# An Improved Composite Fly Ash Gel to Extinguish Underground Coal Fire in Close Distance Coal Seams: A Case Study

Authors: Jun Guo; Guobin Cai; Yan Jin; Xuezhao Zheng; Yin Liu
Journal: Advances in Materials Science and Engineering
 (2020)

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## Abstract

Fire extinguishing with the superior performance of fly ash composite colloid material is a cost-effective colloid fire prevention technology. In this paper, a new powder additive (suspending agent (XK-XJ) and gelling agent) was developed for the existing fire extinguishing technology of fly ash compound colloid. Tests show that the best additions to the fly ash slurry were 0.3% and 0.1∼0.3%, respectively. The grouting technical scheme of adding a suspending agent on the ground and gelling agent downhole was proposed to solve the problems of solid material settlement and blockage in the long-distance pipeline transportation process. Finally, the optimized fly ash colloid fire prevention and extinguishing technology was successfully applied to the fire control engineering examples of close-range coal seam groups, and the rationality of the developed powder and its proportion was tested, and the feasibility in coal fire control was tested.


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## Body

## 1. Introduction

Occurrence of coal fire disaster is a huge problem faced by all major coal-producing countries in the world; between 1947 and 2006, there were 7757 coal fire accidents in Poland [1], and there were 138 coal fires in the United States from 1990 to 2007 [2], which seriously threatens the safety production of coal and the safety of workers [3, 4]. In India, more than 80% of coal mine fires are caused by spontaneous combustion [5]. Also, the spontaneous combustion attacks Chinese coal mines seriously [6]. Along with the continuous development of science and technology, coal spontaneous combustion prevention technology has been greatly developed. At present, technologies commonly used in coal mines are leakage plugging, pressure equalization, insert gas, insert foam, three-phase foam, atomizing inhibitor, inserting inhibitor, water injection, injection of yellow mud, coal surface spraying, injection gel, and other fire preventing and extinguishing technologies [7–10]. As a new technology, the gel fire preventing and technology has been studied by a large number of scholars since the beginning of 1990s. Three kinds of gel materials have been formed: silicic acid gel, thickened gel, and fly ash solidified material, which has become a kind of important mine fire preventing and fighting technology. The technology integrates the function of plugging, cooling, blocking, and solidifying water so that the easy flowing aqueous solution is gelatinized at a specified time and a position, high-temperature coal body is wrapped, and the endothermic cooling effect of water is fully exerted. The problem of leakage and loss of grouting and water injection is well solved, and the gel will not vaporize rapidly in the open fire at nearly 1000°C. But it will gradually shrink due to the slow evaporation of water with good fire extinguishing safety and strong applicability [11, 12]. In China, in the application and popularization process of gel fire preventing and extinguishing technology, several technologies such as in the pit or surface mobile, pipe network type and multifunctional grouting and glue injection fire preventing, and extinguishing system have been developed, which can be flexibly selected according to the actual conditions of mines [11, 13].The rapid and steady development of gel fire preventing and extinguishing technology has made it successfully widely applied to the prevention and control of coal spontaneous combustion. For example, Jin et al. [14], Zhai et al. [15], and Xiao et al. [16] have respectively analyzed the formation mechanism and characteristics of coal spontaneous combustion in a coal mine and coal outcrop fire area. A comprehensive fire preventing and extinguishing technology scheme mainly composed of polymer colloid and light-paste material and the fire area is successfully treated. In the field of coal spontaneous combustion disaster, fire is the most difficult to prevent and control. In the mining process of close-distance coal seam group, the coal left in the upper layer gob or the nonmined coal body falls into the coal seam gob, or the coal left in the upper layer gob will cause oxidation spontaneous combustion to form coal seam fire under the condition of air leakage and oxygen supply. Of course, gel fire preventing and extinguishing technology is widely used in this kind of fire prevention and control. For example, Guo et al. [17] have successfully treated the fire area with composite gel technology aiming at the phenomenon of spontaneous combustion of the close-distance coal seam group in a mining area. In view of the spontaneous combustion in close-distance coal seam mining in Baijiao Coal Mine of Furong Mining Area in Sichuan Province, Zheng et al. [18] successfully adopted the technology of composite gel and fly ash composite gel to prevent and extinguish fire. Guo et al. [19] and Hu et al. [20, 21] have successfully treated the fire area by using ground drilling and filling gel, three-phase foam, and fly ash gel materials combined with inert gas to cover the fire area of close-distance coal seams. Li et al. [22] and Xue et al. [23] have prepared new composite gels for the prevention of spontaneous combustion of coal and successfully treated the fire area. Fan et al. [24]and Zhao et al. [25] have successfully used gel-stabilization foam and grouting technology for drilled pipe to inhibit spontaneous combustion of coal.Although the gel fire extinguishing materials have been successfully applied in the abovementioned engineering examples and achieved good results, some deficiencies have been exposed in the practical application process, especially when the fly ash/loess composite gel slurry is transported in the long-distance pipeline. The gelling time is not properly controlled and the concentration of gel slurry is too large, and the solid material (fly ash or loess) of the slurry settle due to the difference between the solute and the solution density, which may block the pipeline of the slurry, making it difficult to deliver the fire extinguishing material to the designated position for extinguishing fire. If the long-distance transmission is realized by reducing the concentration of gel slurry, although the problem of pipeline plugging can be solved, it is also difficult to achieve the purpose of extinguishing fire because the effective components of the slurry are too low (gel fire extinguishing agent, fly ash, or loess). In order to solve the abovementioned problems, a technical scheme has been proposed, that is, a suspending agent is added onto the surface of fly ash water solution and a gelling agent is added in the pit to realize long-distance pipeline transportation of fly ash slurry, as shown in Figure1.Figure 1
Principle of the composite gel fire preventing and extinguishing system.In the scheme, the suspending agent is an additive with suspending and dispersion effect. After the suspending agent is added into the slurry of fly ash or loess, the liquid-solid interface property can be remarkably changed so that the surface tension is lowered and the dispersion system is more stable. This can improve the fluidity of the slurry, reduce the sedimentation speed and the flow resistance of the slurry, effectively prevent sedimentation, and facilitate pipeline transportation. However, due to the different properties of the suspending agent and gelling agent and the respective added amounts, the flow and gelling properties of the slurry are greatly influenced.On the basis of the existing gel fire extinguishing material, this study conducts a modification test on the fly ash gel material, explores the formula of a new composite gel suspending agent and its optimum addition amount, and deals with the influence of a new suspending agent and gelling agent on sedimentation and gelling properties of fly ash aqueous solution. The fly ash composite gel fire preventing and extinguishing technology is improved, and an industrial test is carried out in a close-distance coal seam group fire control of a mine in Xinjiang to test the fire preventing and extinguishing effect.


