.0</td><td align="center" valign="middle" >28 mL</td><td align="center" valign="middle" >24 mL</td><td align="center" valign="middle" >30 mL</td></tr></tbody></table></table-wrap><table-wrap id="table9" ><label><xref ref-type="table" rid="table9">Table 9</xref></label><caption><title> The plugging effect of CCP-3 with 3 mm particles as the main body under different dosages</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Displacement pressure (MPa)</th><th align="center" valign="middle"  colspan="3"  >CCP-3 for large and small particles</th></tr></thead><tr><td align="center" valign="middle" >10%</td><td align="center" valign="middle" >20%</td><td align="center" valign="middle" >30%</td></tr><tr><td align="center" valign="middle" >1.5</td><td align="center" valign="middle" >8.5 mL</td><td align="center" valign="middle" >7 mL</td><td align="center" valign="middle" >8 mL</td></tr><tr><td align="center" valign="middle" >3.0</td><td align="center" valign="middle" >9 mL</td><td align="center" valign="middle" >8 mL</td><td align="center" valign="middle" >9 mL</td></tr><tr><td align="center" valign="middle" >5.0</td><td align="center" valign="middle" >10 mL</td><td align="center" valign="middle" >9 mL</td><td align="center" valign="middle" >10 mL</td></tr><tr><td align="center" valign="middle" >7.5</td><td align="center" valign="middle" >11.5 mL</td><td align="center" valign="middle" >11 mL</td><td align="center" valign="middle" >13 mL</td></tr><tr><td align="center" valign="middle" >10.0</td><td align="center" valign="middle" >13 mL</td><td align="center" valign="middle" >12 mL</td><td align="center" valign="middle" >17 mL</td></tr><tr><td align="center" valign="middle" >12.0</td><td align="center" valign="middle" >27 mL</td><td align="center" valign="middle" >24 mL</td><td align="center" valign="middle" >31 mL</td></tr></tbody></table></table-wrap></sec></sec><sec id="s3_2"><title>3.2. Determination of Expandable Particles</title>Optimization of Expandable Particles<p>Adopt BGRL-2 roller heating furnace, the base slurry is plugging gel, add 3% expandable particles, heat roll at 110˚C for 16 hours, observe the change of expandable particles at 110˚C [<xref ref-type="bibr" rid="scirp.106035-ref11">11</xref>]. The evaluation results are shown in <xref ref-type="table" rid="table1">Table 1</xref>0:</p><table-wrap id="table10" ><label><xref ref-type="table" rid="table1">Table 1</xref>0</label><caption><title> Evaluation of temperature resistance of different expansive particles</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Material name</th><th align="center" valign="middle" >110˚C</th></tr></thead><tr><td align="center" valign="middle" >SJ-6</td><td align="center" valign="middle" >Discoloration in appearance</td></tr><tr><td align="center" valign="middle" >GLP-1</td><td align="center" valign="middle" >The appearance is slightly discolored</td></tr><tr><td align="center" valign="middle" >LPC-4</td><td align="center" valign="middle" >Discoloration in appearance</td></tr><tr><td align="center" valign="middle" >SMK-1</td><td align="center" valign="middle" >No obvious change in appearance</td></tr></tbody></table></table-wrap><p>According to <xref ref-type="table" rid="table1">Table 1</xref>0, except for SMK-1, the appearance of other materials has changed more or less. Therefore, 3 mm SMK-1 is selected as the swelling particles to play a plugging role in the plugging process.</p><p>The 3 mm SMK-1 was selected, combined with the above-mentioned ratio and concentration of the granular plugging agent, and the plugging experimental data for investigating the plugging and compressive performance are as follows:</p><table-wrap id="table11" ><label><xref ref-type="table" rid="table1">Table 1</xref>1</label><caption><title> The blocking effect of CCP-3 with 5 mm particles as the main body at different SMK-1 concentrations</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Displacement pressure (MPa)</th><th align="center" valign="middle"  colspan="3"  >SMK-1 dosage</th></tr></thead><tr><td align="center" valign="middle" >0.5%</td><td