Experimental Study on Rheological Properties and Strength Variation of High Concentration Cemented Unclassified Tailings Backfill

,is experimental study presents the rheological properties and strength characteristics of cemented unclassified tailings backfill (CUTB). ,e particle size distribution and chemical properties of tailings from the Shizhuyuan lead-zinc mine were examined experimentally. A series of rheological properties and uniaxial compressive strength (UCS) tests were conducted to study the relations between the rheological properties of CUTB and two factors of cement-tailings ratio (c/t) and solid content (SD). ,e two-factor nonrepetitive analysis of variance (ANOVA) method was used to study the sensitivity of rheological properties to two factors of c/t and SD. Relations between UCS performance of CUTB and c/t, SD, and curing time (CT) were discussed. Results indicate that CUTB samples exhibit obvious shear thinning characteristics and the rheological process is the result of multiple rheological model composites. Yield stress and viscosity of CUTB increase with the increase of SD and c/t as quadratic. ,e solid content is the most important factor for the rheological properties of CUTB, followed by c/t. UCS of CUTB increases exponentially with the increase of SD and increases with c/t as quadratic. ,e larger the ratio of c/t, the greater the influence of the CT on the increasing strength of CUTB.,e smaller the c/t, the slower the increase of the CUTB’s strength with the increase of the SD. ,e findings of this study can provide the efficient mix proportion of backfill slurry for the backfill mining design, so as to have better performance of the underground mining structure and reduce the cost of backfill mining.


Introduction
Mine backfill has gained increasing popularity in the mining industry all over the world due to the fact that it provides ground support for mining operations, reduces ore dilution, and allows safe disposal of tailings [1][2][3]. Generally, the cemented paste backfill (CPB) is made of complex composite composed of filtered tailings, water, and binders [4] and is transported underground to mine stopes by gravity delivered or pumped through a network of pipelines [5]. e CPB usually uses classified tailings as aggregate leads to a problem of low utilization of tailings. Meanwhile, superfine tailings remaining after classification has always been a treatment and utilization challenges due to safety and environmental problems [6]. Considering the advantages of CPB based on high concentration unclassified tailings, such as realizing the full utilization of tailings, no bleeding, no segregation, and no sedimentation of CPB slurry, this method has become one of the vital development directions of backfill technology. Rheological properties and mechanical properties are two key factors in high concentration unclassified backfill technology, which significantly influence the pipeline transportation of slurry and safety of adjacent stope [7,8].
e transport pattern of the CPB slurry in the pipeline is different from the traditional two-phase fluid, and it is generally believed to exist in the form of structural flow. It is a common method to calculate the rheological parameters to get the resistance of pipeline by CPB rheology [9]. Numerous studies on the rheological behaviors of backfill slurry have been carried out. Some experimental studies indicated that the slump flow could reflect the rheological properties of backfill samples intuitively [10,11]. However, the slump flow cannot reflect the rheological properties from an academic point of view. High concentration slurry is generally considered to be a non-Newtonian fluid. Hence, the viscosity and yield stress are two vitally important parameters, which are often used to evaluate the rheological properties of high concentration slurry [12]. ere are many factors that can determine the rheological properties of CPB slurry including external factors [13,14] (such as temperature and loading pressure) and internal factors (such as solid content and cement content of the CPB mixtures and properties of the CPB mixture constituents) [12,[15][16][17]. Furthermore, some researchers reported that the time-dependent rheological behavior significantly influences the transportability of CPB slurry due to the fact that the rheological properties of CPB slurry change with time [7,17,18]. e uniaxial compressive strength test is most widely used to study the mechanical properties of CPB, which is a simple and economical test method [19]. Numerous previous experimental studies concentrate a lot on the components (tailings, cement, admixture, and water) of CPB mixture which influence the UCS of CPB [2,4,[19][20][21][22][23][24][25][26][27][28][29][30][31][32][33][34][35][36][37]. Megan et al. [38] investigated that curing with elevated temperature and effective stress can significantly increase the UCS of CPB. Yilmaz et al. [8] reported that the stope depth has a positive effect on UCS of CPB, and the UCS of CPB samples near the stope's bottom is always higher than those located at the top of the stope. Qi et al. [39] proposed an intelligent modeling framework for the prediction of CPB's mechanical properties using machine learning algorithms and genetic algorithm. Cao et al. [40][41][42] and Wang et al. [43,44] investigated the influence of structural factors (filling time, filling interval time, and filling surface angle) on UCS of CPB.
Although reports about the properties of CPB are numerous, all of them show no quantitative relationship between rheological property parameters and the two factors (solid content (SD) and cement-to-tailings ratio (c/t)), especially for high concentration cemented unclassified tailings backfill (CUTB). is study aims to characterize the rheological property parameters and strength behavior of CUTB using the control variable method. Rheology test on CTUB with different SD and c/t ratios was conducted to reveal the relationship between rheological property parameters and the two factors. e sensitivity of rheological properties to different influencing factors was analyzed by the two-factor nonrepetitive analysis of variance (ANOVA) method. Additionally, the major factors such as the c/t, SD, and curing time (CT) were considered for uniaxial compressive experiments, and relationships between the above three factors and the UCS of CUTB samples were studied. e research results provide a theoretical basis and data reference for an efficient and effective tailings backfill design of such mine. China. e density and bulk density of the studied tailings are 2550 and 1720 kg/m 3 , respectively. e particle size of the tailings was analyzed by S3500 (Microtrac, Florida, USA) laser particle analyzer. e results are shown in Figure 1(a). It was found that the particle composition is D 10 � 5.85 μm, D 90 � 362.9 μm, and D 50 � 104.7 μm, which is a typical coarse-grained tailing.

