# Calibration of Discrete Element Simulation Parameters for Powder Screw Conveying

Authors: Changpu Shen; Yongxiang Li; Xuemeng Xu
Journal: Journal of Engineering
 (2021)

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## Abstract

In order to obtain the accurate contact parameters in the simulation process of powder screw conveying, this paper took wheat flour as an example, based on the discrete element JKR (Johnson-Kendall-Roberts) contact model, and directly calibrated the simulation contact parameters in the process of screw conveying in response to the mass flow rate of wheat flour. Firstly, the simulation density of wheat flour particles was calibrated, and the simulation density of wheat flour particles was 1320 kg/m. Then, Plackett-Burman experiment was used to screen out the parameters that had significant influence on the mass flow rate: surface energy JKR, coefficient of static friction between wheat flour and wheat flour, and the coefficient of static friction between wheat flour and stainless steel. The second-order regression model of mass flow rate and significance parameters was established and optimized based on Box-Behnken experiment, and the optimal combination of significance parameters: JKR was obtained to be 0.364; the static friction coefficient of wheat flour to wheat flour was 0.437; and the static friction coefficient of wheat flour to stainless steel was 0.609. Finally, the calibration parameters were used for simulation. By comparing the mass flow rate of simulation and experiment, the relative error of the two was 1.37%. The simulation and experiment flow rate values at different rotating speeds (60 r/min, 80 r/min, 100 r/min, 120 r/min, and 140 r/min) were further compared, and the errors were all within 3%. The method of directly calibrating the simulation contact parameters through the screw conveying process can improve the accuracy of screw conveying simulation, and providing a method and basis for powder contact parameters calibration and screw conveying simulation of wheat flour.


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## Body

## 1. Introduction

With small particle size and large specific surface area, the powder has good solubility, dispersibility, adsorbability, and chemical reactivity, etc. It is widely used in many fields such as chemical industry, medicine, food, electronics, and aviation. The powder is usually transported by screw conveyors when it is packaged and used as raw material. Experimental studies, theoretical analysis, and numerical simulation are usually used to study the screw conveying process of powder. Because the movement of powder particles in the screw conveyor is extremely complicated, it is difficult to describe the force and movement of powder particles through experimental research and theoretical analysis. The numerical simulation can make up for the deficiency of experimental research and theoretical analysis and can analyze the force and movement of powder in the process of screw conveying in detail. Moreover, it can also determine the effect of specific parameters on performance through sensitivity analysis and experimental detail reproduction.Since the discrete element method was proposed by Cundall and Strack in 1980 [1], it has been used as an effective analytical method to study the structure and motion law of discontinuous particulate matter. In recent years, the gradually mature discrete element method (DEM) and relevant numerical analysis software can track and analyze the movement of particles very well in multi-scale structures and can greatly reduce the cost of bulk material research. Discrete element method has been widely used in agriculture [2–8], pharmaceutical [9], mining [10–12], steel manufacturing [13], and other industries. When the discrete element method or the corresponding numerical analysis software is used to analyze, the built particle model needs to define its physical parameters, mainly including intrinsic parameters (density, elastic modulus, Poisson’s ratio), and parameters (static friction coefficient, crash recovery coefficient, rolling friction coefficient) between particles and particles, and particles and equipment. However, due to the different physical parameters of various material particles, it is necessary to calibrate the material particles before the numerical simulation. At present, a variety of materials have been calibrated at home and abroad, such as soybean [14, 15], corn [16–18], wheat [19, 20], rice [21, 22], soil [23, 24], and coal [25, 26], etc., but the parameters of these materials are calibrated through the angle of repose, rather than directly through the equipment under normal working conditions. Due to the fluidity, adhesion, compressibility, and other characteristics of the bulk materials, the parameters of the materials are calibrated only through the angle of repose. When the parameters calibrated by this method are simulated, the numerical simulation error will be large. Using the discrete element parameters calibrated by angle of repose to simulate the screw conveying [27], the relative error of the mass flow rate in the simulation and experiment is up to 8.5%. If the corresponding equipment is used to directly calibrate the material parameters, the error of numerical simulation caused by parameter calibration can be greatly reduced.In this paper, wheat flour is used as the transport material; considering the cohesion between wheat flour particles, JKR contact model is adopted. On this basis, the simulation density of wheat flour particles was calibrated by experiment and numerical simulation firstly, and then the discrete element simulation contact parameters of wheat flour particles were calibrated by Plackett-Burman, steepest climb, and Box-Behnken experiments to obtain the optimal parameter combination. Finally, the optimal parameter combination is used to conduct the numerical simulation of the screw conveying at different speeds, and the mass flow rate of the numerical simulation is compared with the mass flow rate of the experiment, and the error is analyzed.


## 2. JKR Contact Model

In this paper, wheat flour was used as the material transported by screw. The particle size was small and contained 13%–15% water. There were van der Waals force, liquid bridge force, and electrostatic force among the particles, which made the particle surface cohesive. Hertz contact theory only considers the elastic deformation of particle interaction, but does not consider the surface adhesion between particles. In this paper, JKR contact model is adopted to consider the adhesion between particles, and surface energy is introduced to represent the adhesion between particles.In the conveying process of wheat flour, the force between wheat flour particles is composed of normal force and tangential force, and the normal force is divided into normal damping force and normal elastic force, and the tangential force is divided into tangential damping force and tangential elastic force. The JKR contact physical model of the interaction between the two particles is shown in Figure1.Figure 1
JKR physical model. (a) JKR contact model. (b) JKR contact force.
(a)(b)JKR contact theory is an extension of Hertz contact theory. Based on Hertz contact theory, the interaction between two particles is analyzed as follows:(1)
Tangential damping force of two particles based on JKR modelFτd is(1)Fτd=−256cτkτm∗vτrel¯.Here,cτ, kτ, m∗, and vτrel¯ represent the tangential damping coefficient, the tangential stiffness coefficient, the equivalent mass, and the tangential component of the relative velocity of the contact particle, respectively.Among them, the damping coefficientcτ is(2)cτ=lneln2e+π2.Here,e and π represent the particle recovery coefficient and the circumference ratio, respectively.Tangential stiffnesskτ is(3)kτ=8G∗R∗α.Here,G∗, R∗, and α represent the particle equivalent shear modulus, the particle equivalent radius, and the particle normal overlap, respectively.The equivalent shear modulusG∗ is(4)G∗=2−vj2Gi+2−vj2Gj.Here,vi, vj, Gi, and Gj represent the velocity of particle i, the velocity of particle j, the shear modulus of grain i, and the shear modulus of particle j, respectively.Equivalent particle radiusR∗ is(5)1R∗=1Ri+1Rj.Here,Ri and Rj represent the radius of particle i and the radius of particle j, respectively.Equivalent particle massm∗ is(6)1m∗=1mi+1mj.Here,mi and mj represent the mass of particle i and the mass of particle j, respectively.(2)
Tangential elastic force of two particles based on JKR modelFτ is(7)Fτ=kτδτ.Here,δτ and kτ represent the particle tangential overlap and the average value, respectively.The tangential force is related to the friction force, and the friction force has a great influence on the simulation, so the static friction forceff is(8)f=μsFn.Here,μs and Fn represent the coefficient of static friction and the normal force, respectively.Rolling friction can be explained by the torque on the contact surfaceTi as(9)Ti=−μrRiωi.Here,μr, Ri, and ωi represent the rolling friction coefficient, the radius of particle i, and the angular velocity of particle i, respectively.(3)
The normal damping force of two particles based on JKR modelFnd is(10)Fnd=−256cnknm∗vnrel¯.Here,cn, kn, m∗, and vnrel¯ represent the normal damping coefficient, the normal stiffness coefficient, the equivalent mass, and the tangential component of the relative, respectively.Among them, the normal stiffnesskn is(11)kn=8E∗R∗α.Here,E∗, R∗, and α represent the particle equivalent elastic modulus, the particle equivalent radius, and the particle normal overlap, respectively.Equivalent modulus of elasticityE∗ is(12)1E∗=1−vj2Ei+1−vj2Ej.Here,vi, vj, Ei, and Ej represent the velocity of particle i, the velocity of particle j, the elastic modulus of particle i, and the elastic modulus of particle j, respectively.(4)
In the JKR model, the normal phase elasticity can effectively reflect the viscoelastic characteristics between particles, so the normal phase elastic forceFJKR is(13)FJKR=−4πγE∗α3/2+4E∗3R∗α3.Here,π, γ, α,E∗, and R∗ represent the circumference ratio, the surface energy, the particle normal overlap, the particle equivalent elastic modulus, and the particle equivalent radius, respectively.


