# A Cleaner Mining Method for Waste Tailings as Paste Materials to Goafs

Authors: Yuxi Liu; Zhixiang Liu; Keming Li; Sijia Deng; Longjun Dong
Journal: Geofluids
 (2020)

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## Abstract

Underground mining is the primary method to obtain economically valuable minerals, but it usually brings a large number of goafs (mined-out voids) and large quantities of waste tailings. The gradual accumulation of mine tailings has attracted worldwide attention because of its occupation and acidification of land, and a large number of goafs often lead to stope instability and ground subsidence. To solve the waste tailing accumulation and ground subsidence, a cleaner mining method—cemented tailing backfilling (CTB)—for filling mining goafs by tailings was proposed. Firstly, the volume of the goafs was detected, and the hydraulic-mechanical coupling properties of the original tailings were tested. Then, a reasonable mix proportion of tailings, binder, and water was determined based on laboratory experiments. Finally, the filling pipe network and filling system were designed according to the actual situation of the mine. This paper provides an environmental and economic method for treating tailing accumulation and preventing ground subsidence. At the same time, it was demonstrated in Linglong Gold Mine (LLGM), and a plan which allows 15.8 service years of nondischarge of tailings was designed in LLGM.


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## Body

## 1. Introduction

The management of mine tailings is a serious environmental issue in various countries [1]. Currently, the mineral resources extraction and the mining scale have constantly expanded to meet the growing demand for consumption [2, 3], which results in the increasing amount of solid tailing waste [4]. A large amount of tailings not only occupies the land but also poisons and acidifies the land [5, 6], which causes serious threats to the lives and property of people [7–9]. At the same time, underground mining often leads to stope instability and ground subsidence [10–12], causing damage to residential buildings and infrastructures [13]. The accumulation of tailings in China is close to 20 billion tons which ranking first in the world, and the subsidence area caused by mining activity has reached 314,765 km2, resulting in 535 deaths and economic losses of $1.9 billion [14]. The issue has aroused the high attention of the national government. In the 18th national congress of the communist party of China (18th CPC National Congress), the Chinese government highlights the construction of ecological civilization at the top of the list.To solve this problem, many scholars carried out a lot of experiments and developed a large number of methods, including (a) covering the tailings with soil for growing plants [15], (b) constructing tailing dam to storage tailings [16], (c) filling the tailings into the goafs [17], and (d) chemical treatment of tailings [18]. Some treatment approaches have been adopted to deal with tailings [19]; however, some methods are not widely used because of significant increases in costs [20]. The tailing storage is reaching the limit, and 1,886t of new tailings need to be processed every day in LLGM. The environmental and economic method to treat accumulation of mine tailings in LLGM is back fill technology, which fills the underground goafs with CTB [21]. The main purposes of stope backfill are (a) improving the working environment [22], (b) preventing surface subsidence [23], (c) reducing ore dilution and mining cycles [24], and (d) mitigating the surface storing problem of tailings [25]. Meanwhile, CTB has lower operating costs and higher strength acquisition compared with other backfill technologies [26]. The 60-75% of the mining waste could be consumed by applying the CTB technology [27]. In fact, the best method of dealing with tailings is to backfill the goafs, and the best strategy to prevent surface subsidence is to use the tailings [28]. Therefore, the solid tailing waste and the goafs are the resources of each other [29]. Figure 1 shows the schematic diagram of cemented tailing backfill. Today, filling the tailings into the goafs is considered a green, environmentally, friendly, and efficient model [30, 31], which can meet the people’s requirements for mining environmental protection and ecological balance [32].Figure 1
Schematic diagram of cemented tailing backfill.The concentration of classified tailings is 50-60%, low concentration filling slurry on the pipe wear more serious with the deepening of the mining [33]. Therefore, the mining processes need to be improved with the full tailings filling technology to achieve safe and efficient recovery [34, 35]. Compared with classified tailings, the advantage of full tailings is that the raw materials are more widely, and the utilization of tailings is higher [36, 37]. In this study, a more economical and cleaner method was proposed, and the specific steps are shown in Figure 2.Figure 2
The specific steps of more economical and cleaner method.This study selected the address of the application experiments at the Linglong Gold Mine (LLGM), because the LLGM has a large number of accumulated tailings and goafs. The LLGM is located in Shandong province including Jiuqu mining area and Xishan mining area. The tailings account for 96 percent in early process of LLGM mining gold mine, filling 67% of the tailings back to new goafs and nearly 33% of the tailings can be filled to the early goafs and deposed laneway [38]. The early goafs of LLGM have the characteristics of strongly concealed, spatial distribution is not obvious, and the roof collapses [39]. The various detection techniques were analyzed and compared based on five main factors: safety, convenience, good working environment, low cost, and high accuracy [40]. Finally, the MDL C-ALS device was used to detect the goafs [41]. The final three dimensional data coordinates, shape, and volume of goafs have been obtained based on the analysis of the scanned data. Result is in accordance with the actual shape of the goafs. C-ALS system can be used to scan goafs automatically from all directions. Then, a three-dimensional model can be built automatically for the goafs based on the obtained data [42]. The results show that the volume of goafs was 5.2 million m3, and the volume of deposed laneway was 0.32 million m3, which is the precondition for backfilling the tailings. Chemical compositions and physical properties of tailings were detected [43]. Then, the most economical and environmental mix proportion was obtained by compressive strength tests [44, 45]. In order to realize the rapid subsidence of the full tailings in the tailing towers and reduce settling time, rapid subsidence tests were carried out [46]. At the same time, a lot of tailings need to be backfilled quickly into the goafs; therefore, rapid solidification tests were carried out [47]. Finally, the backfill plan was designed by the test results and demonstrated by the application experiment.


## 2. Materials and Methods

### 2.1. Tailings

The tailing samples used in this study were collected from the processing plant of LLGM, which specific gravity is 2.78 g/HC3, bulk density is 1.24 g/HC3, porosity is 46.5%, and permeability coefficient is 0.00623 HC/s. Particle size distributions, as the most significant physical characteristic of filling material of tailings [48], were analyzed using a Mastersizer2000 laser particle size analyzer[49]. Figure 3 and Table 1 show the particle size distributions of the tailings.Figure 3
The particle size distributions of full tailings of LLGM (curve 1 is cumulative; curve 2 is incremental).Table 1
Particle size characteristics of unclassified tailings.
Particle size (mm)(0.50,+∞)(0.30, 0.50)(0.10, 0.30)(0.05, 0.10)(0.01, 0.05)(0.001, 0.01)Proportion (%)3.4411.2137.9316.418.5612.46Characteristic diameter (mm)d10d50d90Size (μm)7.137109.58371.68According to the Tabor Study conclusion, the ratio ofCu=d60/d10 is used as the particle size distributions nonuniform coefficient [50]. The nonuniform coefficient of the tailings is 12.73. Therefore, it is easy to transport in filling pipe and can reduce the separation of cement.Another important characteristic of tailings is its chemical composition, which has a pronounced effect on the hardening process of backfill [51]. The mineralogical analysis of tailings and homemade cement was performed via an IEMENS D500 X-ray fluorescence spectrometer, and the result is given in Table 2.Table 2
Chemical compositions of tailings and homemade cement (%).
CompositionsMgAlKCaFeMnLiSiBaNaOtherTailings4.876.102.0525.11.770.510.1011.20.080.97<0.11Homemade cement2.999.671.9836.90.960.310.0714.30.040.65<0.08The main elements of the tailings are Ca (25.1%), Si (11.2%), Al (6.10%), and Mg (4.87%), indicating the high quality and activity of tailings. The sulfide content is very low, indicating that the strength of cemented filling is not affected, and the raw materials are environmental [52, 53].


