Effect of Temperature on Densiﬁcation Pressure and the Unit Density in Production of Corn Straw Pellet with a Post-Heating Method

: In the biomass densiﬁcation process, a lot of energy is needed to prevent its spring-back and to overcome the friction between the material and the channel surface of the die so as to build up pressure. However, moisture, particle size, temperature, and type of material all inﬂuence the densiﬁcation pressure, pellet quality, and the density. The research was aimed to ﬁnd out how the densiﬁcation pressure and density were affected by the die temperature based on an open-end densiﬁcation method using a self-developed pellet extruder. When the piston ﬁxed in the front of the extruder moved in a reciprocating way, the raw material was pressed into the opening die, which had a heater wrapped up. Crushed corn straw with a particle size under 4 mm and with a given moisture content of 10% was used to be compacted by the extruder. The results showed that with the increase of the die temperature, the value of densiﬁcation pressure decreased; however, the quality of pellets was not good at temperatures higher than 140 ◦ C. The proper temperature for corn straw densiﬁcation was 100 ◦ C, and the value of the unit density was above 1.0 g/cm 3 . Meanwhile, the surface quality of the pellet was comparatively good. The reference values of the friction coefﬁcient at different temperatures were provided. into Contributions: Conceptualization, visualization, supervision, Q.W. and Z.C.; project funding acquisition, Q.W.


Introduction
Nowadays, growing attention is being paid to the preparation and industrial utilization of biomass material because of either increasing environmental concerns or the non-renewability of fossil resources [1][2][3]. Various advantages provided by biomass material, such as recyclability, renewability, abundant availability, and low cost, have drawn the attention of many researchers to use them in industrial production [4]. Corn straw, a kind of important biomass widely distributed in China, is suitable for energy use as fuel [5]. However, the bulk density of the corn straw is one of the most major limitations to its largescale viability for energy application. One of the main technologies of biomass processing is physical conversion, or more precisely, agglomeration [6]. Producing a compacted corn straw product would reduce transportation costs, resulting in a viable pathway for the use of corn straw as a biomass feedstock [7,8]. Thus, it is important to find out the optimal process parameters to compact the biomass by means of analyzing the influence of various factors on the process of compaction.
Material variables and process variables are the main factors determining the characteristics of the final product in the process of producing pellets. Material variables are the type of biomass, moisture content, degree of fragmentation, and method of raw material preparation. Process variables include the densification pressure, temperature, and geometry of the matrix channel [9][10][11].
At present, the screw extruder and the briquette press are both necessary conditions for compacting the feedstock. It needs a lot of energy in the densification process of the screw extruder to overcome the friction between the inner surface of the die wall and the material and the forces, such as shearing and mixing, between the screw and the material [12]. Thus, the wear of the contact parts is very high. For the screw extruder, since the screw and the material are always in the shearing and mixing state, the wear of the screw surface is very serious [13,14].
There are some obvious problems existing in the briquette press. According to previous studies, in the compaction process, a lot of energy is required to overcome the friction between the materials and the friction between the materials and the surface of the die. This leads to accelerating the abrasion of the die. Usually, the die is needed to be repaired at intervals [15].
In order to decrease the energy needed in the process of compaction, there are some new methods to be proposed, one of which is the vibration-assisted compaction of biomass. The results of the study showed that with the vibration applied to a die surface, the compression energy requirement would be reduced, and the product quality would be improved [16]. Moreover, changing the moisture content of the raw materials is another efficient method. The most appropriate moisture content for the compaction of the straws is 10-15% [17]. In this way, the cost of the compaction would decrease with qualified quality.
Compared with the compaction without heat, the densification of the biomass with heat could decrease the compaction force, resulting in decreasing the friction needed to be overcome and increasing the die life [18]. Lignin in the biomass at temperatures above about 140 • C will be softened, and that will improve the binding of particles [12], resulting in decreasing the friction resistance of the compaction and improving the quality of the product. It is concluded from the study of the heated-die wafer densification of alfalfa and Bermuda grass that the pressure required to compact would decrease with the die temperature increasing [19].
The main quality parameters depending on the process and material factors are mechanical durability (DU) and specific density (DE). Durability (crushing strength) reflects the ability of pellets to resist deformation after multiple falls and tumbling collisions. The process of pressure compaction of biomass is intended to obtain the unit density and bulk density (BD), as well as the mechanical durability at appropriate levels, and the minimum thresholds are defined by the appropriate standards. Unified bulk density (or specific density) guarantees similar values of the energy density of fuel-regardless of the raw material used. On the other hand, high mechanical durability guarantees safe and non-abrasive use of the fuel [20,21].
Based on the above research, it could be concluded that although the research on the densification process with heating has been further improved, the universal mechanical testing machine is in the experimental equipment, whose production rate is obviously lower than industrialized equipment. There is a great difference between compaction using a universal mechanical and compaction using a pellet extruder, which does not have much significance to production practice. In addition, the effect of heating on the coefficient of friction between the raw material and the internal surface of the die has not been investigated.
In this research, a self-developed extruder for biomass pellet production was applied, and a heater used to change the temperature of the compaction was added to the die. The objective of this paper is to study the effects of temperature on the densification pressure and the unit density in the production of corn straw pellet through an open-end die. The results of the study can be used to find out a better way to treat biomass using a post-heating method instead of the traditional preheating method. By controlling the temperature properly, it is easier to find out a way to gain much better products with smaller energy costs.