## 3. Discrete Element Simulation Parameter Calibration

### 3.1. Particle Density Calibration of Wheat Flour

Particle density is an essential and critical parameter in discrete element simulation of powder. However, it is difficult to obtain accurate particle density through experiments and there is a large error in simulation. In this paper, in order to obtain the accurate particle density of discrete element simulation of wheat flour, the volume density of wheat flour was obtained through the experiment firstly, and then the particle density of wheat flour was adjusted through simulation, so that the volume density of wheat flour obtained through experiment was equal to that of the simulated particle, so as to obtain the particle density of wheat flour.


#### 3.1.1. Experimental Measurement of Wheat Flour Particle

The particle density of wheat flour was measured with a container and an electronic scale. The container has a diameter of 0.1 m, a height of 0.195 m, and a volume of 0.00152 m³. The measurement steps of bulk density of wheat flour are shown in Figure2:(1)
Weigh the empty containermmc(2)
Free fall the wheat flour from the entrance into the container until it overflows(3)
Scrape off the excess wheat flour and weigh the totalmmt(4)
According toρc=mt−mc/Vc, measured wheat flour bulk density ρc=500.13 kg/m³Figure 2
Measurement of wheat flour volume density. (a) Container weight measurement. (b) Pour the flour until it overflows. (c) Measurement of total weight of container and wheat flour.
(a)(b)(c)


#### 3.1.2. The Particle Density Calibration

The volume density of wheat flour was measured as 500.13 kg/m3 through experiments. During the simulation process, the density of wheat flour simulated particles was adjusted to make its volume density as 500.13 kg/m3. During the calibration of this density, a container with a radius of 0.1 m and a height of 0.1 m was created, and a scraper was used to scrape off the excess simulation particles above the container. The calibration process of wheat grain density is shown in Figure 3.Figure 3
Calibration process of wheat flour simulated grain density. (a) Particles injection start. (b) Particles injection end. (c) Particles stand still. (d) Particles scraping begin. (e) Particles scraping process. (f) Particles scraping end.
(a)(b)(c)(d)(e)(f)Particle injection: particles are generated from the particle factory and fall freely into the container, so that particles fill the container and overflow.Particles stand still: after the particles are filled, let them stand and freely overflow for a period of time to make the particles completely still.Scrape particles: at the end of standing, the scraper moves to scrape off excess particles so that the particles in the container are flush with the mouth of the container.Through the calibration of wheat flour simulated grain density, the grain density is 1320 kg/m³.


### 3.2. Calibration of Wheat Flour Particle Contact Parameters

Using wheat flour flow rate as the response value, the discrete element simulation contact parameters of the wheat flour particles were calibrated directly in the screw conveying process by Plackett-Burman, steepest climbing, and Box-Behnken experiments, and the optimal combination of contact parameters was obtained. The discrete element simulation of wheat flour and other powders provides a reference.


#### 3.2.1. Mass Flow Rate Experiment of Wheat Flour

In this experiment, the screw conveyor of Jingu Co., Ltd. was used. The pitch is 0.1 m; the inner shaft diameter is 0.035 m; the outer diameter of the blade is 0.12 m; the inner diameter of the shaft cylinder is 0.13 m; the gap is 0.005 m; and the length of the feeding section is 0.5 m; and speed range is 60 r/min–150 r/min. The rotation speed of this screw conveyor is 100 rad/s. The weight of wheat flour was measured using a load cell (RS485 plane load cell: Hengyuan Sensor Technology Co., Ltd.; weighing range 0–50 kg; sampling frequency 10–30 Hz; measurement error ±0.003 kg). The data is set to record data every 0.1 s and the duration is set to 20 s. After the data recording is completed, the wheat flour time-quality data is derived to calculate the mass flow rate of wheat flour. The mass flow rate value of the wheat flour was experimented 5 times to take the average value. The mass flow rate value of the wheat flour screw conveyor was measured to be 0.805 kg/s. The experimental process and time-mass curve are shown in Figure4.Figure 4
Determination of mass flow rate of wheat flour screw conveyor. (a) Mass flow rate experiment of wheat flour. (b) Time-mass curve
(a)(b)