Materials and Experimental Method
e unevenness coefficient C u � 28.051, and the particle size gradation is good. e chemical compositions of the tailings were tested by X-ray diffraction, and the results were shown in Figure 1(b) and Table 1 Table 2. Municipal tap water was used as mixing water to prepare CUTB samples.

CUTB Samples Preparation.
CUTB samples (360 in total) were prepared by blending and homogenizing the lead-zinc unclassified tailings, OPC, and water (Table 3). e mixtures were then casted in metal cubes with dimensions of 70.7 mm × 70.7 mm × 70.7 mm. e CUTB samples were cured in a humidity chamber at 20°C and 95% relative humidity for different curing times (7, 28, and 56 days).

Rheology Testing.
To investigate the rheological properties of the CUTB slurry, the stress and strain of 20 groups of CUTB slurry mixes were tested by MCR52 rheometer (Anton Paar, Graz, Austria), and the rotor was measured with ST24-2D/2V-30 paddle rotor (diameter/height: 20/ 40 mm). e operating software was RheoCompass rheometer software. e experiment adopts the controlled shear rate (CSR) mode for parameter design. Compared with the test method for controlling the shear stress (CSS), the range of the slurry rheological characteristic curve of the CCR method is more comprehensive, and the rheological properties of the whole process of the slurry transition from the low-speed state to the high-speed state can be reflected. e measurement parameters are set to non-Newtonian fluid mode. e prepared CUTB slurry was poured into a cylindrical glass beaker (D/H: 95/122 mm) and bubbles were removed in the mix. e CUTB samples were tamped. e shear time was set to 120s, and the shear rate increased linearly from 0 to 10 2 s − 1 . e temperature was 20°C at room temperature to avoid the effects of temperature changes. e software automatically may save the yield stress and fluid viscosity data, and the operating software can automatically generate the rheological curve after each experimental test is completed. e RheoCompass rheometer software can form a corresponding linear fitting curve to monitor the output shear stress-shear rate curve and viscosity-shear rate curve in real time.

Uniaxial Compressive
Testing. UCS tests of CUTB samples were performed using an electrohydraulic pressure testing machine (Xinluda, Wuxi, China) with a 300 WR loading capacity for uniaxial compression chamber test; the loading rate was set to 0.5 mm/min according to ASTM C39 [45].