### 2.2. Binders and Water

Homemade cement (HC) which was made by LLGM was chosen as the binder in this study. The function of homemade cement is similar to that of ordinary portland cement. Compared with ordinary portland cement, HC is stronger and more affordable. The chemical compositions of HC are listed in Table2. Tap water was used to mix the binder and tailings in the laboratory.


### 2.3. Compressive Strength Tests and Bleeding Tests

The ratio of HC to tailings is 1 : 4, 1 : 6, 1 : 8, 1 : 10, 1 : 12, 1 : 16, 1 : 20, and 1 : 30, and the mass concentration is 65%, 67%, 70%, and 75% in laboratory. The mixed slurry was injected into the plastic molds of internal dimension 70 mm∗70 mm∗70 mm. After 24 h of precoagulation, test blocks were taken out of the molds and moved into the box with constant temperature and humidity. For each HC/tailing ratio and mass concentration, there were three different curing periods: 3 d, 14 d, and 28 d. Then, the test blocks were subjected to compressive strength tests using a machine with 50kN loading capability at a displacement rate of 1 mm/min. The mean value of each set of triplicate test blocks was selected as the overall outcome.The bleeding rates are different with variable cement and water contents. In bleeding tests, slurry was poured into a 1000 ml graduated cylinder. Bleeding rate was measured according to the final bleed water on the sample surface, divided by initial water volume.


### 2.4. Rapid Solidification Tests

The amounts of tailings in LLGM are huge. In order to reduce the maintenance time, sodium aluminate cements quick-setting agent (SCQA) was added; its main working principle is to convert the gypsum in cement into Na2SO4. The test mass concentrations depend on the results of compressive strength tests and bleeding tests. SCQA which the content was 3%, 4%, and 5%, respectively, was added. The experimental method and the uniaxial compression test method are the same, and the curing time is 1 day, 3 days, and 7 days, respectively.


### 2.5. Rapid Subsidence Tests

In general, the natural subsidence of tailings is slow. In order to realize the rapid subsidence of the full tailings in the tailing towers, polyacrylamide cationic is considered as flocculants to be added. The polyacrylamide cationic (molecular weight 15 million) was selected in test. The flocculants of 0.02%, 0.03%, and 0.05% concentration, respectively, were prepared. Finally, the slurry was poured into the 1000 ml graduated cylinder. To evaluate the settlement behavior of mixtures, different calibration times were recorded, and readings were taken at 50 ml intervals.


## 2.1. Tailings

The tailing samples used in this study were collected from the processing plant of LLGM, which specific gravity is 2.78 g/HC3, bulk density is 1.24 g/HC3, porosity is 46.5%, and permeability coefficient is 0.00623 HC/s. Particle size distributions, as the most significant physical characteristic of filling material of tailings [48], were analyzed using a Mastersizer2000 laser particle size analyzer[49]. Figure 3 and Table 1 show the particle size distributions of the tailings.Figure 3
The particle size distributions of full tailings of LLGM (curve 1 is cumulative; curve 2 is incremental).Table 1
Particle size characteristics of unclassified tailings.
Particle size (mm)(0.50,+∞)(0.30, 0.50)(0.10, 0.30)(0.05, 0.10)(0.01, 0.05)(0.001, 0.01)Proportion (%)3.4411.2137.9316.418.5612.46Characteristic diameter (mm)d10d50d90Size (μm)7.137109.58371.68According to the Tabor Study conclusion, the ratio ofCu=d60/d10 is used as the particle size distributions nonuniform coefficient [50]. The nonuniform coefficient of the tailings is 12.73. Therefore, it is easy to transport in filling pipe and can reduce the separation of cement.Another important characteristic of tailings is its chemical composition, which has a pronounced effect on the hardening process of backfill [51]. The mineralogical analysis of tailings and homemade cement was performed via an IEMENS D500 X-ray fluorescence spectrometer, and the result is given in Table 2.Table 2
Chemical compositions of tailings and homemade cement (%).
CompositionsMgAlKCaFeMnLiSiBaNaOtherTailings4.876.102.0525.11.770.510.1011.20.080.97<0.11Homemade cement2.999.671.9836.90.960.310.0714.30.040.65<0.08The main elements of the tailings are Ca (25.1%), Si (11.2%), Al (6.10%), and Mg (4.87%), indicating the high quality and activity of tailings. The sulfide content is very low, indicating that the strength of cemented filling is not affected, and the raw materials are environmental [52, 53].


## 2.2. Binders and Water

Homemade cement (HC) which was made by LLGM was chosen as the binder in this study. The function of homemade cement is similar to that of ordinary portland cement. Compared with ordinary portland cement, HC is stronger and more affordable. The chemical compositions of HC are listed in Table2. Tap water was used to mix the binder and tailings in the laboratory.


## 2.3. Compressive Strength Tests and Bleeding Tests

The ratio of HC to tailings is 1 : 4, 1 : 6, 1 : 8, 1 : 10, 1 : 12, 1 : 16, 1 : 20, and 1 : 30, and the mass concentration is 65%, 67%, 70%, and 75% in laboratory. The mixed slurry was injected into the plastic molds of internal dimension 70 mm∗70 mm∗70 mm. After 24 h of precoagulation, test blocks were taken out of the molds and moved into the box with constant temperature and humidity. For each HC/tailing ratio and mass concentration, there were three different curing periods: 3 d, 14 d, and 28 d. Then, the test blocks were subjected to compressive strength tests using a machine with 50kN loading capability at a displacement rate of 1 mm/min. The mean value of each set of triplicate test blocks was selected as the overall outcome.The bleeding rates are different with variable cement and water contents. In bleeding tests, slurry was poured into a 1000 ml graduated cylinder. Bleeding rate was measured according to the final bleed water on the sample surface, divided by initial water volume.


## 2.4. Rapid Solidification Tests

The amounts of tailings in LLGM are huge. In order to reduce the maintenance time, sodium aluminate cements quick-setting agent (SCQA) was added; its main working principle is to convert the gypsum in cement into Na2SO4. The test mass concentrations depend on the results of compressive strength tests and bleeding tests. SCQA which the content was 3%, 4%, and 5%, respectively, was added. The experimental method and the uniaxial compression test method are the same, and the curing time is 1 day, 3 days, and 7 days, respectively.


## 2.5. Rapid Subsidence Tests

In general, the natural subsidence of tailings is slow. In order to realize the rapid subsidence of the full tailings in the tailing towers, polyacrylamide cationic is considered as flocculants to be added. The polyacrylamide cationic (molecular weight 15 million) was selected in test. The flocculants of 0.02%, 0.03%, and 0.05% concentration, respectively, were prepared. Finally, the slurry was poured into the 1000 ml graduated cylinder. To evaluate the settlement behavior of mixtures, different calibration times were recorded, and readings were taken at 50 ml intervals.