#### 3.2.2. Simulation Model and Parameters

(1) Simulation parameters. Based on the settings of powder particle and stainless steel discrete element simulation parameters at home and abroad [28–32] and the built-in GEMM database of EDEM software, the variation range of each simulation parameter in this study is shown in Table 1. Combining the literature related to powder simulation [33–35] and the theory of particle scaling, the intrinsic parameters required for the simulation are set to wheat flour density of 1320 kg/m3, wheat flour Poisson’s ratio of 0.25, and wheat flour shear modulus of 6.0 × 107 Pa. The contact parameters of the material vary greatly with the density, shape, and particle size of the material, which cannot be obtained by consulting the physical property manual or literature, and using virtual experiments for calibration.Table 1
Parameters required in DEM simulation.
Simulation parametersValueDensity of wheat flour/(kg·m−3)1320Poisson’s ratio of wheat flour0.2–0.4Shear modulus of wheat/Pa1.1 × 107–6 × 107Density of stainless steel/(kg·m−3)7800Poisson’s ratio of stainless steel0.3Shear modulus of stainless steel/Pa7 × 1010Wheat flour-wheat flour restitution coefficient0.15–0.55Wheat flour-wheat flour static friction coefficient0.2–0.8Wheat flour-wheat flour rolling friction coefficient0.05–0.25Wheat flour-stainless steel restitution coefficient0.15–0.55Wheat flour-stainless steel static friction coefficient0.2–1.0Wheat flour-stainless steel rolling friction coefficient0.1–0.8JKR0.1–0.5(2) Simulation model. This simulation refers to the actual physical model and is appropriately simplified. The design dimensions of the hopper and spiral are the same as the actual physical model. Due to simulation conditions and time constraints, the particles radius was magnified two times, and the circle of the enlarged particles was set to 0.1 mm. Spherical particles were used for the simulation [36–39]. The simulation model is shown in Figure 5. During the simulation, the contact model is “Hertz-Mindlin with JKR,” the simulation time is 10 s, the particle generation method is dynamic, the generation rate is set to 200,0000/s, the number of generations is set to 4000000, and after the generation is completed, the rotation speed of the screw shaft is set, and the rotation speed of the screw shaft is 100 rad/s. After the simulation calculation is completed, the mass flow rate sensor in the software post-processing is used to measure the spiral conveyance of wheat flour.Figure 5
Simulation of wheat flour screw conveying. (a) Simulation process. (b). Post-processed mass flow rate.
(a)(b)


#### 3.2.3. Design of Parameter Calibration Simulation Experiment

(1) Plackett-Burman experiment. Plackett-Burman design is a two-level partial experimental design. Factor significance is determined by examining the relationship between the target response and each factor, and comparing the differences between the two levels of each factor. This Plackett-Burman design screens the significance of simulated contact parameters based on the response rate of wheat spiral conveying mass flow rate. The low level is set to the original level, and the high level is set to twice the low level. The experiment parameters are shown in Table 2.Table 2
Parameters of Plackett-Burman experiment.
SymbolParametersLow levelHigh levelAWheat flour-wheat flour restitution coefficient0.150.3BWheat flour-wheat flour static friction coefficient0.20.4CWheat flour-wheat flour rolling friction coefficient0.050.1DWheat flour-stainless steel restitution coefficient0.150.3EWheat flour-stainless steel static friction coefficient0.20.4FWheat flour-stainless steel rolling friction coefficient0.10.2GJKR0.10.5V1Virtual parameters 1−11V2Virtual parameters 2−11V3Virtual parameters 3−11V4Virtual parameters 4−11The design and results of Plackett-Burman are shown in Table3. The analysis of the results by Design Expert software is used to obtain the significance of each contact parameter as shown in Table 4. From Table 4, it can be seen that JKR, the static friction coefficient of wheat flour-wheat flour, and the static friction coefficient of wheat flour-stainless steel P<0.01 have extremely significant effects on the spiral mass flow rate, while the remaining parameters P>0.05 have minimal effects on the spiral mass flow rate. In order to facilitate subsequent experiments, only the three parameters with the most significant impact (P<0.01) are considered in the steepest climbing and Box-Behnken experiments. The rest of the parameters combined with the relevant literature [20, 23, 24, 34] take the values (wheat flour-wheat flour recovery coefficient 0.2, wheat flour-wheat flour rolling friction coefficient 0.15, wheat flour-stainless steel recovery coefficient 0.2, and wheat flour-stainless steel rolling friction coefficient 0.15) for the steepest climbing and response surface experiment design.Table 3
Design and results of Plackett-Burman experiment.
Running sequenceABCDEFGV1V2V3V4Mass flow rate (kg/s)1−11−111−1111−1−10.803721−1111−1−1−11−111.10063−111−1111−1−1−110.8108411−1−1−11−111−1−11.129151−111−1111−1−1−11.14446−1−1−1−1−1−1−1−1−1−1−11.119711−1111−1−1−11−11.00368000000000001.02429111−1−1−11−111−11.0007101−1−1−11−111−1110.89511−1−1−11−111−11111.093112−1−11−111−1111−11.030713−1111−1−1−11−1111.032Table 4
Analysis of the significance of parameters in Plackett-Burman experiment.
ParametersEffectSum of squaresContribution/%SignificanceA0.0640.0127.8964B−0.1000.03119.4543C0.0130.0010.3077D0.0320.0031.9756E−0.1460.03640.8741F0.0430.0063.6375G−0.1110.03723.8332(2) Steepest climbing experiment. After the Plackett-Burman experiment, the steepest climbing experiment is performed according to the screened significance parameters so that it can quickly enter the vicinity of the optimal value. The steepest climbing experiment starts from the center point of the PB experiment, and the climbing step length is determined according to the regression coefficient obtained from the PB experiment. In order to approach the optimal value as quickly as possible, the climbing step length is usually taken as a larger value. The selected steps and results of this climbing experiment are shown in Table 5. According to the results in Table 5, it can be seen that the relative error of the mass flow rate at the 3rd level is the smallest, and the relative error from the 2nd to the 4th level changes from large to small and then becomes larger. Therefore, the 3rd level is selected as the center point, and the 2nd and 4th levels are follow-up response surface design at low and high levels.Table 5
Design and results of steepest ascent experiment.
No.JKRWheat flour-wheat flour rolling friction coefficientWheat flour-stainless steel static friction coefficientMass flow rate (kg/s)Relative error (%)10.10.20.21.18847.5820.20.40.40.96119.3830.30.60.60.7911.7440.40.80.80.7496.9650.51.01.00.67715.9(3) Box-Behnken experiment and regression model. Based on the results of the steepest climbing experiment and the principle of response surface design, the low, medium, and high levels of significant parameters were selected for the experiment design, and three center points were selected to evaluate the error. The Box-Behnken experiment results are shown in Table 6. Using Design Expert to establish a second-order regression equation with three significant parameters and the mass flow rate value is(14)Q=1.6+0.35H−1.8J−1.1K+0.036HJ+0.088HK−0.074JK−0.452H2+1.153J2+1.538K2.Table 6
Design and results of Box-Behnken experiment.
Running serial numberWheat flour-wheat static friction coefficient (H)Coefficient of static friction of wheat flour-stainless steel (J)JKR (K)Mass flow rate (kg/s)10000.799120000.8053−10−10.838140−1−10.9718510−10.795260110.75370−110.94048−1−100.9475901−10.7903100000.803111100.716212−1100.7925131−100.865514−1010.8006151010.7648Box-Behnken experiment model analysis results are shown in Table7. According to the results in Table 7, the fitted model P<0.005; JKR surface energy (H), static friction coefficient between wheat flour particles (J), and static friction coefficient of wheat flour-stainless steel (K), the quadratic term of JKR surface energy (H2), and the quadratic term of the static friction coefficient between wheat flour particles (J2) are all less than 0.05, indicating that each parameter has a significant effect on the mass flow rate, and the regression model is valid. The coefficient of variation CV = 0.72% in the experiment, which indicates that the experiment has higher reliability. The determination coefficient R2 = 0.9828; the adjusted determination coefficient Adjusted R2 = 0.9520; it shows that the model can truly reflect the actual situation. The experiment precision is Adep Precision = 18.42, which shows that the model has good accuracy.Table 7
ANOVA of quadratic polynomial model of Box-Behnken experiment.
Source of variationMean squareFreedomQuadratic sumF valueP valueModel0.006390.008531.830.0007H0.007010.007026.360.0037J0.056610.0566212.69<0.0001K0.002310.00238.760.0315HJ8.1 × 10–618.1 × 10–60.03050.8682HK0.000010.00000.04730.8364JK8.7 × 10–618.7 × 10–60.03270.8637H20.001210.00124.530.0867J20.007910.007929.500.0029K20.000910.00093.280.1299Residual0.001350.0003Lack of fit0.001330.000448.640.0202Pure error0.000029 × 10–6Sum0.077614R2 = 0.9828. Adjusted R2 = 0.9520. Predicted R2 = 0.7287. CV = 0.72%. Adep Precision = 18.42According to the results in Table8, under the premise of ensuring the model is good, remove the terms that have no significant effect on the mass flow rate. The results of the analysis of variance after optimizing the model are shown in Table 8. The misfit term P=0.0279; the coefficient of variation CV = 1.91%; Coefficient R2 = 0.9712; Adjusted R2 = 0.9552; Predicted R2 = 0.9131; experiment precision Adep Precision = 23.5. It can be seen that the model has good fit, reliability, and accuracy, which has been improved to some extent before optimization. The regression equation after optimization is(15)Q=1.435+0.429H−1.769J−0.171K−0.481H2+1.124J2.Table 8
ANOVA of the modified model of Box-Behnken experiment.
Source of variationMean squareFreedomQuadratic sumF ValuePvalueModel0.075450.015160.73<0.0001H0.007010.007028.280.0005J0.056610.0566228.17<0.0001K0.002310.00239.390.0135H20.001410.00145.550.0430J20.007510.007530.220.0004Residual0.002290.0002Lack of fit0.002270.000335.170.0279Pure error0.000029 × 10–6Sum0.077614R2 = 0.9712. Adjusted R2 = 0.9552. Predicted R2 = 0.9131. CV = 1.9%. Adep Precision = 23.5