align="center" valign="middle" >1%</td><td align="center" valign="middle" >1.5%</td></tr><tr><td align="center" valign="middle" >1.5</td><td align="center" valign="middle" >7 mL</td><td align="center" valign="middle" >6 mL</td><td align="center" valign="middle" >8 mL</td></tr><tr><td align="center" valign="middle" >3.0</td><td align="center" valign="middle" >8 mL</td><td align="center" valign="middle" >6 mL</td><td align="center" valign="middle" >9 mL</td></tr><tr><td align="center" valign="middle" >5.0</td><td align="center" valign="middle" >9 mL</td><td align="center" valign="middle" >7 mL</td><td align="center" valign="middle" >10 mL</td></tr><tr><td align="center" valign="middle" >7.5</td><td align="center" valign="middle" >11 mL</td><td align="center" valign="middle" >8 mL</td><td align="center" valign="middle" >12 mL</td></tr><tr><td align="center" valign="middle" >10</td><td align="center" valign="middle" >12 mL</td><td align="center" valign="middle" >9 mL</td><td align="center" valign="middle" >14 mL</td></tr><tr><td align="center" valign="middle" >12.5</td><td align="center" valign="middle" >14 mL</td><td align="center" valign="middle" >11 mL</td><td align="center" valign="middle" >15 mL</td></tr><tr><td align="center" valign="middle" >15</td><td align="center" valign="middle" >27 mL</td><td align="center" valign="middle" >25 mL</td><td align="center" valign="middle" >29 mL</td></tr></tbody></table></table-wrap><table-wrap id="table12" ><label><xref ref-type="table" rid="table1">Table 1</xref>2</label><caption><title> The blocking effect of CCP-3 with 3 mm particles as the main body under different SMK-1 concentrations</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Displacement pressure (MPa)</th><th align="center" valign="middle"  colspan="3"  >SMK-1 dosage</th></tr></thead><tr><td align="center" valign="middle" >0.5%</td><td align="center" valign="middle" >1%</td><td align="center" valign="middle" >1.5%</td></tr><tr><td align="center" valign="middle" >1.5</td><td align="center" valign="middle" >7.5 mL</td><td align="center" valign="middle" >6 mL</td><td align="center" valign="middle" >8.5 mL</td></tr><tr><td align="center" valign="middle" >3.0</td><td align="center" valign="middle" >9 mL</td><td align="center" valign="middle" >7 mL</td><td align="center" valign="middle" >10 mL</td></tr><tr><td align="center" valign="middle" >5.0</td><td align="center" valign="middle" >10 mL</td><td align="center" valign="middle" >7 mL</td><td align="center" valign="middle" >11.5 mL</td></tr><tr><td align="center" valign="middle" >7.5</td><td align="center" valign="middle" >11.5 mL</td><td align="center" valign="middle" >8 mL</td><td align="center" valign="middle" >13 mL</td></tr><tr><td align="center" valign="middle" >10</td><td align="center" valign="middle" >13 mL</td><td align="center" valign="middle" >9 mL</td><td align="center" valign="middle" >14 mL</td></tr><tr><td align="center" valign="middle" >12.5</td><td align="center" valign="middle" >16 mL</td><td align="center" valign="middle" >11 mL</td><td align="center" valign="middle" >17 mL</td></tr><tr><td align="center" valign="middle" >15</td><td align="center" valign="middle" >30 mL</td><td align="center" valign="middle" >24 mL</td><td align="center" valign="middle" >32 mL</td></tr></tbody></table></table-wrap><p>According to the <xref ref-type="table" rid="table1">Table 1</xref>1 and <xref ref-type="table" rid="table1">Table 1</xref>2, the pressure under the three concentrations can reach 12.5 MPa, and there is no obvious leakage. In summary, adding 1% of brucite has the smallest filtration loss, so the optimal addition of brucite is 1%.</p></sec><sec id="s3_3"><title>3.3. Optimum Fiber</title><p>Select a 1 ~ 2 mm SRXW-10 fiber, combined with the above-mentioned granular plugging agent, and investigate the plugging and compressive performance. The plugging experimental data are shown in <xref ref-type="table" rid="table1">Table 1</xref>3 and <xref ref-type="table" rid="table1">Table 1</xref>4.