## 3. Results and Discussions

### 3.1. Optimum Mix Formulation of the Homemade Cement and Water

The test results of average compressive strength in different mass concentrations and different HC-tailing ratios were shown in Table3.Table 3
The average test results of compressive strength of test blocks (unit: MPa).
Curing periods7 d14 d28 dConcentration65%67%70%75%65%67%70%75%65%67%70%75%Ratio1 : 40.85611.05421.17581.35711.07591.35841.46031.87152.13382.43263.41544.78361 : 60.28500.32540.55470.97530.77120.78341.34121.47651.15511.32372.02763.15621 : 80.20510.30560.37180.51580.39310.55280.69050.87610.65340.77131.13372.04231 : 100.19280.26430.34630.39410.320650.46040.53510.45630.47160.46690.78520.95641 : 120.17090.20230.30150.37250.25270.33270.40180.38360.28570.53380.57190.50361 : 160.10630.12260.20870.20560.13510.15360.21020.21220.15420.18150.21280.28761 : 200.08210.09360.08260.09740.10120.10470.08260.12630.11280.12730.12820.1514The results showed that HC is the decisive factor of the cemented filling. The compressive of test blocks depended on the HC concentration, and the mass concentrations had a small impact. While the HC concentration is the same, compressive strength is positively correlated with curing time and mass concentrations. The strength of the test blocks with a curing period of 28 days is higher than that of the test blocks with a curing period of 7 days, and the higher the mass concentration, the more significant the effect is. According to the mine data, the uniaxial compressive strength of the test block needs to reach 1 MPa or more to ensure safety. When the HC-tailing ratio is 1 : 10 to 1 : 20, the intensity of each group cannot reach 1 MPa. Under the premise of ensuring safety, the lower the content of HC is, the more economical it is, and the lower the mass concentration, the easier it is to transport. When the concentration is 70%, the HC-tailing ratio is 1 : 8 and can reach more than 1 MPa in 28 days. Therefore, 70% concentration was selected in LLGM.The test blocks which HC-tailing ratio is 1 : 8 and the concentration is 70% were prepared. They were subjected to a bleeding test; bleeding rate was only 9.77%. The results show that the filling material in the transport process does not appear segregation.


### 3.2. The OMF of Cement Quick-Setting Agent

After adding cement quick-setting agent, the coagulation cycle is shortened, so the recorded data is 1 day, 3 days, and 7 days. The rapid solidification test (concentration is 70%) results were shown in Table4.Table 4
The average compressive strength of the test blocks (unit: MPa).
HC-tailing ratio1 d (unit: MPa)3 d (unit: MPa)7 d (unit: MPa)Quick-setting agent (%)1 : 60.6331.2651.9693%0.6231.1861.7334%0.6131.1261.5715%1 : 80.580.8251.2883%0.5540.7291.1374%0.4850.7771.0885%1 : 100.3450.6330.8563%0.3130.6370.8124%0.2930.5930.7285%The results show that the SCQA can speed up the solidification rate of the test blocks, but it does not increase the final strength. When the quick-setting agent was added, the test block which HC-tailings are 1 : 10 still cannot reach the safety requirement. While the HC-tailing ratio is 1 : 6 and 1 : 8, the addition of the quick-setting agent is 3%; the effect is best. Solidification time decreased from 14 days and 28 days to 3 days and 7 days, respectively. When the SCQA content increases to 4% and 5%, compressive strength of test blocks decreases. According to the test results and the requirements of LLGM mining method and goafs filling, it can be found that it is reasonable to add 3% SCQA to the 70% concentration filling slurry.


### 3.3. The OMF of Flocculants

The results of rapid subsidence tests were plotted in Figure4.Figure 4
The settlement curve of tailings at different time: (a) the flocculant concentration was 0, (b) the flocculant concentration was 0.2 g/1000 ml, (c) the flocculant concentration was 0.3 g/1000 ml, and (d) the flocculant concentration was 0.5 g/1000 ml.
(a)(b)(c)(d)The results show that the settling time of tailings is 39.8 min without the addition of flocculants. After flocculants are added, the settling rate of full tailings shows a rapid increase. Settling time reduces to 12 to 20 minutes. When flocculants reach to a certain value, there is no obvious change in increasing the amount of flocculants. Settling velocity and stable settling time can be intuitively obtained by Figure3. When the concentration of flocculants was 0.02%, the addition of 2.4 g was the best. The amount of flocculation required for the tailings is 4.8 g/m3. When the concentration of flocculants was 0.03%, the addition of 1.2 g was the best. The amount of flocculation required for the tailings is 3.6 g/m3. When the concentration of flocculants was 0.05%, the addition of 1.2 g was the best. The amount of flocculation required for the tailings is 6 g/m3. Finally, the 0.03% concentration flocculants and the addition of 1.2 g were selected in LLGM.


## 3.1. Optimum Mix Formulation of the Homemade Cement and Water

The test results of average compressive strength in different mass concentrations and different HC-tailing ratios were shown in Table3.Table 3
The average test results of compressive strength of test blocks (unit: MPa).
Curing periods7 d14 d28 dConcentration65%67%70%75%65%67%70%75%65%67%70%75%Ratio1 : 40.85611.05421.17581.35711.07591.35841.46031.87152.13382.43263.41544.78361 : 60.28500.32540.55470.97530.77120.78341.34121.47651.15511.32372.02763.15621 : 80.20510.30560.37180.51580.39310.55280.69050.87610.65340.77131.13372.04231 : 100.19280.26430.34630.39410.320650.46040.53510.45630.47160.46690.78520.95641 : 120.17090.20230.30150.37250.25270.33270.40180.38360.28570.53380.57190.50361 : 160.10630.12260.20870.20560.13510.15360.21020.21220.15420.18150.21280.28761 : 200.08210.09360.08260.09740.10120.10470.08260.12630.11280.12730.12820.1514The results showed that HC is the decisive factor of the cemented filling. The compressive of test blocks depended on the HC concentration, and the mass concentrations had a small impact. While the HC concentration is the same, compressive strength is positively correlated with curing time and mass concentrations. The strength of the test blocks with a curing period of 28 days is higher than that of the test blocks with a curing period of 7 days, and the higher the mass concentration, the more significant the effect is. According to the mine data, the uniaxial compressive strength of the test block needs to reach 1 MPa or more to ensure safety. When the HC-tailing ratio is 1 : 10 to 1 : 20, the intensity of each group cannot reach 1 MPa. Under the premise of ensuring safety, the lower the content of HC is, the more economical it is, and the lower the mass concentration, the easier it is to transport. When the concentration is 70%, the HC-tailing ratio is 1 : 8 and can reach more than 1 MPa in 28 days. Therefore, 70% concentration was selected in LLGM.The test blocks which HC-tailing ratio is 1 : 8 and the concentration is 70% were prepared. They were subjected to a bleeding test; bleeding rate was only 9.77%. The results show that the filling material in the transport process does not appear segregation.


## 3.2. The OMF of Cement Quick-Setting Agent

After adding cement quick-setting agent, the coagulation cycle is shortened, so the recorded data is 1 day, 3 days, and 7 days. The rapid solidification test (concentration is 70%) results were shown in Table4.Table 4
The average compressive strength of the test blocks (unit: MPa).
HC-tailing ratio1 d (unit: MPa)3 d (unit: MPa)7 d (unit: MPa)Quick-setting agent (%)1 : 60.6331.2651.9693%0.6231.1861.7334%0.6131.1261.5715%1 : 80.580.8251.2883%0.5540.7291.1374%0.4850.7771.0885%1 : 100.3450.6330.8563%0.3130.6370.8124%0.2930.5930.7285%The results show that the SCQA can speed up the solidification rate of the test blocks, but it does not increase the final strength. When the quick-setting agent was added, the test block which HC-tailings are 1 : 10 still cannot reach the safety requirement. While the HC-tailing ratio is 1 : 6 and 1 : 8, the addition of the quick-setting agent is 3%; the effect is best. Solidification time decreased from 14 days and 28 days to 3 days and 7 days, respectively. When the SCQA content increases to 4% and 5%, compressive strength of test blocks decreases. According to the test results and the requirements of LLGM mining method and goafs filling, it can be found that it is reasonable to add 3% SCQA to the 70% concentration filling slurry.