## 3.1. Particle Density Calibration of Wheat Flour

Particle density is an essential and critical parameter in discrete element simulation of powder. However, it is difficult to obtain accurate particle density through experiments and there is a large error in simulation. In this paper, in order to obtain the accurate particle density of discrete element simulation of wheat flour, the volume density of wheat flour was obtained through the experiment firstly, and then the particle density of wheat flour was adjusted through simulation, so that the volume density of wheat flour obtained through experiment was equal to that of the simulated particle, so as to obtain the particle density of wheat flour.


### 3.1.1. Experimental Measurement of Wheat Flour Particle

The particle density of wheat flour was measured with a container and an electronic scale. The container has a diameter of 0.1 m, a height of 0.195 m, and a volume of 0.00152 m³. The measurement steps of bulk density of wheat flour are shown in Figure2:(1)
Weigh the empty containermmc(2)
Free fall the wheat flour from the entrance into the container until it overflows(3)
Scrape off the excess wheat flour and weigh the totalmmt(4)
According toρc=mt−mc/Vc, measured wheat flour bulk density ρc=500.13 kg/m³Figure 2
Measurement of wheat flour volume density. (a) Container weight measurement. (b) Pour the flour until it overflows. (c) Measurement of total weight of container and wheat flour.
(a)(b)(c)


### 3.1.2. The Particle Density Calibration

The volume density of wheat flour was measured as 500.13 kg/m3 through experiments. During the simulation process, the density of wheat flour simulated particles was adjusted to make its volume density as 500.13 kg/m3. During the calibration of this density, a container with a radius of 0.1 m and a height of 0.1 m was created, and a scraper was used to scrape off the excess simulation particles above the container. The calibration process of wheat grain density is shown in Figure 3.Figure 3
Calibration process of wheat flour simulated grain density. (a) Particles injection start. (b) Particles injection end. (c) Particles stand still. (d) Particles scraping begin. (e) Particles scraping process. (f) Particles scraping end.
(a)(b)(c)(d)(e)(f)Particle injection: particles are generated from the particle factory and fall freely into the container, so that particles fill the container and overflow.Particles stand still: after the particles are filled, let them stand and freely overflow for a period of time to make the particles completely still.Scrape particles: at the end of standing, the scraper moves to scrape off excess particles so that the particles in the container are flush with the mouth of the container.Through the calibration of wheat flour simulated grain density, the grain density is 1320 kg/m³.


## 3.1.1. Experimental Measurement of Wheat Flour Particle

The particle density of wheat flour was measured with a container and an electronic scale. The container has a diameter of 0.1 m, a height of 0.195 m, and a volume of 0.00152 m³. The measurement steps of bulk density of wheat flour are shown in Figure2:(1)
Weigh the empty containermmc(2)
Free fall the wheat flour from the entrance into the container until it overflows(3)
Scrape off the excess wheat flour and weigh the totalmmt(4)
According toρc=mt−mc/Vc, measured wheat flour bulk density ρc=500.13 kg/m³Figure 2
Measurement of wheat flour volume density. (a) Container weight measurement. (b) Pour the flour until it overflows. (c) Measurement of total weight of container and wheat flour.
(a)(b)(c)


## 3.1.2. The Particle Density Calibration

The volume density of wheat flour was measured as 500.13 kg/m3 through experiments. During the simulation process, the density of wheat flour simulated particles was adjusted to make its volume density as 500.13 kg/m3. During the calibration of this density, a container with a radius of 0.1 m and a height of 0.1 m was created, and a scraper was used to scrape off the excess simulation particles above the container. The calibration process of wheat grain density is shown in Figure 3.Figure 3
Calibration process of wheat flour simulated grain density. (a) Particles injection start. (b) Particles injection end. (c) Particles stand still. (d) Particles scraping begin. (e) Particles scraping process. (f) Particles scraping end.
(a)(b)(c)(d)(e)(f)Particle injection: particles are generated from the particle factory and fall freely into the container, so that particles fill the container and overflow.Particles stand still: after the particles are filled, let them stand and freely overflow for a period of time to make the particles completely still.Scrape particles: at the end of standing, the scraper moves to scrape off excess particles so that the particles in the container are flush with the mouth of the container.Through the calibration of wheat flour simulated grain density, the grain density is 1320 kg/m³.


## 3.2. Calibration of Wheat Flour Particle Contact Parameters

Using wheat flour flow rate as the response value, the discrete element simulation contact parameters of the wheat flour particles were calibrated directly in the screw conveying process by Plackett-Burman, steepest climbing, and Box-Behnken experiments, and the optimal combination of contact parameters was obtained. The discrete element simulation of wheat flour and other powders provides a reference.