</p><table-wrap-group id="13"><label><xref ref-type="table" rid="table1">Table 1</xref>3</label><caption><title> The plugging effect of CCP-3 with 5 mm particles as the main body under different fiber concentrations</title></caption><table-wrap id="13_1"><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Displacement pressure (MPa)</th><th align="center" valign="middle"  colspan="3"  >Fiber addition</th></tr></thead><tr><td align="center" valign="middle" >0.5%</td><td align="center" valign="middle" >1%</td><td align="center" valign="middle" >1.5%</td></tr><tr><td align="center" valign="middle" >1.5</td><td align="center" valign="middle" >6 mL</td><td align="center" valign="middle" >5 mL</td><td align="center" valign="middle" >7 mL</td></tr><tr><td align="center" valign="middle" >3.0</td><td align="center" valign="middle" >7 mL</td><td align="center" valign="middle" >5 mL</td><td align="center" valign="middle" >8 mL</td></tr><tr><td align="center" valign="middle" >5.0</td><td align="center" valign="middle" >7 mL</td><td align="center" valign="middle" >6 mL</td><td align="center" valign="middle" >10 mL</td></tr></tbody></table></table-wrap><table-wrap id="13_2"><table><tbody><thead><tr><th align="center" valign="middle" >7.5</th><th align="center" valign="middle" >8 mL</th><th align="center" valign="middle" >7 mL</th><th align="center" valign="middle" >11 mL</th></tr></thead><tr><td align="center" valign="middle" >10</td><td align="center" valign="middle" >10 mL</td><td align="center" valign="middle" >9 mL</td><td align="center" valign="middle" >12 mL</td></tr><tr><td align="center" valign="middle" >12.5</td><td align="center" valign="middle" >12 mL</td><td align="center" valign="middle" >10 mL</td><td align="center" valign="middle" >14 mL</td></tr><tr><td align="center" valign="middle" >15</td><td align="center" valign="middle" >14 mL</td><td align="center" valign="middle" >11 mL</td><td align="center" valign="middle" >16 mL</td></tr><tr><td align="center" valign="middle" >17.5</td><td align="center" valign="middle" >30 mL</td><td align="center" valign="middle" >28 mL</td><td align="center" valign="middle" >35 mL</td></tr></tbody></table></table-wrap></table-wrap-group><table-wrap id="table14" ><label><xref ref-type="table" rid="table1">Table 1</xref>4</label><caption><title> The plugging effect of CCP-3 with 3 mm particles as the main body under different fiber concentrations</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Displacement pressure (MPa)</th><th align="center" valign="middle"  colspan="3"  >Fiber addition</th></tr></thead><tr><td align="center" valign="middle" >0.5%</td><td align="center" valign="middle" >1%</td><td align="center" valign="middle" >1.5%</td></tr><tr><td align="center" valign="middle" >1.5</td><td align="center" valign="middle" >6.5 mL</td><td align="center" valign="middle" >5 mL</td><td align="center" valign="middle" >7 mL</td></tr><tr><td align="center" valign="middle" >3.0</td><td align="center" valign="middle" >8 mL</td><td align="center" valign="middle" >6 mL</td><td align="center" valign="middle" >8 mL</td></tr><tr><td align="center" valign="middle" >5.0</td><td align="center" valign="middle" >9 mL</td><td align="center" valign="middle" >6 mL</td><td align="center" valign="middle" >8 mL</td></tr><tr><td align="center" valign="middle" >7.5</td><td align="center" valign="middle" >10.5 mL</td><td align="center" valign="middle" >7 mL</td><td align="center" valign="middle" >9 mL</td></tr><tr><td align="center" valign="middle" >10</td><td align="center" valign="middle" >11.5 mL</td><td align="center" valign="middle" >8 mL</td><td align="center" valign="middle" >11 mL</td></tr><tr><td align="center" valign="middle" >12.5</td><td align="center" valign="middle" >14 mL</td><td align="center" valign="middle" >10 mL</td><td align="center" valign="middle" >14 mL</td></tr><tr><td align="center" valign="middle" >15</td><td align="center" valign="middle" >16 mL</td><td align="center" valign="middle" >12 mL</td><td align="center" valign="middle" >16 mL</td></tr><tr><td align="center" valign="middle" >17.5</td><td align="center" valign="middle" >36 mL</td><td align="center" valign="middle" >30 mL</td><td align="center" valign="middle" >34 mL</td></tr></tbody></table></table-wrap><p>According to the above table, the pressure under the three concentrations can reach 15 MPa, and there is no obvious leakage. In summary, adding 1% of acid-soluble fiber has the smallest total fluid loss, so the optimal addition of SRXW-10 is 1%.