## 2. Modification Test on Fly Ash Composite Gel

### 2.1. Test Method

#### 2.1.1. Technical Route

Based on the previous research of the research group, the modification experiment under various conditions is carried out to prepare a new suspending agent, and the optimum addition amount of the suspending agent and gelling agent is determined to improve the performance of fly ash slurry [11, 26]. Figure 2 shows the technical route of the test.Figure 2
Technical route of the test.


#### 2.1.2. Test Conditions

For the modification test of the suspending agent, XK and XJ are selected as the main components of the suspending agent, and the influence of XK and XJ on the sedimentation effect of slurry is studied under the conditions of different mixing ratio and total addition. After adding the suspending agent of different ratio and addition amount to fly ash slurry and after being stirred evenly, the sedimentation height of solid material in slurry at different time is measured. Then, the curve of sedimentation height with time is drawn and the suspending effect under each condition is examined. Each set of data is repeated 5 times in the same conditions, and the average value of the experimental data is taken. Similarly, a modification test is conducted on the gelling agent. The viscosity of the slurry may be used to measure the gelling effect of the gelling agent, and the changing relationship of the viscosity of the slurry may be measured with the components of the added gelling agent.The test is carried out with fly ash slurry with a water-cement mass ratio of 1 : 1. All test conditions are shown in Table1.Table 1
Test conditions.
Test numberTest conditionTest contentClass conditionGroup12345678910(1–1)Total addition amount of suspending agent (%)—0.10.20.30.40.50.70.80.91.05Settlement height of slurry at different time (cm)Mass ratio of XK and XJ (XK 0.05%)—1 : 11 : 31 : 51 : 71 : 91 : 131 : 151 : 171 : 20(1–2)Total addition amount of suspending agent (%)0.30.30.30.30.30.30.30.30.30.3Quality ratio of XK and XJ1 : 11 : 21 : 31 : 41 : 51 : 61 : 71 : 91 : 111 : 13(1–3)Total addition amount of suspending agent (%)00.30.30.10.20.30.40.50.60.7Quality ratio of XK and XJ—1 : 00 : 11 : 51 : 51 : 51 : 51 : 51 : 51 : 5(2)Total addition amount of gelling agent (%)00.050.10.150.20.250.30.350.40.45Viscosity coefficient (MPa.s)0.50.550.60.650.70.750.80.850.90.95(3)The addition amount of gelling agent (%)00.050.10.150.20.250.30.350.40.450.50.550.60.650.70.750.80.850.90.95The addition amount of new suspending agent (%)New suspending agents of 0, 0.25, 0.3, and 0.35% are selected, respectively, and mixed with the gelling agent added to the abovementioned amount in turn, and then mixed with fly ash slurry, respectivelyNote. The ratio in the table is mass ratio; “—” means that the corresponding suspending agent or pour point depressant is not added.