Materials Preparation
The experimental material was corn straw-a widely cultivated cereal plant that was grown in the city of Chifeng, Inner Mongolia, China. With the increase of the standard of living, lots of agricultural residues, such as corn straw and wheat straw, are no longer used for animal feed, home heating, and cooking. In the field, these by-products are usually burnt directly, which leads to the pollution of the environment and maybe one of the reasons for hazy weather. Such a fact was suggested by current research that these large quantities of resources could be used as low carbon fuel if processed properly instead of the waste of energy.
The corn straw was naturally dried for a week in the summer and then transported to a biomass laboratory. The material was crushed into small fibrous pieces using crumbling equipment (Model GXP-400; Beijing Forestry University; Beijing, China), as shown in Figures 1 and 2. The crushed raw material was separated into two parts by using a sieve with an aperture of 4 mm, and the raw material under 4 mm [22] was utilized in the experiment. The moisture content of the processed raw material was measured according to the following drying procedure. Ten grams of crumbled raw material was put into the rapid moisture meter at a temperature of 100 • C for 24 h; then, samples were weighed every 1 h by an electronic balance until the mass did not reduce. It was calculated that the moisture content was about 10% [22] by dividing the mass loss by the original total mass. The rapid moisture meter is shown in Figure 3.

Materials Preparation
The experimental material was corn straw-a widely cultivated cereal grown in the city of Chifeng, Inner Mongolia, China. With the increase of t living, lots of agricultural residues, such as corn straw and wheat straw, used for animal feed, home heating, and cooking. In the field, these by-pro ally burnt directly, which leads to the pollution of the environment and ma reasons for hazy weather. Such a fact was suggested by current research t quantities of resources could be used as low carbon fuel if processed prop the waste of energy.
The corn straw was naturally dried for a week in the summer and th to a biomass laboratory. The material was crushed into small fibrous piec bling equipment (Model GXP-400; Beijing Forestry University; Beijing, Ch in Figures 1 and 2. The crushed raw material was separated into two parts b with an aperture of 4 mm, and the raw material under 4 mm [22] was util periment. The moisture content of the processed raw material was measure the following drying procedure. Ten grams of crumbled raw material wa rapid moisture meter at a temperature of 100 °C for 24 h; then, samples every 1 h by an electronic balance until the mass did not reduce. It was calc moisture content was about 10% [22] by dividing the mass loss by the origi The rapid moisture meter is shown in Figure 3.   The experimental material was corn straw-a widely cultivated c grown in the city of Chifeng, Inner Mongolia, China. With the increa living, lots of agricultural residues, such as corn straw and wheat s used for animal feed, home heating, and cooking. In the field, these b ally burnt directly, which leads to the pollution of the environment an reasons for hazy weather. Such a fact was suggested by current rese quantities of resources could be used as low carbon fuel if processed the waste of energy.
The corn straw was naturally dried for a week in the summer a to a biomass laboratory. The material was crushed into small fibrous bling equipment (Model GXP-400; Beijing Forestry University; Beijin in Figures 1 and 2. The crushed raw material was separated into two p with an aperture of 4 mm, and the raw material under 4 mm [22] wa periment. The moisture content of the processed raw material was me the following drying procedure. Ten grams of crumbled raw mater rapid moisture meter at a temperature of 100 °C for 24 h; then, sam every 1 h by an electronic balance until the mass did not reduce. It wa moisture content was about 10% [22] by dividing the mass loss by the The rapid moisture meter is shown in Figure 3.    Water was added to the material and mixed thoroughly to obta ture content; the process is described below.
1. Divide the material into three parts, and dry them for a week. 2. Use the rapid moisture meter to figure out the moisture of the b late how much water should be added to the biomass. 3. Mix the materials and the water uniformly through keeping th plastic bag for 3 days. 4. Repeat the third process until the moisture is as needed.