## 3.3. The OMF of Flocculants

The results of rapid subsidence tests were plotted in Figure4.Figure 4
The settlement curve of tailings at different time: (a) the flocculant concentration was 0, (b) the flocculant concentration was 0.2 g/1000 ml, (c) the flocculant concentration was 0.3 g/1000 ml, and (d) the flocculant concentration was 0.5 g/1000 ml.
(a)(b)(c)(d)The results show that the settling time of tailings is 39.8 min without the addition of flocculants. After flocculants are added, the settling rate of full tailings shows a rapid increase. Settling time reduces to 12 to 20 minutes. When flocculants reach to a certain value, there is no obvious change in increasing the amount of flocculants. Settling velocity and stable settling time can be intuitively obtained by Figure3. When the concentration of flocculants was 0.02%, the addition of 2.4 g was the best. The amount of flocculation required for the tailings is 4.8 g/m3. When the concentration of flocculants was 0.03%, the addition of 1.2 g was the best. The amount of flocculation required for the tailings is 3.6 g/m3. When the concentration of flocculants was 0.05%, the addition of 1.2 g was the best. The amount of flocculation required for the tailings is 6 g/m3. Finally, the 0.03% concentration flocculants and the addition of 1.2 g were selected in LLGM.


## 4. Application in Linglong Gold Mine

### 4.1. Design of Cleaner Mining Method for Filling Mining Goafs by Tailings

#### 4.1.1. Filling Capacity and Service Life

According to the existing information provided by LLGM, the bulk density of tailings is 1.8 t/m3, and the ore density is 2.78 t/m3. The daily production of Jiuqu mining area is 4000 t with cemented filling mining method, and daily treatment of tailings is 2679 t. The daily production of Xishan is 650 t, and daily treatment of tailings is 435 t. The daily increase in the amount of tailings is 1536 t. To reduce tailing accumulation and prevent surface subsidence, the capacity of new filling system needs to reach 1886 t per day. The working hours are 10 hours per day; the concentration of filling slurry is 70%; the capacity of new filling system requires to 133.72 m3/h.The total volume of goafs is about 5.2 million m3, and the daily filling volume is 1252.32 m3(1886 t). The working periods are 330 days per year; therefore, the service life of filling system is 15.8 years.


#### 4.1.2. Critical Velocity

The floating condition of the solid particles in the level sap flow generally uses the following empirical formula to calculate the critical velocity [54]:
(1)VC=gD1/2γp−γwKϕγpγwλ1/3,whereVC is the critical velocity, g is the acceleration of gravity as 9.8 m/s2, D is the pipe diameter, γp is the slurry density, γw is the water density as 1.0 t/m3, K is the coefficient as 2.0, and ϕ is the particle settlement resistance coefficient; ϕ=ρs−ρwπgd/6ρwvs2, among them, ρs is the particle density as 1.7902 t/m3, d is the pipe diameter as the maximum 0.6 mm, ρw is the water density as 1.0 t/m3, and V is the particle settlement velocity.The concentration is 70%; HC-tailing ratio is 1 : 4, 1 : 6, 1 : 10, and 1 : 16, respectively. The critical velocities were calculated according to equation (1), and the result is 2.02, 2.25, 2.38, and 2.57, respectively, in the range of 2.0 to 2.6 m/s. In practice, the minimum working flow rate of the filling slurry is 10% to 20% higher than the critical velocity. Considering the complicated and comprehensive factors of the goafs of LLGM, the critical velocity of full tailing is 3.0 m/s.According to the previous calculation, the capacity of new filling system requires to 143.72 m3/h; the critical velocity of full tailing is 3.0 m/s. The diameter of filling pipe is calculated according to the data, and the result is greater than 90 mm. Finally, 100 mm diameter pipes were selected as the filling pipes.


#### 4.1.3. Pipeline Resistance

The Jinchuan formula is applicable to the pipe with a diameter of 100 mm, and the error is small. Therefore, Jinchuan formula was adopted to calculate the pipeline resistance in this study [55].
(2)ij=1.125i01+108mt3.96gDγg−1v2Cx1.12,whereij is the filling Slurry hydraulic gradient, i0 is the water hydraulic gradient, v is the flow speed of slurry, Cx is the particle settlement resistance coefficient as 0.997, γg is the solid material density, and mt is the mass concentration of filling slurry.
(3)i0=λLD×v22g,whereλ is the friction coefficient. According to the Nicolas formula multiplied by the coefficient K:
(4)λ=K1•K22lgD/2Δ+1.742,whereK1 is the Pipeline laying coefficient as 1.12, K2 is the pipe joint coefficient as 1.15, g is the acceleration of gravity, D is the pipe diameter, and Δ is the absolute roughness of pipe as 0.01 mm.The flow resistance was calculated according to the equation, and the result is 2.269 KPa/m; therefore, the pipeline pressure in all the middle sections of LLGM is available. According to the design of the filling pipe network, the pipe resistance distribution of goafs filling pipe networks is shown in Figure5(b).Figure 5
(a) The geographical location of the Xishan mining area and (b) the layout and pressure distribution of pipe network of Xishan mining area.
(a)(b)


#### 4.1.4. Wall Thickness

The filling pipe wall thickness is calculated by allowable strength of the material. The tension of filling pipe wall is [55]:
(5)P=∬δnd2sinal=dlδn,whered is the filling pipe diameter, δ is the pipe wall thickness, and m3 is the filling pipe pressure.The inner wall sectional area of the filling pipe is:(6)S=2t×Δl,whereS is the inner wall sectional area, t is the pipe wall thickness, and Δl is the unit length of pipe.The filling pipe in the middle of the roadway is used for a long time, so the seamless steel pipe is used. When the pipe is close to the empty zone, the PVC material pipe is used for the convenience of folding and filling. Through a large number of calculations, the 100 mm diameter of seamless steel pipes was selected, and the wall thickness was 5.0 mm. The 90 mm diameter PVC plastic pipes with a thickness of 10 mm which can meet the technical requirements of pressure 4 MPa were selected.


#### 4.1.5. Filling Pipe Network of Xishan Mining Area

As the resources in the shallow areas are declining, the mines have entered the state of deep resource exploitation successively. But the digging deepens with the pressure appears more and more obvious. Therefore, filling method is necessary in deep mining. First, the filling pipe network of the Xishan Mining Area was designed. The construction of filling system of Xishan mining area should not only consider the production of mining area filling but also the deposed and old laneway filling. The geographical location of the Xishan mining area was shown in Figure5(a); the pressure distribution of pipe network of Xishan mining area was plotted in Figure 5(b).In the natural state, the pressure at each location is shown in Figure5(a); the maximum insufficient pressure is 5.016 MPa. Filling times line of the filling pipe network was calculated; the farthest filling distance of mining area is 4091 m; the maximum vertical drop is 390 m. The filling lines of 190 m, 150 m, 110 m, 70 m, 30 m, -10 m, -50 m, -90 m, and -130 m and middle parts were 62, 32, 23, 21, 11, 10, 13, 12, and 7, respectively. Because of the high filling line, it is necessary to add a booster pump during transportation.