Rheological Properties Parameter Results of CUTB
Samples. Carrying out research on the rheological properties of the unclassified tailings slurry to obtain rheological data (such as viscosity and yield stress) can provide good theoretical support for the fluidity of the slurry, the ease of pipeline transportation, and the design of the transportation pipeline. At the same time, the mix proportion range that meets the needs of engineering is obtained by rheological test, which also provides a reference for the compressive strength test. e yield stress is the adhesion and friction between the particles in the slurry. When the shear stress acting on the slurry is higher than the yield stress, the slurry begins to flow [46]. e yield stress can be tested directly by rheometer and calculated by the maximum torque measured by the rheometer and the size of the mixing blade. e calculation formula was listed in equation (1), and calculation results were listed in Table 4.
where τ is the yield stress of the CUTB slurry, M 0 is the maximum torque of blade, h is the height of the mixing blade, and d is the diameter of the mixing blade.
Considering that the slurry is always in the dynamic process during the rheological test, apparent viscosity at the moment cannot effectively and comprehensively reflect the rheological properties of CUTB slurry. erefore, the arithmetic means of viscosity throughout the shear time were used to reflect the rheological property of CUTB slurry and calculation was listed in equation (2). e corresponding calculation results were listed in Table 4.
where η is the viscosity of CUTB slurry and n is the number of test records.   Figure 1: Fundamental characteristics of the studied tailings: (a) particle size distribution curve; (b) X-ray diffraction curve.    [47], and the apparent viscosity reflects the degree of shear stress at a given shear rate. e apparent viscosity of the Newtonian material is independent of the shear rate. For Bingham or pseudoplastic materials, the apparent viscosity is usually not a fixed value but decreases as the shear rate increases. e apparent viscosity and shear rate curve were obtained automatically by RheoCompass software. Part of the results is shown in Figure 2 due to the limited space. It is evident from Figure 2(a) that the apparent viscosity of the slurry is positively correlated with the solid content. e variation of CUTB slurry's apparent viscosity is not obvious at the low SDs (72-76 wt.%), but it is significantly increased at the high SDs (78-80 wt.%).
In addition, when the value of solid contents is lower than 78 wt.%, the variation of the CUTB slurry's apparent viscosity with shear rate can be divided into three phases. e first phase is a rapid decrease in apparent viscosity (0-10 s − 1 ). e initial apparent viscosity of the CUTB slurry is very large, and it is necessary to destroy the internal floc structure to make the slurry flow. At this phase, the apparent viscosity drops sharply, and the flow capacity increases rapidly. e second phase is a linear decrease in apparent viscosity (10-60 S − 1 ). During this phase, as the shear rate increases, the CUTB slurry's apparent viscosity decreases slowly and tends to be in a dynamic stability state. At last, the dynamic stability of apparent viscosity is the third phase, which exhibits shear thinning behavior. An explanation for this behavior is that the fine particles inside the slurry are continuously dispersed, collided, aggregated, and redispersed under the action of higher shear rate [18], and the slurry behaves as Newtonian. Furthermore, the similar characteristics of CUTB slurry at different c/t ratio also can be seen from Figure 2 When the value of solid contents is higher than 78 wt.%, the variation of the apparent viscosity of CUTB slurry with increased shear rate can be divided into two stages: rapid reduction (0-20 s − 1 ) and gradual decrease (20 s − 1 ). is variation showed a noticeable derivative trend, and with the shear rate increasing, the slurry behaves as Bingham or similar Bingham after a short shear.
It can be noticed from Figure 2(b) that the CUTB slurry's apparent viscosity changed as a derivative function at different c/t ratio. is behavior indicates that the c/t ratio has little effect on the apparent viscosity of the slurry and controlling appropriate solid content of CUTB slurry is the key in pipeline transportation.