### 2.2. Test Result and Discussion

#### 2.2.1. Modification Test of Suspending Agent

The variation curve of the sedimentation height of the fly ash slurry with time under different conditions and different total additions obtained in the test (1–1) is shown in Figure3.Figure 3
Variation of sedimentation height of fly ash slurry with time in test (1–1).As can be seen from Figure3, when XK : XJ = 1 : 5 (total addition amount is 0.3%), the sedimentation speed of the slurry is the slowest, that is, the suspension effect is the best; the sedimentation speed of a blank sample without any additive is the fastest. When XK : XJ = 1 : 3 and 1 : 13, the suspension is also good, but it is slightly worse than 1 : 5. When XK : XJ = 1 : 20 and 1 : 1, the suspension is poor. The mixture of XJ and XK can promote the suspension of fly ash slurry, so XK : XJ = 1 : (3–13) can be controlled.The variation curve of the sedimentation height of the fly ash slurry with time under the condition of different ratios and constant total additive amount obtained by the test (1–2) is shown in Figure4.Figure 4
Variation of sedimentation height of fly ash slurry with time in test (1–2).It can be seen from Figure4 that, when the total additive amount is the same, the difference between the ratio of XK and XJ on the influence of sedimentation speed is not obvious, but the overall performance is still that XK : XJ = 1 : 5 is the best.The sedimentation height of fly ash slurry changes with time under the condition of the same ratio and different total additive amounts as shown in Figure5.Figure 5
Variation of settlement height of fly ash slurry with time in test (1–3).As can be seen from Figure5, the addition of pure XK or pure XJ contributes to the suspension of fly ash slurry to some extent, but the effect is weaker than the addition of the mixture of both. Under the same ratio, with the increase of the total addition amount, the suspension effect is better and the effect is better when the addition amount is 0.3, 0.4, 0.5, 0.6, and 0.7%. The suspending agent with XK : XJ = 1 : 5 is optimized when the total amount of suspension is 0.3% by considering the suspending property and the economic index.


#### 2.2.2. Gelling Agent Test

Figure6 shows the test results of test (2) and test (3), that is, the influence of different amounts of gelling agent and three kinds of suspending agent (0.25, 0.3, 0.35%) on the viscosity of fly ash slurry.Figure 6
Effect of gelling and suspending agents on the viscosity of fly ash slurry.As can be seen from Figure6, with the addition of a gelling agent, the viscosity of fly ash slurry significantly increases and reaches the first maximum value, when the addition amount reaches 0.1%, and reaches the second maximum value, when the addition amount reaches 0.3%. After that, the viscosity of the slurry slows down with the increase of the amount of gelling agent. The addition of a new suspending agent will not only not destroy the gelling property of fly ash slurry but also promote it to a certain extent. In the practical application process, the addition amount of the gelling agent can be selected according to the on-site requirements of the gelling property. Generally, the addition amount is preferably from 0.1 to 0.3%.


## 2.1. Test Method

### 2.1.1. Technical Route

Based on the previous research of the research group, the modification experiment under various conditions is carried out to prepare a new suspending agent, and the optimum addition amount of the suspending agent and gelling agent is determined to improve the performance of fly ash slurry [11, 26]. Figure 2 shows the technical route of the test.Figure 2
Technical route of the test.