</p></sec></sec><sec id="s4"><title>4. Research on the Performance of the Plugging System</title><sec id="s4_1"><title>4.1. Research on the Gel Breaking Performance of the Plugging System</title><p>As a gel breaker, HCl can not only break gel but also acid-soluble particle plugging agent [<xref ref-type="bibr" rid="scirp.106035-ref12">12</xref>]. The plugging gel is used as the base carrier fluid, and the above-developed particle plugging agent is added separately. The experimental temperature is 110˚C. The gel breaking conditions are shown in <xref ref-type="table" rid="table1">Table 1</xref>5 and <xref ref-type="table" rid="table1">Table 1</xref>6:</p><table-wrap-group id="15"><label><xref ref-type="table" rid="table1">Table 1</xref>5</label><caption><title> CCP-3 glue breaking situation with 5 mm particles as the main body</title></caption><table-wrap id="15_1"><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Time</th><th align="center" valign="middle"  colspan="3"  >HCl concentration</th></tr></thead><tr><td align="center" valign="middle" >1%</td><td align="center" valign="middle" >3%</td><td align="center" valign="middle" >5%</td></tr><tr><td align="center" valign="middle" >0 h</td><td align="center" valign="middle" >366 g</td><td align="center" valign="middle" >377 g</td><td align="center" valign="middle" >370 g</td></tr><tr><td align="center" valign="middle" >12 h</td><td align="center" valign="middle" >256 g</td><td align="center" valign="middle" >63 g</td><td align="center" valign="middle" >219 g</td></tr><tr><td align="center" valign="middle" >24 h</td><td align="center" valign="middle" >201 g</td><td align="center" valign="middle" >19 g</td><td align="center" valign="middle" >20 g</td></tr><tr><td align="center" valign="middle" >36 h</td><td align="center" valign="middle" >185 g</td><td align="center" valign="middle" >19 g</td><td align="center" valign="middle" >20 g</td></tr></tbody></table></table-wrap><table-wrap id="15_2"><table><tbody><thead><tr><th align="center" valign="middle" >48 h</th><th align="center" valign="middle" >115 g</th><th align="center" valign="middle" >19 g</th><th align="center" valign="middle" >20 g</th></tr></thead><tr><td align="center" valign="middle" >60 h</td><td align="center" valign="middle" >105 g</td><td align="center" valign="middle" >19 g</td><td align="center" valign="middle" >20 g</td></tr><tr><td align="center" valign="middle" >72 h</td><td align="center" valign="middle" >96 g</td><td align="center" valign="middle" >19 g</td><td align="center" valign="middle" >20 g</td></tr><tr><td align="center" valign="middle" >Glue breaking rate</td><td align="center" valign="middle" >73.8%</td><td align="center" valign="middle" >95%</td><td align="center" valign="middle" >94.6%</td></tr></tbody></table></table-wrap></table-wrap-group><table-wrap id="table16" ><label><xref ref-type="table" rid="table1">Table 1</xref>6</label><caption><title> CCP-3 gel breaking situation with 3 mm particles as the main body</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Time</th><th align="center" valign="middle"  colspan="3"  >HCl concentration</th></tr></thead><tr><td align="center" valign="middle" >1%</td><td align="center" valign="middle" >3%</td><td align="center" valign="middle" >5%</td></tr><tr><td align="center" valign="middle" >0 h</td><td align="center" valign="middle" >365 g</td><td align="center" valign="middle" >365 g</td><td align="center" valign="middle" >372 g</td></tr><tr><td align="center" valign="middle" >12 h</td><td align="center" valign="middle" >306 g</td><td align="center" valign="middle" >223 g</td><td align="center" valign="middle" >205 g</td></tr><tr><td align="center" valign="middle" >24 