Analysis of Yield Stress.
e two-factor nonrepetitive analysis of variance was used to study the influence degree of c/t ratio and solid content on the yield stress of CUTB slurry, and the ANOVA data and analyzed results were listed in Tables 5 and 6, respectively. Given the value of significant level (α) of 0.05, check the critical value F checklist to get F 0.05 (3, 12) � 3.49 and F 0.05 (4, 12) � 3.26.
It can be seen from Table 6 that the value of F x (3.974) is larger than F 0.05 (3, 12) � 3.49 and F Y � 58.758 is larger than F 0.05 (4, 12) � 3.26, which indicate that factor X (cement-totailings ratio) and factor Y (solid content) both significantly influence the yield stress of CUTB slurry. Additionally, the influence of c/t ratio is significantly larger than the influence of SD on the yield stress of CUTB slurry according to the comparison of the differential values between F (F X and F Y ) and F 0.05 . e CUTB slurry based on unclassified tailings contains a certain number of particles with a smaller particle size which forms a skeleton structure as to resist shearing when the slurry is static. is structure will make the slurry have a certain cohesion, and the yield stress is the force that enables the slurry to begin to flow as the torque increases. Figure 3 represents the fitted histogram of solid content and yield stress of CUTB slurry. One can say that the value of the increase in yield stress significantly increases with the solid content increasing from 72% to 80%. Setting the cement-totailing ratio of 1 : 08 as an example, the value of yield stress increases from 26.79 Pa to 43.02 Pa when the solid content increased from 72% to 74%, and the values of increase were not obvious. When the solid content increased from 74% to 80% respectively, the corresponding slurry yield stress with a   Advances in Materials Science and Engineering c/t ratio of 1 : 08 increased from 43.02 Pa to 77.59 Pa, 224.92 Pa, and 388.85 Pa. e values of the increase in yield stress were approximately 35 Pa, 182 Pa, and 346 Pa, which became more and more big. In addition, the variations of the yield stress of CUTB slurry with c/t ratios of 1 : 04, 1 : 12, and 1 : 16 are similar to the CUTB's c/t ratio of 1 : 08. e reason behind this increase is that the yield stress is the resistance that needs to be overcome during the initial flow of the slurry. is resistance is caused by the adhesion and friction between the particles inside the slurry. When the interdependence and frictional effects between the particles increase or decrease, the yield stress will increase or decrease. e high-quality concentration of the slurry is due to the high solid content, the free water content of the lubrication is relatively low, resulting in increased flow resistance, and the yield stress of the mixture is also increasing.
e cement-to-tailings ratio was considered as constant to better investigate the relationship between the yield stress of CUTB slurry and different solid content. Quadratic fitting of the variation of yield stress was conducted and the relevant correlation coefficient (R 2 ) and equation parameters were listed in Table 7.
It was found from Table 7 that quadratic fitting methods have great regression degrees. e average value of multiple R 2 is greater than 0.97, which shows that the relationship between solid content and yield stress of CUTB slurry could be well expressed as the quadratic equation, and the relevant expression can be defined as where Y is the yield stress of the CUTB slurry, SD is the solid content, and c 1 , b 1 , and a 1 are the fitting parameters related to the influence of solid content and yield stress factors. Figure 4 shows the fitted histogram curves between cement-to-tailings ratio and yield stress of CUTB slurry. One can say from the results that, for a given SD in the mix, the yield stress of CUTB slurry increases as the c/t ratio of CUTB slurry increases. Among them, when the SD of the slurry was lower than 78 wt.%, the increased range of yield stress of CUTB slurry was not obvious. For CUTB slurry with solid content higher than 78 wt.%, the increased range of yield stress of CUTB slurry had a significant increase.
To better investigate the relationship between yield stress values and cement-to-tailings ratio for CUTB slurry, the solid content was fixed. Quadratic fitting of the variation of yield stress was conducted and the relevant correlation coefficient (R 2 ) and equation parameters were listed in Table 8.
It was found from Table 8 that quadratic fitting methods have great regression degrees. e corresponding average value of multiple R 2 is larger than 0.98, which shows that the relationship between c/t ratio and yield stress of CUTB slurry could be well expressed as the quadratic equation. e relevant expression can be definedas where Y is the yield stress of the CUTB slurry and c/t is the cement-to-tailings ratio. d 1 , e 1 , and f 1 are the fitting parameters related to the influence of cement-to-tailings ratio and yield stress factors.