### 2.1.2. Test Conditions

For the modification test of the suspending agent, XK and XJ are selected as the main components of the suspending agent, and the influence of XK and XJ on the sedimentation effect of slurry is studied under the conditions of different mixing ratio and total addition. After adding the suspending agent of different ratio and addition amount to fly ash slurry and after being stirred evenly, the sedimentation height of solid material in slurry at different time is measured. Then, the curve of sedimentation height with time is drawn and the suspending effect under each condition is examined. Each set of data is repeated 5 times in the same conditions, and the average value of the experimental data is taken. Similarly, a modification test is conducted on the gelling agent. The viscosity of the slurry may be used to measure the gelling effect of the gelling agent, and the changing relationship of the viscosity of the slurry may be measured with the components of the added gelling agent.The test is carried out with fly ash slurry with a water-cement mass ratio of 1 : 1. All test conditions are shown in Table1.Table 1
Test conditions.
Test numberTest conditionTest contentClass conditionGroup12345678910(1–1)Total addition amount of suspending agent (%)—0.10.20.30.40.50.70.80.91.05Settlement height of slurry at different time (cm)Mass ratio of XK and XJ (XK 0.05%)—1 : 11 : 31 : 51 : 71 : 91 : 131 : 151 : 171 : 20(1–2)Total addition amount of suspending agent (%)0.30.30.30.30.30.30.30.30.30.3Quality ratio of XK and XJ1 : 11 : 21 : 31 : 41 : 51 : 61 : 71 : 91 : 111 : 13(1–3)Total addition amount of suspending agent (%)00.30.30.10.20.30.40.50.60.7Quality ratio of XK and XJ—1 : 00 : 11 : 51 : 51 : 51 : 51 : 51 : 51 : 5(2)Total addition amount of gelling agent (%)00.050.10.150.20.250.30.350.40.45Viscosity coefficient (MPa.s)0.50.550.60.650.70.750.80.850.90.95(3)The addition amount of gelling agent (%)00.050.10.150.20.250.30.350.40.450.50.550.60.650.70.750.80.850.90.95The addition amount of new suspending agent (%)New suspending agents of 0, 0.25, 0.3, and 0.35% are selected, respectively, and mixed with the gelling agent added to the abovementioned amount in turn, and then mixed with fly ash slurry, respectivelyNote. The ratio in the table is mass ratio; “—” means that the corresponding suspending agent or pour point depressant is not added.


## 2.1.1. Technical Route

Based on the previous research of the research group, the modification experiment under various conditions is carried out to prepare a new suspending agent, and the optimum addition amount of the suspending agent and gelling agent is determined to improve the performance of fly ash slurry [11, 26]. Figure 2 shows the technical route of the test.Figure 2
Technical route of the test.


## 2.1.2. Test Conditions

For the modification test of the suspending agent, XK and XJ are selected as the main components of the suspending agent, and the influence of XK and XJ on the sedimentation effect of slurry is studied under the conditions of different mixing ratio and total addition. After adding the suspending agent of different ratio and addition amount to fly ash slurry and after being stirred evenly, the sedimentation height of solid material in slurry at different time is measured. Then, the curve of sedimentation height with time is drawn and the suspending effect under each condition is examined. Each set of data is repeated 5 times in the same conditions, and the average value of the experimental data is taken. Similarly, a modification test is conducted on the gelling agent. The viscosity of the slurry may be used to measure the gelling effect of the gelling agent, and the changing relationship of the viscosity of the slurry may be measured with the components of the added gelling agent.The test is carried out with fly ash slurry with a water-cement mass ratio of 1 : 1. All test conditions are shown in Table1.Table 1
Test conditions.
Test numberTest conditionTest contentClass conditionGroup12345678910(1–1)Total addition amount of suspending agent (%)—0.10.20.30.40.50.70.80.91.05Settlement height of slurry at different time (cm)Mass ratio of XK and XJ (XK 0.05%)—1 : 11 : 31 : 51 : 71 : 91 : 131 : 151 : 171 : 20(1–2)Total addition amount of suspending agent (%)0.30.30.30.30.30.30.30.30.30.3Quality ratio of XK and XJ1 : 11 : 21 : 31 : 41 : 51 : 61 : 71 : 91 : 111 : 13(1–3)Total addition amount of suspending agent (%)00.30.30.10.20.30.40.50.60.7Quality ratio of XK and XJ—1 : 00 : 11 : 51 : 51 : 51 : 51 : 51 : 51 : 5(2)Total addition amount of gelling agent (%)00.050.10.150.20.250.30.350.40.45Viscosity coefficient (MPa.s)0.50.550.60.650.70.750.80.850.90.95(3)The addition amount of gelling agent (%)00.050.10.150.20.250.30.350.40.450.50.550.60.650.70.750.80.850.90.95The addition amount of new suspending agent (%)New suspending agents of 0, 0.25, 0.3, and 0.35% are selected, respectively, and mixed with the gelling agent added to the abovementioned amount in turn, and then mixed with fly ash slurry, respectivelyNote. The ratio in the table is mass ratio; “—” means that the corresponding suspending agent or pour point depressant is not added.