h</td><td align="center" valign="middle" >292 g</td><td align="center" valign="middle" >18 g</td><td align="center" valign="middle" >19 g</td></tr><tr><td align="center" valign="middle" >36 h</td><td align="center" valign="middle" >281 g</td><td align="center" valign="middle" >18 g</td><td align="center" valign="middle" >19 g</td></tr><tr><td align="center" valign="middle" >48 h</td><td align="center" valign="middle" >265 g</td><td align="center" valign="middle" >18 g</td><td align="center" valign="middle" >19 g</td></tr><tr><td align="center" valign="middle" >60 h</td><td align="center" valign="middle" >218 g</td><td align="center" valign="middle" >18 g</td><td align="center" valign="middle" >19 g</td></tr><tr><td align="center" valign="middle" >72 h</td><td align="center" valign="middle" >133 g</td><td align="center" valign="middle" >18 g</td><td align="center" valign="middle" >19 g</td></tr><tr><td align="center" valign="middle" >Glue breaking rate</td><td align="center" valign="middle" >60.7%</td><td align="center" valign="middle" >95.1%</td><td align="center" valign="middle" >94.9%</td></tr></tbody></table></table-wrap><p>When the two particle plugging agents are used as the base carrier fluid for the plugging gel, the 3% and 5% concentration of HCl have the highest gel breaking rate at the same time, reaching 95%, and the residual is the least. Considering the cost and gel breaking rate, plugging, the best concentration of the system for gel breaking is 3%; both of them can complete the gel breaking within 24 h.</p></sec><sec id="s4_2"><title>4.2. Evaluation of Swelling Performance of Granular Plugging Agent under Different Water Quality</title><p>Under normal temperature conditions, take the dried granular plugging agent of the same quality and put them into three identical beakers at the same time. The three beakers are added with different salinity salt solutions to measure different absorption media [<xref ref-type="bibr" rid="scirp.106035-ref13">13</xref>]. Water swellability under water absorption, the experimental results are shown in <xref ref-type="fig" rid="fig3">Figure 3</xref>.</p><p>It can be seen from <xref ref-type="fig" rid="fig3">Figure 3</xref> that as the salt concentration increases, the water swelling rate of the particulate plugging agent increases. Since the swelling multiples of granular plugging agents in salt water are all over 7 times [<xref ref-type="bibr" rid="scirp.106035-ref14">14</xref>], they meet the requirements of leak-proof plugging operations under high salinity.</p></sec><sec id="s4_3"><title>4.3. Evaluation of the Plugging Performance of the Plugging System</title><p>Through the water plugging and profile control experimental system, the sand-filled pipe is used to simulate the plugging effect under high temperature and high pressure, and three sets of parallel experiments are carried out [<xref ref-type="bibr" rid="scirp.106035-ref15">15</xref>]. The experiment uses artificial core (12 mm aperture), the experiment temperature is 110˚C, and the experimental data are shown in <xref ref-type="table" rid="table1">Table 1</xref>7:</p><table-wrap id="table17" ><label><xref ref-type="table" rid="table1">Table 1</xref>7</label><caption><title> Pressure resistance and plugging situation of the plugging system</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Plugging system</th><th align="center" valign="middle" >Experiment number</th><th align="center" valign="middle" >temperature/˚C</th><th align="center" valign="middle" >Pressure time</th><th align="center" valign="middle" >Maximum compression/MPa</th><th align="center" valign="middle" >Gelling effect</th></tr></thead><tr><td align="center" valign="middle"  rowspan="3"  >Plugging system with 5 mm particles as the main body</td><td align="center" valign="middle" >1</td><td align="center" valign="middle" >110</td><td align="center" valign="middle" >5 days</td><td align="center" valign="middle" >20</td><td align="center" valign="middle" >Successfully blocked</td></tr><tr><td align="center" valign="middle" >2</td><td