Analysis of Mean
Viscosity. e two-factor nonrepetitive analysis of variance (ANOVA) was used to study the influence degree of c/t ratio and solid content on the viscosity of CUTB slurry, and the analyzed results were listed in Table 9. Given the value of significant level (α) of 0.05, check the critical value F checklist to get F 0.05 (3, 12) � 3.49 and F 0.05 (4, 12) � 3.26. Table 10 shows that F x (4.134) and F Y (61.429) are both larger than corresponding critical value F α . erefore, the two factors have a significant influence on the mean viscosity of CUTB slurry. Additionally, the influence of SD is significantly larger than the influence of c/t ratio on the viscosity of CUTB slurry according to the comparison of the differential values between F (F X and F Y ) and F 0.05 . Figure 5 shows the histogram curves between cement-totailings ratio and the mean viscosity of CUTB slurry. One can say that mean viscosities of the CUTB slurry with low solid contents (72-76 wt.%) have lower values (3.35-16.37 Pa·s). As expected, the higher the solid contents  (78-80 wt.%) yield, the higher the mean viscosities (22.14-80.83 Pa·s). is is mainly due to the fact that the higher solid content means a higher aggregate content, which increases the probability of collision between fine particles of CUTB while also increasing the internal friction of CUTB. Additionally, when the solid contents are lower than 76%, the mean viscosity does not change significantly as the solid content increases. However, the mean viscosity of CUTB increases obviously when the solid contents are higher than 76%, which is 2-3 times the CUTB with solid content of 76%. With the solid contents of 80%, the variation of mean viscosity does not conform to the overall variation law. e cement-to-tailings ratio was considered as constant to better study the variation of the viscosity of CUTB slurry with different solid content. Quadratic fitting of the variation of mean viscosity was conducted and the relevant correlation coefficient (R 2 ) and equation parameters were listed in Table 11.
It was found from Table 11 that the quadratic fitting methods have great fitting degrees. e corresponding multiple R 2 are larger than 0.98, which shows that the relationship between solid content and slurry viscosity could be well expressed as the quadratic equation, and the relevant expression can be defined as where V is the viscosity of the CUTB slurry, SD is the solid content, and c 2 , b 2 , and a 2 are the fitting parameters related to the influence of solid content and viscosity factors. It is evident from Figure 6 that as the solid content of CUTB slurry increases from 72 wt.% to 80 wt.%, the mean viscosity of the slurry with a c/t ratio of 1 : 04, 1 : 08, 1 : 12, and 1 : 16 increases from 5.56 to 80.83 Pa·s, from 4.08 to 56.49 Pa·s, from 3.42 to 55.32 Pa·s, and from 3.35 to 54.52 Pa·s, respectively. is behavior can be explained by the viscosity as an apparent characteristic of the internal structure of the slurry, which may hinder the flow performance. Its size depends mainly on the amount of flocculation structure inside the slurry and the degree of damage. e high hydration of the slurry to produce more hydrated     products will increase the internality of the slurry. Additionally, the adhesion between the particles forms a flocculated structure and a network structure, thereby hindering the flow of the particles and increasing the viscosity of the slurry. e solid content was considered as constant to better study the variation of the viscosity of CUTB slurry with different cement-to-tailings ratio. Quadratic fitting of the variation of viscosity was conducted and the relevant correlation coefficient (R 2 ) and equation parameters were listed in Table 12. Table 12 shows that the quadratic fitting methods have great regression degrees. e corresponding multiple R 2 are larger than 0.98, which shows that the relationship between cement-to-tailings ratio and slurry viscosity could be well expressed as the quadratic equation, and the relevant expression can be defined as where V is the viscosity of the CUTB slurry mixes, SD is the solid content, and d 2 , e 2 , and f 2 are the fitting parameters related to the influence of cement-to-tailings ratio and viscosity factors.