## 2.2. Test Result and Discussion

### 2.2.1. Modification Test of Suspending Agent

The variation curve of the sedimentation height of the fly ash slurry with time under different conditions and different total additions obtained in the test (1–1) is shown in Figure3.Figure 3
Variation of sedimentation height of fly ash slurry with time in test (1–1).As can be seen from Figure3, when XK : XJ = 1 : 5 (total addition amount is 0.3%), the sedimentation speed of the slurry is the slowest, that is, the suspension effect is the best; the sedimentation speed of a blank sample without any additive is the fastest. When XK : XJ = 1 : 3 and 1 : 13, the suspension is also good, but it is slightly worse than 1 : 5. When XK : XJ = 1 : 20 and 1 : 1, the suspension is poor. The mixture of XJ and XK can promote the suspension of fly ash slurry, so XK : XJ = 1 : (3–13) can be controlled.The variation curve of the sedimentation height of the fly ash slurry with time under the condition of different ratios and constant total additive amount obtained by the test (1–2) is shown in Figure4.Figure 4
Variation of sedimentation height of fly ash slurry with time in test (1–2).It can be seen from Figure4 that, when the total additive amount is the same, the difference between the ratio of XK and XJ on the influence of sedimentation speed is not obvious, but the overall performance is still that XK : XJ = 1 : 5 is the best.The sedimentation height of fly ash slurry changes with time under the condition of the same ratio and different total additive amounts as shown in Figure5.Figure 5
Variation of settlement height of fly ash slurry with time in test (1–3).As can be seen from Figure5, the addition of pure XK or pure XJ contributes to the suspension of fly ash slurry to some extent, but the effect is weaker than the addition of the mixture of both. Under the same ratio, with the increase of the total addition amount, the suspension effect is better and the effect is better when the addition amount is 0.3, 0.4, 0.5, 0.6, and 0.7%. The suspending agent with XK : XJ = 1 : 5 is optimized when the total amount of suspension is 0.3% by considering the suspending property and the economic index.


### 2.2.2. Gelling Agent Test

Figure6 shows the test results of test (2) and test (3), that is, the influence of different amounts of gelling agent and three kinds of suspending agent (0.25, 0.3, 0.35%) on the viscosity of fly ash slurry.Figure 6
Effect of gelling and suspending agents on the viscosity of fly ash slurry.As can be seen from Figure6, with the addition of a gelling agent, the viscosity of fly ash slurry significantly increases and reaches the first maximum value, when the addition amount reaches 0.1%, and reaches the second maximum value, when the addition amount reaches 0.3%. After that, the viscosity of the slurry slows down with the increase of the amount of gelling agent. The addition of a new suspending agent will not only not destroy the gelling property of fly ash slurry but also promote it to a certain extent. In the practical application process, the addition amount of the gelling agent can be selected according to the on-site requirements of the gelling property. Generally, the addition amount is preferably from 0.1 to 0.3%.


## 2.2.1. Modification Test of Suspending Agent

The variation curve of the sedimentation height of the fly ash slurry with time under different conditions and different total additions obtained in the test (1–1) is shown in Figure3.Figure 3
Variation of sedimentation height of fly ash slurry with time in test (1–1).As can be seen from Figure3, when XK : XJ = 1 : 5 (total addition amount is 0.3%), the sedimentation speed of the slurry is the slowest, that is, the suspension effect is the best; the sedimentation speed of a blank sample without any additive is the fastest. When XK : XJ = 1 : 3 and 1 : 13, the suspension is also good, but it is slightly worse than 1 : 5. When XK : XJ = 1 : 20 and 1 : 1, the suspension is poor. The mixture of XJ and XK can promote the suspension of fly ash slurry, so XK : XJ = 1 : (3–13) can be controlled.The variation curve of the sedimentation height of the fly ash slurry with time under the condition of different ratios and constant total additive amount obtained by the test (1–2) is shown in Figure4.Figure 4
Variation of sedimentation height of fly ash slurry with time in test (1–2).It can be seen from Figure4 that, when the total additive amount is the same, the difference between the ratio of XK and XJ on the influence of sedimentation speed is not obvious, but the overall performance is still that XK : XJ = 1 : 5 is the best.The sedimentation height of fly ash slurry changes with time under the condition of the same ratio and different total additive amounts as shown in Figure5.Figure 5
Variation of settlement height of fly ash slurry with time in test (1–3).As can be seen from Figure5, the addition of pure XK or pure XJ contributes to the suspension of fly ash slurry to some extent, but the effect is weaker than the addition of the mixture of both. Under the same ratio, with the increase of the total addition amount, the suspension effect is better and the effect is better when the addition amount is 0.3, 0.4, 0.5, 0.6, and 0.7%. The suspending agent with XK : XJ = 1 : 5 is optimized when the total amount of suspension is 0.3% by considering the suspending property and the economic index.