align="center" valign="middle" >110</td><td align="center" valign="middle" >5 days</td><td align="center" valign="middle" >20</td><td align="center" valign="middle" >Successfully blocked</td></tr><tr><td align="center" valign="middle" >3</td><td align="center" valign="middle" >110</td><td align="center" valign="middle" >5 days</td><td align="center" valign="middle" >20</td><td align="center" valign="middle" >Successfully blocked</td></tr><tr><td align="center" valign="middle"  rowspan="3"  >Plugging system with 3 mm particles as the main body</td><td align="center" valign="middle" >1</td><td align="center" valign="middle" >110</td><td align="center" valign="middle" >5 days</td><td align="center" valign="middle" >20</td><td align="center" valign="middle" >Successfully blocked</td></tr><tr><td align="center" valign="middle" >2</td><td align="center" valign="middle" >110</td><td align="center" valign="middle" >5 days</td><td align="center" valign="middle" >20</td><td align="center" valign="middle" >Successfully blocked</td></tr><tr><td align="center" valign="middle" >3</td><td align="center" valign="middle" >110</td><td align="center" valign="middle" >5 days</td><td align="center" valign="middle" >20</td><td align="center" valign="middle" >Successfully blocked</td></tr></tbody></table></table-wrap><p>According to <xref ref-type="table" rid="table1">Table 1</xref>7, at an experimental temperature of 110˚C, the sand-filled pipe plugging experiment was performed on the two particle plugging systems, and it was shown that both plugging systems can plug for 5 days under high temperature and high pressure conditions. Both plugging systems can achieve a good plugging effect on the formation.</p></sec></sec><sec id="s5"><title>5. Conclusions</title><p>1) A composite plugging system was developed using polymer solution, multi-diameter rigid particles, expandable particles and modified fibers. The formula is: a) water + 2% polyacrylamide + 0.1% N, N-methylene bisacrylamide + 20% rigid particles (5 mm, 1 mm, 0.5 mm CCP-3 ratio 4:2:1) + 1% 3 mm expanded particles SMK-1 + 1% 1 - 2 mm fiber SRXW -10; b) Water + 2% polyacrylamide + 0.1% N, N-methylene bisacrylamide + 20% rigid particles (3 mm, 0.1 mm, 0.05 mm CCP-3 ratio is 3:2:1) + 1% of 3 mm expanded particles SMK-1 + 1% of 1 - 2 mm fiber SRXW-10.</p><p>2) The plugging system can plug for 5 days at a high temperature of 110˚C and a high pressure of 20 MPa, and the plugging system can achieve a good plugging effect on the formation.</p><p>3) The water swelling multiples of the granular plugging agent in salt water are all above 7 times, which meets the requirements of leak-proof plugging operations under high salinity.</p><p>4) The plugging system uses HCl as the breaker, and the optimal concentration is 3%.</p></sec><sec id="s6"><title>Conflicts of Interest</title><p>The authors declare no conflicts of interest regarding the publication of this paper.</p></sec><sec id="s7"><title>Cite this paper</title><p>Gao, Y., Wang, Z.W., Shao, X.L., Tan, D.C. and Liu, E.P. (2021) Study on the Plugging System of the Lower Ancient High Loss Zone in Changqing Gas Field. Open Journal of Yangtze Gas and Oil, 6, 1-12. https://doi.org/10.4236/ojogas.2021.61001</p></sec></body><back><ref-list><title>References</title><ref id="scirp.106035-ref1"><label>1</label><mixed-citation publication-type="other" xlink:type="simple">Zhang, S.H., Luo, P.Y., et al. (1996) Reservoir Protection Technology. Petroleum Industry Press, Beijing.</mixed-citation></ref><ref id="scirp.106035-ref2"><label>2</label><mixed-citation publication-type="other" xlink:type="simple">McGill, C.H., et al. (2016) Sealing Frequency of B104 Cells Declines Exponentially with Decreasing Transection Distance from the Axon Hillock. Experimental Neurology, 279, 149-158.</mixed-citation></ref><ref id="scirp.106035-ref3"><label>3</label><mixed-citation publication-type="other" xlink:type="simple">Cai, L.S., Su, C.M. and Liu, J.H. (2010) Analysis of the Pressure-Bearing Capacity of the Leak-Prone Formation. 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