### 3.2.1. Mass Flow Rate Experiment of Wheat Flour

In this experiment, the screw conveyor of Jingu Co., Ltd. was used. The pitch is 0.1 m; the inner shaft diameter is 0.035 m; the outer diameter of the blade is 0.12 m; the inner diameter of the shaft cylinder is 0.13 m; the gap is 0.005 m; and the length of the feeding section is 0.5 m; and speed range is 60 r/min–150 r/min. The rotation speed of this screw conveyor is 100 rad/s. The weight of wheat flour was measured using a load cell (RS485 plane load cell: Hengyuan Sensor Technology Co., Ltd.; weighing range 0–50 kg; sampling frequency 10–30 Hz; measurement error ±0.003 kg). The data is set to record data every 0.1 s and the duration is set to 20 s. After the data recording is completed, the wheat flour time-quality data is derived to calculate the mass flow rate of wheat flour. The mass flow rate value of the wheat flour was experimented 5 times to take the average value. The mass flow rate value of the wheat flour screw conveyor was measured to be 0.805 kg/s. The experimental process and time-mass curve are shown in Figure4.Figure 4
Determination of mass flow rate of wheat flour screw conveyor. (a) Mass flow rate experiment of wheat flour. (b) Time-mass curve
(a)(b)


### 3.2.2. Simulation Model and Parameters

(1) Simulation parameters. Based on the settings of powder particle and stainless steel discrete element simulation parameters at home and abroad [28–32] and the built-in GEMM database of EDEM software, the variation range of each simulation parameter in this study is shown in Table 1. Combining the literature related to powder simulation [33–35] and the theory of particle scaling, the intrinsic parameters required for the simulation are set to wheat flour density of 1320 kg/m3, wheat flour Poisson’s ratio of 0.25, and wheat flour shear modulus of 6.0 × 107 Pa. The contact parameters of the material vary greatly with the density, shape, and particle size of the material, which cannot be obtained by consulting the physical property manual or literature, and using virtual experiments for calibration.Table 1
Parameters required in DEM simulation.
Simulation parametersValueDensity of wheat flour/(kg·m−3)1320Poisson’s ratio of wheat flour0.2–0.4Shear modulus of wheat/Pa1.1 × 107–6 × 107Density of stainless steel/(kg·m−3)7800Poisson’s ratio of stainless steel0.3Shear modulus of stainless steel/Pa7 × 1010Wheat flour-wheat flour restitution coefficient0.15–0.55Wheat flour-wheat flour static friction coefficient0.2–0.8Wheat flour-wheat flour rolling friction coefficient0.05–0.25Wheat flour-stainless steel restitution coefficient0.15–0.55Wheat flour-stainless steel static friction coefficient0.2–1.0Wheat flour-stainless steel rolling friction coefficient0.1–0.8JKR0.1–0.5(2) Simulation model. This simulation refers to the actual physical model and is appropriately simplified. The design dimensions of the hopper and spiral are the same as the actual physical model. Due to simulation conditions and time constraints, the particles radius was magnified two times, and the circle of the enlarged particles was set to 0.1 mm. Spherical particles were used for the simulation [36–39]. The simulation model is shown in Figure 5. During the simulation, the contact model is “Hertz-Mindlin with JKR,” the simulation time is 10 s, the particle generation method is dynamic, the generation rate is set to 200,0000/s, the number of generations is set to 4000000, and after the generation is completed, the rotation speed of the screw shaft is set, and the rotation speed of the screw shaft is 100 rad/s. After the simulation calculation is completed, the mass flow rate sensor in the software post-processing is used to measure the spiral conveyance of wheat flour.Figure 5
Simulation of wheat flour screw conveying. (a) Simulation process. (b). Post-processed mass flow rate.
(a)(b)