#### 4.1.6. Filling System

Filling station to the adit is about 30-50 m, due to the high pressure, difference is insufficient to deliver the filling slurry to 230 level adit, and therefore, a filling pump is necessary. When slurry is transported to the adit, filling pump need to overcome resistance is 5.13 MPa.Constructing two sets of filling system, a single set of filling capacity is 80 m3/h.LLGM filling system main facilities and equipment are as follows: 4 tailing bin, 4 cement bin, 4 sets of linkage with wind and water activated making pulp device, 4 sets of warehouse with DN150 cast stone wear electrical ball valve, 4 sets of1800×1800 double impeller high concentration mixing drum with motor 30 kw, 4 sets of 3300 × DN200 double-screw feeder with flow 25 m3/h and 7.5 kw motor frequency control, 4 sets of SIWφ125×2.5m double-screw feeder, flow 2~5 m3/h, 1.5 kw motor, frequency control, 4 sets of water pump with flow more than 30 m3/h, 2 sets of 2P mud pump, 4 sets of cement warehouse dust collector, and 2 sets of plunger mud pump.Filling system investment in civil construction costs 7,800,000 Yuan, filling system equipment costs 11,200,000 Yuan (each plunger mud pump costs 800,000 Yuan), pipeline costs 780,000 Yuan, and filling system investment totaling costs 19,780,000 Yuan.


### 4.2. Application Experiments and Economic Analysis

The conclusions obtained from the laboratory may not be applicable to the mine because the geological conditions of the mine are complex and changeable, and the mining methods are not exactly the same. Therefore, application experiment was carried out. Drainage technique is the key of the backfill process; the dehydration technology and dewatering equipment are described in the study for this problem.


#### 4.2.1. Experiment Site

The application experiment was carried out in both the laneway and the goafs for getting the effect in practice. The deposed and old laneway filling was selected in the -70 m middle part section 47 and 50 veins (Figure6), and the goafs filling was selected in the C-50980 goafs and C-51080 goafs (Figure 7).Figure 6
Deposed roadway filling experiment site selection.Figure 7
(a) The vertical projection map of goafs and (b) the floor plan of -565 m.
(a)(b)


#### 4.2.2. Filling Retaining Wall

The structure of retaining wall in Figure8(a), it consists of four parts: observation window, civil cloth, vertical column, and ground retaining blocks. The main material of the retaining wall is wood, the steel pipe was used as a fixed, and the outer layer is wrapped with a wire mesh of 8 mm in diameter. The construction of hanging recycled filling retaining wall is shown in Figure 8(b).Figure 8
(a) The structure of retaining wall and (b) the hanging recycled filling retaining wall.
(a)(b)


#### 4.2.3. Internal and External Drainage of the Stope

The layout of drainage pipes for internal drainage is shown in Figure9(a); the drainage pipe diameter is 100 mm, and the wall thickness is about 10 mm. In the drainage pipes, the diameter is 9 mm, and the holespacing is 57 mm with 50 mm row distance. Because sometimes a drainage pipe is not long enough, it needs a joint extension. Plastic bellows outsourcing filter cloth which specifications is 240 meshes and then in the filter cloth outsourcing layer of sack cloth.Figure 9
(a) The structure of drainage pipes for internal drainage and (b) the equipment of external drainage.
(a)(b)


#### 4.2.4. Backfill Effect

During the application experiment, the effluent flows out through the filling retaining wall and gap, the production of the filling the seepage can be seen, and the effluent water settles formed a very dense layer of mud (Figure10). It is indicated that the backfill of tailings is in good condition, and the application experiment has achieved good results.Figure 10
(a, b) The effect of laneway backfilling. (c, d) The effect of goafs backfilling.
(a)(b)(c)(d)


#### 4.2.5. Backfill Cost

In application experiment goafs and deposed laneway filled with 7014 m3 tailings, the total cost was 217,000 Yuan; filling costs was 30.92 Yuan/m3. The detailed price list is shown in Table 5.Table 5
The cost of backfill tailings.
Serial numberProjectDosageUnit priceFilling costs (Yuan/m3)IHomemade cement0.264 t/m3290 Yuan/t7.66IIAuxiliary materials1Pipe2.5e-3 m/m3200 Yuan/m0.52Filling retaining wall1.7e-2 m3/m3105 Yuan/m31.803Flocculants3.6 g/m30.05 Yuan/g0.184Quick-setting agent7.4 g/m37.2e-4 Yuan/m35.3e-3IIIWater0.7 t/m32.00 Yuan/t1.40IVElectricity0.99 degree/m30.65 Yuan/degree6.45VProductive wages12.05VIDepreciation funds0.87Summation30.92


### 4.3. Economic Benefit

The cleaner mining method was compared with the original method. The cost of using the original method is construction fees, tailing dam management fees, transportation fees, and reclamation fees [56]. The new filling system can fill the amount of 1886 t (1252.3 m3) tailings to the empty area per day. The working days are 330 per year. The amounts of tailings processed each year are 413,259 m3. According to the experience of tailing construction in different regions of China, the unit price of tailing construction fees is 24.06 Yuan/m3, the unit price of tailing management fees is 12 Yuan/m3, the unit price of tailing transportation fees is 4 Yuan/m3, and the unit price of tailing dam reclamation fees is 2.24 Yuan/m2; the annual area of reclamation is 180,000 m2 per year. The final fees are shown in Figure 11(a).Figure 11
(a) The cost of original method and (b) the cost of cleaner method.
(a)(b)The cost of using the cleaner mining method is filling system projects investment budget and filling fees. Filling system project investment budget is 19,780,000 Yuan (the service life is 15.8years, annual depreciation of 1,252,000 Yuan), and the unit price of filling fees is 30.92 Yuan/m3. At the same time, reduce tailing emissions can obtain the state subsidy 15 Yuan/t. The final fees are shown in Figure 11(b).Finally, the new mining method can bring 13,390,888 Yuan economic benefits per year; it also prevented surface subsidence and reduced tailing accumulation. The ecological environmental benefits to humanity are inestimable.


## 4.1. Design of Cleaner Mining Method for Filling Mining Goafs by Tailings

### 4.1.1. Filling Capacity and Service Life

According to the existing information provided by LLGM, the bulk density of tailings is 1.8 t/m3, and the ore density is 2.78 t/m3. The daily production of Jiuqu mining area is 4000 t with cemented filling mining method, and daily treatment of tailings is 2679 t. The daily production of Xishan is 650 t, and daily treatment of tailings is 435 t. The daily increase in the amount of tailings is 1536 t. To reduce tailing accumulation and prevent surface subsidence, the capacity of new filling system needs to reach 1886 t per day. The working hours are 10 hours per day; the concentration of filling slurry is 70%; the capacity of new filling system requires to 133.72 m3/h.The total volume of goafs is about 5.2 million m3, and the daily filling volume is 1252.32 m3(1886 t). The working periods are 330 days per year; therefore, the service life of filling system is 15.8 years.