## 2.2.2. Gelling Agent Test

Figure6 shows the test results of test (2) and test (3), that is, the influence of different amounts of gelling agent and three kinds of suspending agent (0.25, 0.3, 0.35%) on the viscosity of fly ash slurry.Figure 6
Effect of gelling and suspending agents on the viscosity of fly ash slurry.As can be seen from Figure6, with the addition of a gelling agent, the viscosity of fly ash slurry significantly increases and reaches the first maximum value, when the addition amount reaches 0.1%, and reaches the second maximum value, when the addition amount reaches 0.3%. After that, the viscosity of the slurry slows down with the increase of the amount of gelling agent. The addition of a new suspending agent will not only not destroy the gelling property of fly ash slurry but also promote it to a certain extent. In the practical application process, the addition amount of the gelling agent can be selected according to the on-site requirements of the gelling property. Generally, the addition amount is preferably from 0.1 to 0.3%.


## 3. Fire Preventing and Extinguishing Technology of Fly Ash Composite Gel

The fly ash composite gel material grouting system consists of slurry storage site, slurry transportation and pretreatment system, water supply system, continuous quantitative pulping system, slurry filtering system, additive adding device 1, slurry pressure convey device, slurry conveying pipe network system, additive adding device 2, and inlet well, as shown in Figure7. On the ground, fly ash and water are mixed in proportion by equipment such as gel preparation machine to prepare slurry of desired concentration, and the suspending agent is added to the slurry by the mobile adding device 1 and then transported to the pit through the pipe network. In the pit, the slurry pipeline is connected with the glue injection hole, and the fly ash colloid slurry is injected into the fire zone for fire extinguishing, wherein the addition of the gelling agent is completed by the admixture addition device 2.Figure 7
Process of the mobile colloid injection system.


## 4. Application Case Study

### 4.1. Project Profile

In the paper, the fire extinguishing application of improved fly ash colloid is selected in a mine in Xinjiang, China. In the mine field where a mine is located in Xinjiang (as shown in Figures8(a) and 8(b)), the coal seams are relatively concentrated, and there are 6 mined coal seams, and the distribution characteristics are shown in Table 2. Coal seams 4, 5, and 6 are main coal seams, belonging to close-distance coal seam mining, low-gas mine, and spontaneous combustion coal seam. During the mining process of 6# coal seam of 2130 footrill, CO is detected in the return airway of 2120 working face, which exceeds 100 ppm. It is preliminarily judged that the spontaneous combustion occurs in the floating coal in the 2183 air shaft and the original 5# coal seam in the old mining roadway. A large-scale high-temperature area has been formed in the closed wall, and the development speed is relatively fast. It is possible to develop to 2130 footrill along the arch roadway in a relatively short time for the return airway of 2120 working face of 6# coal seam. In view of the characteristics of unknown fire area scope and degree of spontaneous combustion [27–29], the overall idea of “detecting first, isolating, extinguishing later, and observing the whole process” is adopted to carry out fire area control. The method of radon detection is adopted for fire area detection and the instrument is a CD-1α cup radon detector [30–32]. The detection range is 800 m along the east-west direction of the coal seam and 150 m in the north-south direction, and the total detection area is 12,000 m2. A data processing software package (CDTH software package) is used to perform data processing [27], and a fire range distribution map (Figure 8(c)) is obtained. As can be seen from Figure 8(c), the total area of the fire area is 31,140 m2, and there are 7 high-temperature abnormal zones A, B, C, D, E, F, and G, respectively, with areas of 2,100 m2, 1,500 m2, 11,600 m2, 340 m2, 3,400 m2, 3,800 m2, and 8,400 m2, respectively.Figure 8
Location and fire area of the technical application mine. (a) the enlargement of the blue area in (b). (c) the distribution range of fire area in (a).Table 2
Coal seam features.
Coal seam no.Thickness of coal seamDistance of coal seam (m)StabilityRecoverabilityApparent density (m3)Lithology of the roof and floorDip angle (°)RoofSymbolFloorSymbol13.115.93StableMinable1.35The black sandstoneBlack powder sandstone3624.8614.07StableMinable1.35Medium sandstoneSilstone3531.8639.84StableMinable1.35Coarse sandstone with quartzMedium sandstone3543.2624.4StableMinable1.35Gravel sandstoneSilstone3455.3232.14StableMinable1.35Coarse sandstone with quartzSilstone3563.0334.88StableMinable1.35Gravel sandstoneSilstone35