### 3.2.3. Design of Parameter Calibration Simulation Experiment

(1) Plackett-Burman experiment. Plackett-Burman design is a two-level partial experimental design. Factor significance is determined by examining the relationship between the target response and each factor, and comparing the differences between the two levels of each factor. This Plackett-Burman design screens the significance of simulated contact parameters based on the response rate of wheat spiral conveying mass flow rate. The low level is set to the original level, and the high level is set to twice the low level. The experiment parameters are shown in Table 2.Table 2
Parameters of Plackett-Burman experiment.
SymbolParametersLow levelHigh levelAWheat flour-wheat flour restitution coefficient0.150.3BWheat flour-wheat flour static friction coefficient0.20.4CWheat flour-wheat flour rolling friction coefficient0.050.1DWheat flour-stainless steel restitution coefficient0.150.3EWheat flour-stainless steel static friction coefficient0.20.4FWheat flour-stainless steel rolling friction coefficient0.10.2GJKR0.10.5V1Virtual parameters 1−11V2Virtual parameters 2−11V3Virtual parameters 3−11V4Virtual parameters 4−11The design and results of Plackett-Burman are shown in Table3. The analysis of the results by Design Expert software is used to obtain the significance of each contact parameter as shown in Table 4. From Table 4, it can be seen that JKR, the static friction coefficient of wheat flour-wheat flour, and the static friction coefficient of wheat flour-stainless steel P<0.01 have extremely significant effects on the spiral mass flow rate, while the remaining parameters P>0.05 have minimal effects on the spiral mass flow rate. In order to facilitate subsequent experiments, only the three parameters with the most significant impact (P<0.01) are considered in the steepest climbing and Box-Behnken experiments. The rest of the parameters combined with the relevant literature [20, 23, 24, 34] take the values (wheat flour-wheat flour recovery coefficient 0.2, wheat flour-wheat flour rolling friction coefficient 0.15, wheat flour-stainless steel recovery coefficient 0.2, and wheat flour-stainless steel rolling friction coefficient 0.15) for the steepest climbing and response surface experiment design.Table 3
Design and results of Plackett-Burman experiment.
Running sequenceABCDEFGV1V2V3V4Mass flow rate (kg/s)1−11−111−1111−1−10.803721−1111−1−1−11−111.10063−111−1111−1−1−110.8108411−1−1−11−111−1−11.129151−111−1111−1−1−11.14446−1−1−1−1−1−1−1−1−1−1−11.119711−1111−1−1−11−11.00368000000000001.02429111−1−1−11−111−11.0007101−1−1−11−111−1110.89511−1−1−11−111−11111.093112−1−11−111−1111−11.030713−1111−1−1−11−1111.032Table 4
Analysis of the significance of parameters in Plackett-Burman experiment.
ParametersEffectSum of squaresContribution/%SignificanceA0.0640.0127.8964B−0.1000.03119.4543C0.0130.0010.3077D0.0320.0031.9756E−0.1460.03640.8741F0.0430.0063.6375G−0.1110.03723.8332(2) Steepest climbing experiment. After the Plackett-Burman experiment, the steepest climbing experiment is performed according to the screened significance parameters so that it can quickly enter the vicinity of the optimal value. The steepest climbing experiment starts from the center point of the PB experiment, and the climbing step length is determined according to the regression coefficient obtained from the PB experiment. In order to approach the optimal value as quickly as possible, the climbing step length is usually taken as a larger value. The selected steps and results of this climbing experiment are shown in Table 5. According to the results in Table 5, it can be seen that the relative error of the mass flow rate at the 3rd level is the smallest, and the relative error from the 2nd to the 4th level changes from large to small and then becomes larger. Therefore, the 3rd level is selected as the center point, and the 2nd and 4th levels are follow-up response surface design at low and high levels.Table 5
Design and results of steepest ascent experiment.
No.JKRWheat flour-wheat flour rolling friction coefficientWheat flour-stainless steel static friction coefficientMass flow rate (kg/s)Relative error (%)10.10.20.21.18847.5820.20.40.40.96119.3830.30.60.60.7911.7440.40.80.80.7496.9650.51.01.00.67715.9(3) Box-Behnken experiment and regression model. Based on the results of the steepest climbing experiment and the principle of response surface design, the low, medium, and high levels of significant parameters were selected for the experiment design, and three center points were selected to evaluate the error. The Box-Behnken experiment results are shown in Table 6. Using Design Expert to establish a second-order regression equation with three significant parameters and the mass flow rate value is(14)Q=1.6+0.35H−1.8J−1.1K+0.036HJ+0.088HK−0.074JK−0.452H2+1.153J2+1.538K2.Table 6
Design and results of Box-Behnken experiment.
Running serial numberWheat flour-wheat static friction coefficient (H)Coefficient of static friction of wheat flour-stainless steel (J)JKR (K)Mass flow rate (kg/s)10000.799120000.8053−10−10.838140−1−10.9718510−10.795260110.75370−110.94048−1−100.9475901−10.7903100000.803111100.716212−1100.7925131−100.865514−1010.8006151010.7648Box-Behnken experiment model analysis results are shown in Table7. According to the results in Table 7, the fitted model P<0.005; JKR surface energy (H), static friction coefficient between wheat flour particles (J), and static friction coefficient of wheat flour-stainless steel (K), the quadratic term of JKR surface energy (H2), and the quadratic term of the static friction coefficient between wheat flour particles (J2) are all less than 0.05, indicating that each parameter has a significant effect on the mass flow rate, and the regression model is valid. The coefficient of variation CV = 0.72% in the experiment, which indicates that the experiment has higher reliability. The determination coefficient R2 = 0.9828; the adjusted determination coefficient Adjusted R2 = 0.9520; it shows that the model can truly reflect the actual situation. The experiment precision is Adep Precision = 18.42, which shows that the model has good accuracy.Table 7
ANOVA of quadratic polynomial model of Box-Behnken experiment.
Source of variationMean squareFreedomQuadratic sumF valueP valueModel0.006390.008531.830.0007H0.007010.007026.360.0037J0.056610.0566212.69<0.0001K0.002310.00238.760.0315HJ8.1 × 10–618.1 × 10–60.03050.8682HK0.000010.00000.04730.8364JK8.7 × 10–618.7 × 10–60.03270.8637H20.001210.00124.530.0867J20.007910.007929.500.0029K20.000910.00093.280.1299Residual0.001350.0003Lack of fit0.001330.000448.640.0202Pure error0.000029 × 10–6Sum0.077614R2 = 0.9828. Adjusted R2 = 0.9520. Predicted R2 = 0.7287. CV = 0.72%. Adep Precision = 18.42According to the results in Table8, under the premise of ensuring the model is good, remove the terms that have no significant effect on the mass flow rate. The results of the analysis of variance after optimizing the model are shown in Table 8. The misfit term P=0.0279; the coefficient of variation CV = 1.91%; Coefficient R2 = 0.9712; Adjusted R2 = 0.9552; Predicted R2 = 0.9131; experiment precision Adep Precision = 23.5. It can be seen that the model has good fit, reliability, and accuracy, which has been improved to some extent before optimization. The regression equation after optimization is(15)Q=1.435+0.429H−1.769J−0.171K−0.481H2+1.124J2.Table 8
ANOVA of the modified model of Box-Behnken experiment.
Source of variationMean squareFreedomQuadratic sumF ValuePvalueModel0.075450.015160.73<0.0001H0.007010.007028.280.0005J0.056610.0566228.17<0.0001K0.002310.00239.390.0135H20.001410.00145.550.0430J20.007510.007530.220.0004Residual0.002290.0002Lack of fit0.002270.000335.170.0279Pure error0.000029 × 10–6Sum0.077614R2 = 0.9712. Adjusted R2 = 0.9552. Predicted R2 = 0.9131. CV = 1.9%. Adep Precision = 23.5


## 3.2.1. Mass Flow Rate Experiment of Wheat Flour

In this experiment, the screw conveyor of Jingu Co., Ltd. was used. The pitch is 0.1 m; the inner shaft diameter is 0.035 m; the outer diameter of the blade is 0.12 m; the inner diameter of the shaft cylinder is 0.13 m; the gap is 0.005 m; and the length of the feeding section is 0.5 m; and speed range is 60 r/min–150 r/min. The rotation speed of this screw conveyor is 100 rad/s. The weight of wheat flour was measured using a load cell (RS485 plane load cell: Hengyuan Sensor Technology Co., Ltd.; weighing range 0–50 kg; sampling frequency 10–30 Hz; measurement error ±0.003 kg). The data is set to record data every 0.1 s and the duration is set to 20 s. After the data recording is completed, the wheat flour time-quality data is derived to calculate the mass flow rate of wheat flour. The mass flow rate value of the wheat flour was experimented 5 times to take the average value. The mass flow rate value of the wheat flour screw conveyor was measured to be 0.805 kg/s. The experimental process and time-mass curve are shown in Figure4.Figure 4
Determination of mass flow rate of wheat flour screw conveyor. (a) Mass flow rate experiment of wheat flour. (b) Time-mass curve
(a)(b)