Analysis of the Variation Law of Backfill's Compressive
Strength. e solid content, cement-to-tailings ratio, and curing time are the three main factors affecting the strength of CUTB. In this study, single-factor nonlinear regression analysis was performed on the experimental results using the SPSS Statistics software (IBM, Armonk, USA) to evaluate the quantitative relationship between the CUTB's strength and the three factors. e regression models were obtained by using SPSS software according to the comparison between the value of the complex correlation coefficient (R 2 ) and test coefficient index (F) of different regression models.

Uniaxial Compressive Strength Results of CUTB Samples.
A total of 360 CUTB samples were prepared and conducted to UCS testing for this study. Each group was tested 6 times, and the average results were obtained for comparison. e UCS values obtained from the testing were shown in Table 13.
One can note from Table 13 that the CUTB strength increases remarkably when the c/t ratio increases from 1 : 04 to 1 : 16, regardless of solid content and curing time. e c/t ratio is the main factor affecting the compressive strength of the CUTB. With the increase of curing time, the cement can produce a large number of hydration products such as C-S-H and ettringite with strong gelling properties during the hydration reaction and the internal compactness increases the strength of the CUTB. In addition, the strength of the CUTB increases as the solid content increases. is behavior can be explained by the fact that the solid content of the slurry is essentially the amount of water content, and a part of the water in the slurry acts as adsorption to connect the particles in the slurry into a net and another part plays a hydration role to form the strength of the CUTB. From the microscopic point of view, the formation of voids in the CUTB is mainly due to the action of water, while the voids in  Controlling the applicable solid content of CUTB is of great importance in improving the safety of pipeline transportation while satisfying the requirements of strength. erefore, it is especially important to study the relationship between the solid content and the CUTB's strength.

Effect of Solid Content.
Histograms and exponential fitting curves of the CUTB strength of different solid content and curing time are shown in Figure 7. As expected, the compressive strength of CUTB samples increases with increasing SD for a given c/t ratio. For an SD of 72 wt.% at a constant c/t ratio of 1 : 04, the strength of 7-day cured CUTBs is 2.13 MPa. When the SD increased from 72 wt.% to 80 wt.%, the corresponding UCS became 4.32 MPa, causing a 50.7% increase in the strength of CUTB. As the SD is increased from 72 wt.% to 80 wt.%, UCS increases from 2.84 to 6.58 MPa for 28 days and from 3.11 to 6.83 MPa for 56 days, respectively. Under the condition of high solid content, the strength of the CUTB samples increases exponentially with the increase of solid content. e smaller the cement-totailing ratio is, the slower the backfill's strength increases with the solid content. When the cement-to-tailings ratio is less than or equal to 1 : 08, the backfill's strength increases slowly with the increase of solid content. e cement-to-tailings ratio and curing time values were considered as constants to study the variation of the CUTB strength in five levels of solid content (72%, 74%, 76%, 78%, and 80%). Exponential fitting of the variation of mixture viscosity was conducted and the relevant correlation coefficients (R 2 ) were listed in Table 14. Table 14 shows that an obviously exponential relationship exists between CUTB's solid content and UCS of CUTB. e corresponding multiple correlation coefficients (R 2 ) for the exponential fit were 0.968, 0.988, 0.978, and 0.994, respectively. e relationship between the SD and UCS of the CUTB samples can be expressed as an exponential equation, and the relevant expression can be defined as where UCS is the uniaxial compressive strength of the CUTB samples and SD is the solid content. A 1 and B 1 are the fitting parameters related to the influence of solid content and UCS factors. ese fitting parameters were listed in Table 15. Figure 8 represents the quadratic fitted scatter plot of strength gain of CUTB samples versus c/t ratio with different curing time and solid content. One can observe from the performed test results       e compressive strength of the CUTB samples with the high c/t ratio increases faster with the curing time because the cement can produce a large amount of C-S-H and ettringite with strong gelling properties during the hydration reaction. e hydration product increases the degree of internal compaction and increases the strength of the CUTB samples. e solid content and curing time values were considered as constants to better study the UCS variation of CUTB samples with different cement-to-tailings ratios. e relationship between the CUTB's strength and c/t ratio shows quadratic properties, and the relevant correlation coefficients (R 2 ) were listed in Table 16.