### 4.2. Application of Fly Ash Slurry

In order to better prepare and inject improved fly ash colloids into the fire area, the gel preparation machine and the mobile adding device are respectively “MYZ-30 ground mobile grouting and gel injection fire preventing and extinguishing system” and “ZHJ-5/1.8 mine-used mobile grouting fire preventing and extinguishing device” developed by the Innovation Team of the Ministry of Education for Prevention and Control of Coal Fire Disaster of Xi’an University of Science and Technology [33], as shown in Figure 9. The area gap is filled with gel, and the total amount of slurry is about 15,350 m3. Table 3 shows the specific gel process in combination with the goal of filling gel in each area.Figure 9
The application of fly ash slurry in the fire area.
(a)(b)Table 3
Technological parameters of injection gel.
No.Filled areaAmount of colloid injected (m3)Quality ratio of water and fly ashAddition amount of gelling agent (%)Addition amount of suspending agent (%)Operating modeMain purposes1Abandoned roadway90001 : (1–1.5)0.10.3Discontinuous glue injection. 3-4 hours of injection, pause for about 1 hourFully exfoliate the water in the colloid to increase the colloid accumulation rate2Existing masonry roadways1350(1–1.5) : 10.30.3Continuous large amount of glue injectionIncrease the fluidity and coverage of colloids in the cracks of high-temperature coal to improve the fire extinguishing effect3Roof falling zone and goaf area5000(1–1.5) : 10.10.3Discontinuous glue injection. 1 hour of injection, pause for about half an hourRelease water from the colloid and fill the fissure with solid material as much as possible


### 4.3. Field Investigation Analyses

When predicting the coal spontaneous combustion process, CO has always been one of the commonly used index gases, and its existence runs through the entire coal seam spontaneous combustion process [7, 34]. The fire area is monitored by means of manual detection through ground gel injection drilling hole and special observation hole. CO gas data in the borehole are collected, and the variation curve of CO gas concentration in the fire area with the treatment progress of the fire area is obtained, as shown in Figure 10.Figure 10
Obtaining CO data through surface drilling monitoring. (a) Monitoring of the ground borehole fire area. (b) Monitoring the variation curve of CO gas concentration.As can be seen from Figure10, the CO gas data in the observation borehole of the fire area obviously decreases and the fire area is effectively controlled rapidly within one month after the drilling and injection work is carried out. The CO gas concentration in the observation borehole in the fire area decreases from the highest 160 ppm to 40 ppm with the increase of injected gel. The CO gas concentration in the observation borehole in the fire area reduces to 0 ppm within two months by continuous injection of the subsequent composite gel. After that, the fire area is continuously observed. The CO gas concentration is stable at 0 ppm all the time. It can be concluded that the fire area is extinguished.


## 4.1. Project Profile

In the paper, the fire extinguishing application of improved fly ash colloid is selected in a mine in Xinjiang, China. In the mine field where a mine is located in Xinjiang (as shown in Figures8(a) and 8(b)), the coal seams are relatively concentrated, and there are 6 mined coal seams, and the distribution characteristics are shown in Table 2. Coal seams 4, 5, and 6 are main coal seams, belonging to close-distance coal seam mining, low-gas mine, and spontaneous combustion coal seam. During the mining process of 6# coal seam of 2130 footrill, CO is detected in the return airway of 2120 working face, which exceeds 100 ppm. It is preliminarily judged that the spontaneous combustion occurs in the floating coal in the 2183 air shaft and the original 5# coal seam in the old mining roadway. A large-scale high-temperature area has been formed in the closed wall, and the development speed is relatively fast. It is possible to develop to 2130 footrill along the arch roadway in a relatively short time for the return airway of 2120 working face of 6# coal seam. In view of the characteristics of unknown fire area scope and degree of spontaneous combustion [27–29], the overall idea of “detecting first, isolating, extinguishing later, and observing the whole process” is adopted to carry out fire area control. The method of radon detection is adopted for fire area detection and the instrument is a CD-1α cup radon detector [30–32]. The detection range is 800 m along the east-west direction of the coal seam and 150 m in the north-south direction, and the total detection area is 12,000 m2. A data processing software package (CDTH software package) is used to perform data processing [27], and a fire range distribution map (Figure 8(c)) is obtained. As can be seen from Figure 8(c), the total area of the fire area is 31,140 m2, and there are 7 high-temperature abnormal zones A, B, C, D, E, F, and G, respectively, with areas of 2,100 m2, 1,500 m2, 11,600 m2, 340 m2, 3,400 m2, 3,800 m2, and 8,400 m2, respectively.Figure 8
Location and fire area of the technical application mine. (a) the enlargement of the blue area in (b). (c) the distribution range of fire area in (a).Table 2
Coal seam features.
Coal seam no.Thickness of coal seamDistance of coal seam (m)StabilityRecoverabilityApparent density (m3)Lithology of the roof and floorDip angle (°)RoofSymbolFloorSymbol13.115.93StableMinable1.35The black sandstoneBlack powder sandstone3624.8614.07StableMinable1.35Medium sandstoneSilstone3531.8639.84StableMinable1.35Coarse sandstone with quartzMedium sandstone3543.2624.4StableMinable1.35Gravel sandstoneSilstone3455.3232.14StableMinable1.35Coarse sandstone with quartzSilstone3563.0334.88StableMinable1.35Gravel sandstoneSilstone35