### 4.1.2. Critical Velocity

The floating condition of the solid particles in the level sap flow generally uses the following empirical formula to calculate the critical velocity [54]:
(1)VC=gD1/2γp−γwKϕγpγwλ1/3,whereVC is the critical velocity, g is the acceleration of gravity as 9.8 m/s2, D is the pipe diameter, γp is the slurry density, γw is the water density as 1.0 t/m3, K is the coefficient as 2.0, and ϕ is the particle settlement resistance coefficient; ϕ=ρs−ρwπgd/6ρwvs2, among them, ρs is the particle density as 1.7902 t/m3, d is the pipe diameter as the maximum 0.6 mm, ρw is the water density as 1.0 t/m3, and V is the particle settlement velocity.The concentration is 70%; HC-tailing ratio is 1 : 4, 1 : 6, 1 : 10, and 1 : 16, respectively. The critical velocities were calculated according to equation (1), and the result is 2.02, 2.25, 2.38, and 2.57, respectively, in the range of 2.0 to 2.6 m/s. In practice, the minimum working flow rate of the filling slurry is 10% to 20% higher than the critical velocity. Considering the complicated and comprehensive factors of the goafs of LLGM, the critical velocity of full tailing is 3.0 m/s.According to the previous calculation, the capacity of new filling system requires to 143.72 m3/h; the critical velocity of full tailing is 3.0 m/s. The diameter of filling pipe is calculated according to the data, and the result is greater than 90 mm. Finally, 100 mm diameter pipes were selected as the filling pipes.


### 4.1.3. Pipeline Resistance

The Jinchuan formula is applicable to the pipe with a diameter of 100 mm, and the error is small. Therefore, Jinchuan formula was adopted to calculate the pipeline resistance in this study [55].
(2)ij=1.125i01+108mt3.96gDγg−1v2Cx1.12,whereij is the filling Slurry hydraulic gradient, i0 is the water hydraulic gradient, v is the flow speed of slurry, Cx is the particle settlement resistance coefficient as 0.997, γg is the solid material density, and mt is the mass concentration of filling slurry.
(3)i0=λLD×v22g,whereλ is the friction coefficient. According to the Nicolas formula multiplied by the coefficient K:
(4)λ=K1•K22lgD/2Δ+1.742,whereK1 is the Pipeline laying coefficient as 1.12, K2 is the pipe joint coefficient as 1.15, g is the acceleration of gravity, D is the pipe diameter, and Δ is the absolute roughness of pipe as 0.01 mm.The flow resistance was calculated according to the equation, and the result is 2.269 KPa/m; therefore, the pipeline pressure in all the middle sections of LLGM is available. According to the design of the filling pipe network, the pipe resistance distribution of goafs filling pipe networks is shown in Figure5(b).Figure 5
(a) The geographical location of the Xishan mining area and (b) the layout and pressure distribution of pipe network of Xishan mining area.
(a)(b)


### 4.1.4. Wall Thickness

The filling pipe wall thickness is calculated by allowable strength of the material. The tension of filling pipe wall is [55]:
(5)P=∬δnd2sinal=dlδn,whered is the filling pipe diameter, δ is the pipe wall thickness, and m3 is the filling pipe pressure.The inner wall sectional area of the filling pipe is:(6)S=2t×Δl,whereS is the inner wall sectional area, t is the pipe wall thickness, and Δl is the unit length of pipe.The filling pipe in the middle of the roadway is used for a long time, so the seamless steel pipe is used. When the pipe is close to the empty zone, the PVC material pipe is used for the convenience of folding and filling. Through a large number of calculations, the 100 mm diameter of seamless steel pipes was selected, and the wall thickness was 5.0 mm. The 90 mm diameter PVC plastic pipes with a thickness of 10 mm which can meet the technical requirements of pressure 4 MPa were selected.


### 4.1.5. Filling Pipe Network of Xishan Mining Area

As the resources in the shallow areas are declining, the mines have entered the state of deep resource exploitation successively. But the digging deepens with the pressure appears more and more obvious. Therefore, filling method is necessary in deep mining. First, the filling pipe network of the Xishan Mining Area was designed. The construction of filling system of Xishan mining area should not only consider the production of mining area filling but also the deposed and old laneway filling. The geographical location of the Xishan mining area was shown in Figure5(a); the pressure distribution of pipe network of Xishan mining area was plotted in Figure 5(b).In the natural state, the pressure at each location is shown in Figure5(a); the maximum insufficient pressure is 5.016 MPa. Filling times line of the filling pipe network was calculated; the farthest filling distance of mining area is 4091 m; the maximum vertical drop is 390 m. The filling lines of 190 m, 150 m, 110 m, 70 m, 30 m, -10 m, -50 m, -90 m, and -130 m and middle parts were 62, 32, 23, 21, 11, 10, 13, 12, and 7, respectively. Because of the high filling line, it is necessary to add a booster pump during transportation.


### 4.1.6. Filling System

Filling station to the adit is about 30-50 m, due to the high pressure, difference is insufficient to deliver the filling slurry to 230 level adit, and therefore, a filling pump is necessary. When slurry is transported to the adit, filling pump need to overcome resistance is 5.13 MPa.Constructing two sets of filling system, a single set of filling capacity is 80 m3/h.LLGM filling system main facilities and equipment are as follows: 4 tailing bin, 4 cement bin, 4 sets of linkage with wind and water activated making pulp device, 4 sets of warehouse with DN150 cast stone wear electrical ball valve, 4 sets of1800×1800 double impeller high concentration mixing drum with motor 30 kw, 4 sets of 3300 × DN200 double-screw feeder with flow 25 m3/h and 7.5 kw motor frequency control, 4 sets of SIWφ125×2.5m double-screw feeder, flow 2~5 m3/h, 1.5 kw motor, frequency control, 4 sets of water pump with flow more than 30 m3/h, 2 sets of 2P mud pump, 4 sets of cement warehouse dust collector, and 2 sets of plunger mud pump.Filling system investment in civil construction costs 7,800,000 Yuan, filling system equipment costs 11,200,000 Yuan (each plunger mud pump costs 800,000 Yuan), pipeline costs 780,000 Yuan, and filling system investment totaling costs 19,780,000 Yuan.


## 4.1.1. Filling Capacity and Service Life

According to the existing information provided by LLGM, the bulk density of tailings is 1.8 t/m3, and the ore density is 2.78 t/m3. The daily production of Jiuqu mining area is 4000 t with cemented filling mining method, and daily treatment of tailings is 2679 t. The daily production of Xishan is 650 t, and daily treatment of tailings is 435 t. The daily increase in the amount of tailings is 1536 t. To reduce tailing accumulation and prevent surface subsidence, the capacity of new filling system needs to reach 1886 t per day. The working hours are 10 hours per day; the concentration of filling slurry is 70%; the capacity of new filling system requires to 133.72 m3/h.The total volume of goafs is about 5.2 million m3, and the daily filling volume is 1252.32 m3(1886 t). The working periods are 330 days per year; therefore, the service life of filling system is 15.8 years.