## 3.2.2. Simulation Model and Parameters

(1) Simulation parameters. Based on the settings of powder particle and stainless steel discrete element simulation parameters at home and abroad [28–32] and the built-in GEMM database of EDEM software, the variation range of each simulation parameter in this study is shown in Table 1. Combining the literature related to powder simulation [33–35] and the theory of particle scaling, the intrinsic parameters required for the simulation are set to wheat flour density of 1320 kg/m3, wheat flour Poisson’s ratio of 0.25, and wheat flour shear modulus of 6.0 × 107 Pa. The contact parameters of the material vary greatly with the density, shape, and particle size of the material, which cannot be obtained by consulting the physical property manual or literature, and using virtual experiments for calibration.Table 1
Parameters required in DEM simulation.
Simulation parametersValueDensity of wheat flour/(kg·m−3)1320Poisson’s ratio of wheat flour0.2–0.4Shear modulus of wheat/Pa1.1 × 107–6 × 107Density of stainless steel/(kg·m−3)7800Poisson’s ratio of stainless steel0.3Shear modulus of stainless steel/Pa7 × 1010Wheat flour-wheat flour restitution coefficient0.15–0.55Wheat flour-wheat flour static friction coefficient0.2–0.8Wheat flour-wheat flour rolling friction coefficient0.05–0.25Wheat flour-stainless steel restitution coefficient0.15–0.55Wheat flour-stainless steel static friction coefficient0.2–1.0Wheat flour-stainless steel rolling friction coefficient0.1–0.8JKR0.1–0.5(2) Simulation model. This simulation refers to the actual physical model and is appropriately simplified. The design dimensions of the hopper and spiral are the same as the actual physical model. Due to simulation conditions and time constraints, the particles radius was magnified two times, and the circle of the enlarged particles was set to 0.1 mm. Spherical particles were used for the simulation [36–39]. The simulation model is shown in Figure 5. During the simulation, the contact model is “Hertz-Mindlin with JKR,” the simulation time is 10 s, the particle generation method is dynamic, the generation rate is set to 200,0000/s, the number of generations is set to 4000000, and after the generation is completed, the rotation speed of the screw shaft is set, and the rotation speed of the screw shaft is 100 rad/s. After the simulation calculation is completed, the mass flow rate sensor in the software post-processing is used to measure the spiral conveyance of wheat flour.Figure 5
Simulation of wheat flour screw conveying. (a) Simulation process. (b). Post-processed mass flow rate.
(a)(b)


## 3.2.3. Design of Parameter Calibration Simulation Experiment

(1) Plackett-Burman experiment. Plackett-Burman design is a two-level partial experimental design. Factor significance is determined by examining the relationship between the target response and each factor, and comparing the differences between the two levels of each factor. This Plackett-Burman design screens the significance of simulated contact parameters based on the response rate of wheat spiral conveying mass flow rate. The low level is set to the original level, and the high level is set to twice the low level. The experiment parameters are shown in Table 2.Table 2
Parameters of Plackett-Burman experiment.
SymbolParametersLow levelHigh levelAWheat flour-wheat flour restitution coefficient0.150.3BWheat flour-wheat flour static friction coefficient0.20.4CWheat flour-wheat flour rolling friction coefficient0.050.1DWheat flour-stainless steel restitution coefficient0.150.3EWheat flour-stainless steel static friction coefficient0.20.4FWheat flour-stainless steel rolling friction coefficient0.10.2GJKR0.10.5V1Virtual parameters 1−11V2Virtual parameters 2−11V3Virtual parameters 3−11V4Virtual parameters 4−11The design and results of Plackett-Burman are shown in Table3. The analysis of the results by Design Expert software is used to obtain the significance of each contact parameter as shown in Table 4. From Table 4, it can be seen that JKR, the static friction coefficient of wheat flour-wheat flour, and the static friction coefficient of wheat flour-stainless steel P<0.01 have extremely significant effects on the spiral mass flow rate, while the remaining parameters P>0.05 have minimal effects on the spiral mass flow rate. In order to facilitate subsequent experiments, only the three parameters with the most significant impact (P<0.01) are considered in the steepest climbing and Box-Behnken experiments. The rest of the parameters combined with the relevant literature [20, 23, 24, 34] take the values (wheat flour-wheat flour recovery coefficient 0.2, wheat flour-wheat flour rolling friction coefficient 0.15, wheat flour-stainless steel recovery coefficient 0.2, and wheat flour-stainless steel rolling friction coefficient 0.15) for the steepest climbing and response surface experiment design.Table 3
Design and results of Plackett-Burman experiment.
Running sequenceABCDEFGV1V2V3V4Mass flow rate (kg/s)1−11−111−1111−1−10.803721−1111−1−1−11−111.10063−111−1111−1−1−110.8108411−1−1−11−111−1−11.129151−111−1111−1−1−11.14446−1−1−1−1−1−1−1−1−1−1−11.119711−1111−1−1−11−11.00368000000000001.02429111−1−1−11−111−11.0007101−1−1−11−111−1110.89511−1−1−11−111−11111.093112−1−11−111−1111−11.030713−1111−1−1−11−1111.032Table 4
Analysis of the significance of parameters in Plackett-Burman experiment.
ParametersEffectSum of squaresContribution/%SignificanceA0.0640.0127.8964B−0.1000.03119.4543C0.0130.0010.3077D0.0320.0031.9756E−0.1460.03640.8741F0.0430.0063.6375G−0.1110.03723.8332(2) Steepest climbing experiment. After the Plackett-Burman experiment, the steepest climbing experiment is performed according to the screened significance parameters so that it can quickly enter the vicinity of the optimal value. The steepest climbing experiment starts from the center point of the PB experiment, and the climbing step length is determined according to the regression coefficient obtained from the PB experiment. In order to approach the optimal value as quickly as possible, the climbing step length is usually taken as a larger value. The selected steps and results of this climbing experiment are shown in Table 5. According to the results in Table 5, it can be seen that the relative error of the mass flow rate at the 3rd level is the smallest, and the relative error from the 2nd to the 4th level changes from large to small and then becomes larger. Therefore, the 3rd level is selected as the center point, and the 2nd and 4th levels are follow-up response surface design at low and high levels.Table 5
Design and results of steepest ascent experiment.
No.JKRWheat flour-wheat flour rolling friction coefficientWheat flour-stainless steel static friction coefficientMass flow rate (kg/s)Relative error (%)10.10.20.21.18847.5820.20.40.40.96119.3830.30.60.60.7911.7440.40.80.80.7496.9650.51.01.00.67715.9(3) Box-Behnken experiment and regression model. Based on the results of the steepest climbing experiment and the principle of response surface design, the low, medium, and high levels of significant parameters were selected for the experiment design, and three center points were selected to evaluate the error. The Box-Behnken experiment results are shown in Table 6. Using Design Expert to establish a second-order regression equation with three significant parameters and the mass flow rate value is(14)Q=1.6+0.35H−1.8J−1.1K+0.036HJ+0.088HK−0.074JK−0.452H2+1.153J2+1.538K2.Table 6
Design and results of Box-Behnken experiment.
Running serial numberWheat flour-wheat static friction coefficient (H)Coefficient of static friction of wheat flour-stainless steel (J)JKR (K)Mass flow rate (kg/s)10000.799120000.8053−10−10.838140−1−10.9718510−10.795260110.75370−110.94048−1−100.9475901−10.7903100000.803111100.716212−1100.7925131−100.865514−1010.8006151010.7648Box-Behnken experiment model analysis results are shown in Table7. According to the results in Table 7, the fitted model P<0.005; JKR surface energy (H), static friction coefficient between wheat flour particles (J), and static friction coefficient of wheat flour-stainless steel (K), the quadratic term of JKR surface energy (H2), and the quadratic term of the static friction coefficient between wheat flour particles (J2) are all less than 0.05, indicating that each parameter has a significant effect on the mass flow rate, and the regression model is valid. The coefficient of variation CV = 0.72% in the experiment, which indicates that the experiment has higher reliability. The determination coefficient R2 = 0.9828; the adjusted determination coefficient Adjusted R2 = 0.9520; it shows that the model can truly reflect the actual situation. The experiment precision is Adep Precision = 18.42, which shows that the model has good accuracy.Table 7
ANOVA of quadratic polynomial model of Box-Behnken experiment.
Source of variationMean squareFreedomQuadratic sumF valueP valueModel0.006390.008531.830.0007H0.007010.007026.360.0037J0.056610.0566212.69<0.0001K0.002310.00238.760.0315HJ8.1 × 10–618.1 × 10–60.03050.8682HK0.000010.00000.04730.8364JK8.7 × 10–618.7 × 10–60.03270.8637H20.001210.00124.530.0867J20.007910.007929.500.0029K20.000910.00093.280.1299Residual0.001350.0003Lack of fit0.001330.000448.640.0202Pure error0.000029 × 10–6Sum0.077614R2 = 0.9828. Adjusted R2 = 0.9520. Predicted R2 = 0.7287. CV = 0.72%. Adep Precision = 18.42According to the results in Table8, under the premise of ensuring the model is good, remove the terms that have no significant effect on the mass flow rate. The results of the analysis of variance after optimizing the model are shown in Table 8. The misfit term P=0.0279; the coefficient of variation CV = 1.91%; Coefficient R2 = 0.9712; Adjusted R2 = 0.9552; Predicted R2 = 0.9131; experiment precision Adep Precision = 23.5. It can be seen that the model has good fit, reliability, and accuracy, which has been improved to some extent before optimization. The regression equation after optimization is(15)Q=1.435+0.429H−1.769J−0.171K−0.481H2+1.124J2.Table 8
ANOVA of the modified model of Box-Behnken experiment.
Source of variationMean squareFreedomQuadratic sumF ValuePvalueModel0.075450.015160.73<0.0001H0.007010.007028.280.0005J0.056610.0566228.17<0.0001K0.002310.00239.390.0135H20.001410.00145.550.0430J20.007510.007530.220.0004Residual0.002290.0002Lack of fit0.002270.000335.170.0279Pure error0.000029 × 10–6Sum0.077614R2 = 0.9712. Adjusted R2 = 0.9552. Predicted R2 = 0.9131. CV = 1.9%. Adep Precision = 23.5