## 4.2. Application of Fly Ash Slurry

In order to better prepare and inject improved fly ash colloids into the fire area, the gel preparation machine and the mobile adding device are respectively “MYZ-30 ground mobile grouting and gel injection fire preventing and extinguishing system” and “ZHJ-5/1.8 mine-used mobile grouting fire preventing and extinguishing device” developed by the Innovation Team of the Ministry of Education for Prevention and Control of Coal Fire Disaster of Xi’an University of Science and Technology [33], as shown in Figure 9. The area gap is filled with gel, and the total amount of slurry is about 15,350 m3. Table 3 shows the specific gel process in combination with the goal of filling gel in each area.Figure 9
The application of fly ash slurry in the fire area.
(a)(b)Table 3
Technological parameters of injection gel.
No.Filled areaAmount of colloid injected (m3)Quality ratio of water and fly ashAddition amount of gelling agent (%)Addition amount of suspending agent (%)Operating modeMain purposes1Abandoned roadway90001 : (1–1.5)0.10.3Discontinuous glue injection. 3-4 hours of injection, pause for about 1 hourFully exfoliate the water in the colloid to increase the colloid accumulation rate2Existing masonry roadways1350(1–1.5) : 10.30.3Continuous large amount of glue injectionIncrease the fluidity and coverage of colloids in the cracks of high-temperature coal to improve the fire extinguishing effect3Roof falling zone and goaf area5000(1–1.5) : 10.10.3Discontinuous glue injection. 1 hour of injection, pause for about half an hourRelease water from the colloid and fill the fissure with solid material as much as possible


## 4.3. Field Investigation Analyses

When predicting the coal spontaneous combustion process, CO has always been one of the commonly used index gases, and its existence runs through the entire coal seam spontaneous combustion process [7, 34]. The fire area is monitored by means of manual detection through ground gel injection drilling hole and special observation hole. CO gas data in the borehole are collected, and the variation curve of CO gas concentration in the fire area with the treatment progress of the fire area is obtained, as shown in Figure 10.Figure 10
Obtaining CO data through surface drilling monitoring. (a) Monitoring of the ground borehole fire area. (b) Monitoring the variation curve of CO gas concentration.As can be seen from Figure10, the CO gas data in the observation borehole of the fire area obviously decreases and the fire area is effectively controlled rapidly within one month after the drilling and injection work is carried out. The CO gas concentration in the observation borehole in the fire area decreases from the highest 160 ppm to 40 ppm with the increase of injected gel. The CO gas concentration in the observation borehole in the fire area reduces to 0 ppm within two months by continuous injection of the subsequent composite gel. After that, the fire area is continuously observed. The CO gas concentration is stable at 0 ppm all the time. It can be concluded that the fire area is extinguished.


## 5. Conclusions

(1)
The method of adding a suspending agent on the ground and a gelling agent in the pit can effectively improve the long-distance pipeline transportation characteristics of the composite gel slurry, which can ensure good gelling characteristics while solving the sedimentation and plugging of solid material, meeting the actual requirements of on-site firefighting and achieving the purpose of firefighting.(2)
In the modification test of gel, a new suspending agent with XK and XJ as main component (mass ratio XK : XJ = 1 : 3) is developed. It is determined that the optimum addition amounts of the two in the fly ash slurry are 0.3% and 0.1–0.3%, respectively.(3)
The results show that when the coal spontaneous combustion area is filled with improved fly ash colloid fire extinguishing materials, the carbon monoxide concentration in the fire area is significantly reduced. Extinguishing material has excellent long-distance pipeline transportation capacity and fire extinguishing performance. Therefore, it is reasonable to believe that the environmentally and economically improved fly ash colloid fire extinguishing material will be promoted and applied to control the spontaneous combustion of coal effective means.



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*Source: 5695471-2020-06-29.xml*