## 4.1.2. Critical Velocity

The floating condition of the solid particles in the level sap flow generally uses the following empirical formula to calculate the critical velocity [54]:
(1)VC=gD1/2γp−γwKϕγpγwλ1/3,whereVC is the critical velocity, g is the acceleration of gravity as 9.8 m/s2, D is the pipe diameter, γp is the slurry density, γw is the water density as 1.0 t/m3, K is the coefficient as 2.0, and ϕ is the particle settlement resistance coefficient; ϕ=ρs−ρwπgd/6ρwvs2, among them, ρs is the particle density as 1.7902 t/m3, d is the pipe diameter as the maximum 0.6 mm, ρw is the water density as 1.0 t/m3, and V is the particle settlement velocity.The concentration is 70%; HC-tailing ratio is 1 : 4, 1 : 6, 1 : 10, and 1 : 16, respectively. The critical velocities were calculated according to equation (1), and the result is 2.02, 2.25, 2.38, and 2.57, respectively, in the range of 2.0 to 2.6 m/s. In practice, the minimum working flow rate of the filling slurry is 10% to 20% higher than the critical velocity. Considering the complicated and comprehensive factors of the goafs of LLGM, the critical velocity of full tailing is 3.0 m/s.According to the previous calculation, the capacity of new filling system requires to 143.72 m3/h; the critical velocity of full tailing is 3.0 m/s. The diameter of filling pipe is calculated according to the data, and the result is greater than 90 mm. Finally, 100 mm diameter pipes were selected as the filling pipes.


## 4.1.3. Pipeline Resistance

The Jinchuan formula is applicable to the pipe with a diameter of 100 mm, and the error is small. Therefore, Jinchuan formula was adopted to calculate the pipeline resistance in this study [55].
(2)ij=1.125i01+108mt3.96gDγg−1v2Cx1.12,whereij is the filling Slurry hydraulic gradient, i0 is the water hydraulic gradient, v is the flow speed of slurry, Cx is the particle settlement resistance coefficient as 0.997, γg is the solid material density, and mt is the mass concentration of filling slurry.
(3)i0=λLD×v22g,whereλ is the friction coefficient. According to the Nicolas formula multiplied by the coefficient K:
(4)λ=K1•K22lgD/2Δ+1.742,whereK1 is the Pipeline laying coefficient as 1.12, K2 is the pipe joint coefficient as 1.15, g is the acceleration of gravity, D is the pipe diameter, and Δ is the absolute roughness of pipe as 0.01 mm.The flow resistance was calculated according to the equation, and the result is 2.269 KPa/m; therefore, the pipeline pressure in all the middle sections of LLGM is available. According to the design of the filling pipe network, the pipe resistance distribution of goafs filling pipe networks is shown in Figure5(b).Figure 5
(a) The geographical location of the Xishan mining area and (b) the layout and pressure distribution of pipe network of Xishan mining area.
(a)(b)


## 4.1.4. Wall Thickness

The filling pipe wall thickness is calculated by allowable strength of the material. The tension of filling pipe wall is [55]:
(5)P=∬δnd2sinal=dlδn,whered is the filling pipe diameter, δ is the pipe wall thickness, and m3 is the filling pipe pressure.The inner wall sectional area of the filling pipe is:(6)S=2t×Δl,whereS is the inner wall sectional area, t is the pipe wall thickness, and Δl is the unit length of pipe.The filling pipe in the middle of the roadway is used for a long time, so the seamless steel pipe is used. When the pipe is close to the empty zone, the PVC material pipe is used for the convenience of folding and filling. Through a large number of calculations, the 100 mm diameter of seamless steel pipes was selected, and the wall thickness was 5.0 mm. The 90 mm diameter PVC plastic pipes with a thickness of 10 mm which can meet the technical requirements of pressure 4 MPa were selected.


## 4.1.5. Filling Pipe Network of Xishan Mining Area

As the resources in the shallow areas are declining, the mines have entered the state of deep resource exploitation successively. But the digging deepens with the pressure appears more and more obvious. Therefore, filling method is necessary in deep mining. First, the filling pipe network of the Xishan Mining Area was designed. The construction of filling system of Xishan mining area should not only consider the production of mining area filling but also the deposed and old laneway filling. The geographical location of the Xishan mining area was shown in Figure5(a); the pressure distribution of pipe network of Xishan mining area was plotted in Figure 5(b).In the natural state, the pressure at each location is shown in Figure5(a); the maximum insufficient pressure is 5.016 MPa. Filling times line of the filling pipe network was calculated; the farthest filling distance of mining area is 4091 m; the maximum vertical drop is 390 m. The filling lines of 190 m, 150 m, 110 m, 70 m, 30 m, -10 m, -50 m, -90 m, and -130 m and middle parts were 62, 32, 23, 21, 11, 10, 13, 12, and 7, respectively. Because of the high filling line, it is necessary to add a booster pump during transportation.


## 4.1.6. Filling System

Filling station to the adit is about 30-50 m, due to the high pressure, difference is insufficient to deliver the filling slurry to 230 level adit, and therefore, a filling pump is necessary. When slurry is transported to the adit, filling pump need to overcome resistance is 5.13 MPa.Constructing two sets of filling system, a single set of filling capacity is 80 m3/h.LLGM filling system main facilities and equipment are as follows: 4 tailing bin, 4 cement bin, 4 sets of linkage with wind and water activated making pulp device, 4 sets of warehouse with DN150 cast stone wear electrical ball valve, 4 sets of1800×1800 double impeller high concentration mixing drum with motor 30 kw, 4 sets of 3300 × DN200 double-screw feeder with flow 25 m3/h and 7.5 kw motor frequency control, 4 sets of SIWφ125×2.5m double-screw feeder, flow 2~5 m3/h, 1.5 kw motor, frequency control, 4 sets of water pump with flow more than 30 m3/h, 2 sets of 2P mud pump, 4 sets of cement warehouse dust collector, and 2 sets of plunger mud pump.Filling system investment in civil construction costs 7,800,000 Yuan, filling system equipment costs 11,200,000 Yuan (each plunger mud pump costs 800,000 Yuan), pipeline costs 780,000 Yuan, and filling system investment totaling costs 19,780,000 Yuan.


## 4.2. Application Experiments and Economic Analysis

The conclusions obtained from the laboratory may not be applicable to the mine because the geological conditions of the mine are complex and changeable, and the mining methods are not exactly the same. Therefore, application experiment was carried out. Drainage technique is the key of the backfill process; the dehydration technology and dewatering equipment are described in the study for this problem.


### 4.2.1. Experiment Site

The application experiment was carried out in both the laneway and the goafs for getting the effect in practice. The deposed and old laneway filling was selected in the -70 m middle part section 47 and 50 veins (Figure6), and the goafs filling was selected in the C-50980 goafs and C-51080 goafs (Figure 7).Figure 6
Deposed roadway filling experiment site selection.Figure 7
(a) The vertical projection map of goafs and (b) the floor plan of -565 m.
(a)(b)


### 4.2.2. Filling Retaining Wall

The structure of retaining wall in Figure8(a), it consists of four parts: observation window, civil cloth, vertical column, and ground retaining blocks. The main material of the retaining wall is wood, the steel pipe was used as a fixed, and the outer layer is wrapped with a wire mesh of 8 mm in diameter. The construction of hanging recycled filling retaining wall is shown in Figure 8(b).Figure 8
(a) The structure of retaining wall and (b) the hanging recycled filling retaining wall.
(a)(b)


### 4.2.3. Internal and External Drainage of the Stope

The layout of drainage pipes for internal drainage is shown in Figure9(a); the drainage pipe diameter is 100 mm, and the wall thickness is about 10 mm. In the drainage pipes, the diameter is 9 mm, and the holespacing is 57 mm with 50 mm row distance. Because sometimes a drainage pipe is not long enough, it needs a joint extension. Plastic bellows outsourcing filter cloth which specifications is 240 meshes and then in the filter cloth outsourcing layer of sack cloth.Figure 9
(a) The structure of drainage pipes for internal drainage and (b) the equipment of external drainage.
(a)(b)