## 4. Experiment Verification

### 4.1. Determination of the Best Parameter Combination and Simulation Verification

Using Design Expert software to take the actual wheat flour mass flow rate as the target and optimize the regression equation after optimization, we can understand that, to minimize the mass flow rate error obtained by simulation and experiment, the surface energy of JKR is 0.364 and the static friction coefficient of wheat flour-wheat flour is 0.437, and the coefficient of static friction of wheat flour-stainless steel is 0.609. The best parameter combination was used for the wheat flour mass flow rate simulation experiment. The comparison between the simulation and the physical experiment is shown in Figure6. The mass flow rate value obtained from the simulation experiment was 0.816 kg/s, and the error value was 1.37% from the actual value of 0.805 kg/s, indicating that the simulation results were not significantly different from the actual experiment values.Figure 6
Comparison of simulation and physical experiments. (a) Simulation experiment. (b) Physical experiment.
(a)(b)


### 4.2. Simulation Verification at Different Speeds

In order to further confirm the reliability of the contact parameters of wheat flour calibration, the simulation and experimental mass flow rates at different speeds are compared, as shown in Figure7. It can be seen from the comparison that the mass flow rate errors at different speeds are all within 3%, and the DEM simulation is very close to the experiment.Figure 7
Comparative analysis of simulation and experiment of screw conveying at different speeds.


## 4.1. Determination of the Best Parameter Combination and Simulation Verification

Using Design Expert software to take the actual wheat flour mass flow rate as the target and optimize the regression equation after optimization, we can understand that, to minimize the mass flow rate error obtained by simulation and experiment, the surface energy of JKR is 0.364 and the static friction coefficient of wheat flour-wheat flour is 0.437, and the coefficient of static friction of wheat flour-stainless steel is 0.609. The best parameter combination was used for the wheat flour mass flow rate simulation experiment. The comparison between the simulation and the physical experiment is shown in Figure6. The mass flow rate value obtained from the simulation experiment was 0.816 kg/s, and the error value was 1.37% from the actual value of 0.805 kg/s, indicating that the simulation results were not significantly different from the actual experiment values.Figure 6
Comparison of simulation and physical experiments. (a) Simulation experiment. (b) Physical experiment.
(a)(b)


## 4.2. Simulation Verification at Different Speeds

In order to further confirm the reliability of the contact parameters of wheat flour calibration, the simulation and experimental mass flow rates at different speeds are compared, as shown in Figure7. It can be seen from the comparison that the mass flow rate errors at different speeds are all within 3%, and the DEM simulation is very close to the experiment.Figure 7
Comparative analysis of simulation and experiment of screw conveying at different speeds.


## 5. Conclusion

(1)
Based on the JKR model in discrete element method, the simulated contact parameters required for the screw conveying of wheat flour were calibrated. The Plackett-Burman experiment screened out the factors that significantly affected the mass flow rate of screw conveying of wheat flour: the static friction coefficient of wheat flour-wheat flour, the static friction coefficient of wheat flour-stainless steel, and surface energy JKR.(2)
Based on the results of the Box-Behnken experiment, a quadratic regression model between three significant parameters and mass flow rate was established and optimized. According to the results of the analysis of variance of the optimized model, it is known that, except for three significant parameters (JKR surface energy, wheat flour-wheat flour static friction in addition to the primary term of the coefficient, and the static friction coefficient of wheat flour-stainless steel), the quadratic term of the JKR surface energy (H2) and the secondary term of the static friction coefficient of wheat flour-wheat flour (J2) also have a significant effect on the mass flow rate of screw flour transportation.(3)
Taking the actual mass flow rate value of wheat flour screw conveying as the target, the regression equation was optimized and the best combination of significant parameters was obtained: wheat flour-wheat static friction coefficient is 0.437, wheat flour-stainless steel static friction coefficient is 0.609, and the surface energy JKR is 0.364.(4)
Use the calibrated contact parameters for simulation, and compare the simulated mass flow rate with the experimental mass flow rate. The error value is only 1.37%. To further demonstrate the accuracy of the calibration parameters, the simulation and experimental results at different speeds are compared. The mass flow rates were compared, and the error values were all in the range of 3%. It is shown that parameter calibration in the process of screw conveying can improve the accuracy of the parameters and provide a reference for the screw conveying simulation of powder.



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*Source: 6671511-2021-04-23.xml*