Effect of Cement-to-Tailings Ratio.
It was found from Table 16 that quadratic function regression has high fitting degrees whose responding multiple R 2 are larger than 0.95. Moreover, it was also found experimentally that the UCS performance of CUTB samples increases with increasing cement-to-tailings ratio, and when the curing time is 7 days and the c/t ratio is lower than 1 : 12, the regression model reflects that the strength of the CUTB increases slowly with the increase of the c/t ratio. e relationship between c/t ratio and UCS of CUTB samples could be well expressed as the quadratic equation, and the relevant expression can be defined as where c/t is the cement-to-tailings ratio; A 2 , B 2 , and C 1 are the fitting parameters related to the influence of c/t and UCS factors. e equation parameters were listed in Table 17.

Effect of Curing Time.
Dotted-line graphs of the backfill's strength of different curing time and c/t ratio are shown in Figure 9. Since the curing time is only 7, 28, and 56 days, the three-point data do not draw a trend line, so no relevant data fitting analysis has been conducted. Instead, one can observe from results that as curing time increases, the compressive strength performance of CUTB samples increases.
For instance, the strengths of CUTB with a cement-totailings ratio of 1 : 04 and solid content of 80 wt.% are 4.32, 7.11, and 7.34 MPa for curing times of 7, 28, and 56 days, respectively. At a fixed cement-to-tailings (1 : 04), these values were 2.13, 2.84, and 3.11 MPa; 2.45, 3.58, and 3.97 MPa; 2.86, 4.26, and 4.52 MPa; and 3.84, 6.58, and 6.83 MPa for a solid content of 72%, 74%, 76%, and 78%, respectively. As expected, for a given c/t ratio and curing time, the higher the solid content, the higher the increase rate of the backfill's strength. In addition, when the curing time is larger than 28 days, the backfill's strength increases slowly.

Prediction Model of CUTB's Compressive Strength.
In order to establish the prediction model of CUTB's compressive strength under the change of cement-to-tailings ratio and solid content at different curing times, nonlinear regression analysis was used and relevant expressions at different curing times (7 d, 28 d, and 56 d) can be defined in equations (9) UCS 56d � 89.2 − 2.3SD − 179.7(c/t) + 50.5(c/t) 2 + 2.5SD(c/t), where c/t is the cement-to-tailings ratio and SD is the solid content.
In the above prediction model, the multiple R 2 of equations (9)-(11) are 0.993, 0.988, and 0.990, respectively. erefore, these models can well predict the variation of CUTB's compressive strength under the change of cement-to-tailings ratio and solid content at different curing times.

Conclusions
Based on the results, the following conclusions can be drawn: (1) CUTB samples exhibit shear thinning characteristics irrespective of cement-to-tailings ratio and solid content. e rheological process of the CUTB slurry is the result of multiple rheological model composites and the rheological properties can be the characterizations to distinguish the high concentration slurry mixes and low concentration slurry mixes. increase of SD and c/t and the relationship between two rheological property parameters and two factors can be expressed as the quadratic equation. (3) e sensitivity of rheological properties to SD is strong, and the sensitivity is weak to c/t. e yield stress and mean viscosity of CUTB slurry with a solid content of 78 wt.% are significantly larger than the slurry with a solid content of 76 wt.%, which is 2 to 3 times larger. ese results show that the CUTB's flowability with solid content below 76 wt.% is better. (4) When the other two factors are fixed, the UCS of CUTB increases exponentially with the increase of solid content, while it increases with the cement-totailings ratio as quadratic. (5) e larger c/t CUTB, the more significant effect of the curing time on the CUTB's strength. When the c/ t gets smaller, the CUTB's strength increases slowly with solid content increasing. When the curing time is larger than 28 d, the backfill's strength is not significantly affected by the c/t ratio and solid content, and the strength increases slowly.

Data Availability
e data used to support the findings of this study are included within the article.

Conflicts of Interest
e authors declare that there are no conflicts of interest in this paper.