### 4.2.4. Backfill Effect

During the application experiment, the effluent flows out through the filling retaining wall and gap, the production of the filling the seepage can be seen, and the effluent water settles formed a very dense layer of mud (Figure10). It is indicated that the backfill of tailings is in good condition, and the application experiment has achieved good results.Figure 10
(a, b) The effect of laneway backfilling. (c, d) The effect of goafs backfilling.
(a)(b)(c)(d)


### 4.2.5. Backfill Cost

In application experiment goafs and deposed laneway filled with 7014 m3 tailings, the total cost was 217,000 Yuan; filling costs was 30.92 Yuan/m3. The detailed price list is shown in Table 5.Table 5
The cost of backfill tailings.
Serial numberProjectDosageUnit priceFilling costs (Yuan/m3)IHomemade cement0.264 t/m3290 Yuan/t7.66IIAuxiliary materials1Pipe2.5e-3 m/m3200 Yuan/m0.52Filling retaining wall1.7e-2 m3/m3105 Yuan/m31.803Flocculants3.6 g/m30.05 Yuan/g0.184Quick-setting agent7.4 g/m37.2e-4 Yuan/m35.3e-3IIIWater0.7 t/m32.00 Yuan/t1.40IVElectricity0.99 degree/m30.65 Yuan/degree6.45VProductive wages12.05VIDepreciation funds0.87Summation30.92


## 4.2.1. Experiment Site

The application experiment was carried out in both the laneway and the goafs for getting the effect in practice. The deposed and old laneway filling was selected in the -70 m middle part section 47 and 50 veins (Figure6), and the goafs filling was selected in the C-50980 goafs and C-51080 goafs (Figure 7).Figure 6
Deposed roadway filling experiment site selection.Figure 7
(a) The vertical projection map of goafs and (b) the floor plan of -565 m.
(a)(b)


## 4.2.2. Filling Retaining Wall

The structure of retaining wall in Figure8(a), it consists of four parts: observation window, civil cloth, vertical column, and ground retaining blocks. The main material of the retaining wall is wood, the steel pipe was used as a fixed, and the outer layer is wrapped with a wire mesh of 8 mm in diameter. The construction of hanging recycled filling retaining wall is shown in Figure 8(b).Figure 8
(a) The structure of retaining wall and (b) the hanging recycled filling retaining wall.
(a)(b)


## 4.2.3. Internal and External Drainage of the Stope

The layout of drainage pipes for internal drainage is shown in Figure9(a); the drainage pipe diameter is 100 mm, and the wall thickness is about 10 mm. In the drainage pipes, the diameter is 9 mm, and the holespacing is 57 mm with 50 mm row distance. Because sometimes a drainage pipe is not long enough, it needs a joint extension. Plastic bellows outsourcing filter cloth which specifications is 240 meshes and then in the filter cloth outsourcing layer of sack cloth.Figure 9
(a) The structure of drainage pipes for internal drainage and (b) the equipment of external drainage.
(a)(b)


## 4.2.4. Backfill Effect

During the application experiment, the effluent flows out through the filling retaining wall and gap, the production of the filling the seepage can be seen, and the effluent water settles formed a very dense layer of mud (Figure10). It is indicated that the backfill of tailings is in good condition, and the application experiment has achieved good results.Figure 10
(a, b) The effect of laneway backfilling. (c, d) The effect of goafs backfilling.
(a)(b)(c)(d)


## 4.2.5. Backfill Cost

In application experiment goafs and deposed laneway filled with 7014 m3 tailings, the total cost was 217,000 Yuan; filling costs was 30.92 Yuan/m3. The detailed price list is shown in Table 5.Table 5
The cost of backfill tailings.
Serial numberProjectDosageUnit priceFilling costs (Yuan/m3)IHomemade cement0.264 t/m3290 Yuan/t7.66IIAuxiliary materials1Pipe2.5e-3 m/m3200 Yuan/m0.52Filling retaining wall1.7e-2 m3/m3105 Yuan/m31.803Flocculants3.6 g/m30.05 Yuan/g0.184Quick-setting agent7.4 g/m37.2e-4 Yuan/m35.3e-3IIIWater0.7 t/m32.00 Yuan/t1.40IVElectricity0.99 degree/m30.65 Yuan/degree6.45VProductive wages12.05VIDepreciation funds0.87Summation30.92


## 4.3. Economic Benefit

The cleaner mining method was compared with the original method. The cost of using the original method is construction fees, tailing dam management fees, transportation fees, and reclamation fees [56]. The new filling system can fill the amount of 1886 t (1252.3 m3) tailings to the empty area per day. The working days are 330 per year. The amounts of tailings processed each year are 413,259 m3. According to the experience of tailing construction in different regions of China, the unit price of tailing construction fees is 24.06 Yuan/m3, the unit price of tailing management fees is 12 Yuan/m3, the unit price of tailing transportation fees is 4 Yuan/m3, and the unit price of tailing dam reclamation fees is 2.24 Yuan/m2; the annual area of reclamation is 180,000 m2 per year. The final fees are shown in Figure 11(a).Figure 11
(a) The cost of original method and (b) the cost of cleaner method.
(a)(b)The cost of using the cleaner mining method is filling system projects investment budget and filling fees. Filling system project investment budget is 19,780,000 Yuan (the service life is 15.8years, annual depreciation of 1,252,000 Yuan), and the unit price of filling fees is 30.92 Yuan/m3. At the same time, reduce tailing emissions can obtain the state subsidy 15 Yuan/t. The final fees are shown in Figure 11(b).Finally, the new mining method can bring 13,390,888 Yuan economic benefits per year; it also prevented surface subsidence and reduced tailing accumulation. The ecological environmental benefits to humanity are inestimable.


## 5. Conclusions

Huge amounts of tailings are stored on the surface land, resulting land acidifications and poisons. The goafs can lead to stope instability and ground subsidence, causing damage to residential buildings and infrastructures. This study proposed a cleaner mining method for filling mining goafs by tailings in LLGM, located in Shandong province, China. The mechanical performance of the CTB was related to the slurry concentration and HC/tailing ratio. The compressive strength tests showed that C material was the decisive factor of the cemented filling. In order to realize continuous rapid filling tailings, adding the cements quick-setting agent and flocculants was necessary. The result of tests showed that 70% slurry concentration, 1 : 8 HC/tailing ratio, 3% cement quick-setting, and 0.03% concentration flocculants were reasonable mix proportion.The filling system which can service 15.8 years for LLGM was designed. Then, application experiment was a success in LLGM. Finally, the economic benefits of the cleaner mining method and the old method were compared. The cleaner mining method costs 13,390,888 Yuan less than the old method per year. But when analyzing the related physical parameters of tailings, the tailing parameters are regarded as deterministic parameters. This may affect the subsequent test results. In future research, the uncertainty of the parameters could be taken into consideration. Overall, the cleaner mining method is a greener and economically productive way to be widely used in the future. When analyzing the related physical parameters of tailings, the tailing parameters are regarded as deterministic parameters. This may affect the subsequent test results. In future research, the uncertainty of the parameters could be taken into consideration.



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*Source: 8857290-2020-10-22.xml*