Pellet Production Method
The biomass pellet extruder was developed and manufactured Forestry University. The self-developed extruder is shown in Figure   Figure 4. Mechanical structure of the self-developed extruder. 1. Reducer. 2. F 4. Cylinder die. 5. Thermocouple. 6. Hopper. 7. Piston. 8. Pressure sensor. Spring. 11. Rolling bearing. 12. Displacement sensor. 13. Eccentric shaft. 14. T Water was added to the material and mixed thoroughly to obtain the desired moisture content; the process is described below.

1.
Divide the material into three parts, and dry them for a week.

2.
Use the rapid moisture meter to figure out the moisture of the biomass. Then calculate how much water should be added to the biomass.

3.
Mix the materials and the water uniformly through keeping them in the packaged plastic bag for 3 days.

4.
Repeat the third process until the moisture is as needed.

Pellet Production Method
The biomass pellet extruder was developed and manufactured in the lab of Beijing Forestry University. The self-developed extruder is shown in Figure 4. Water was added to the material and mixed thoroughly to obtain the desired moisture content; the process is described below.
1. Divide the material into three parts, and dry them for a week. 2. Use the rapid moisture meter to figure out the moisture of the biomass. Then calculate how much water should be added to the biomass. 3. Mix the materials and the water uniformly through keeping them in the packaged plastic bag for 3 days. 4. Repeat the third process until the moisture is as needed.

Pellet Production Method
The biomass pellet extruder was developed and manufactured in the lab of Beijing Forestry University. The self-developed extruder is shown in Figure 4.  A reducer with the specified rotation of 50 rpm was applied as a power source, which drove the eccentric shaft with an eccentricity of 30 mm. The rotating eccentric shaft forced a piston to reciprocate linearly along with a sliding bearing by driving the rolling bearing set up on one side of the piston of 16 mm in diameter. When the piston moved to one end by the drive of the eccentric shaft, the reset spring started to make the piston move back to the original position.
In front of the piston, there was a cylinder die with a 16 mm inside diameter and was 72 mm in length installed for making a single pellet. Thus, the ratio of the length to the inside diameter is 4.5.
A heating tape wrapped the cylinder die and heated the die to a certain temperature with a thermocouple controlled by a temperature controller and monitor.  A reducer with the specified rotation of 50 rpm was applied as a power source, which drove the eccentric shaft with an eccentricity of 30 mm. The rotating eccentric shaft forced a piston to reciprocate linearly along with a sliding bearing by driving the rolling bearing set up on one side of the piston of 16 mm in diameter. When the piston moved to one end by the drive of the eccentric shaft, the reset spring started to make the piston move back to the original position.
In front of the piston, there was a cylinder die with a 16 mm inside diameter and was 72 mm in length installed for making a single pellet. Thus, the ratio of the length to the inside diameter is 4.5.
A heating tape wrapped the cylinder die and heated the die to a certain temperature with a thermocouple controlled by a temperature controller and monitor.
The cylinder die was wrapped by a heating strip with a thermocouple to preheat the cylinder die to a certain temperature controlled by a temperature controller and a monitor. A pressure sensor (Model SEF-5T; Dongguan Risheng Technology Development Co. Ltd.; Dongguan, China) was joined to the piston to test the required pressure in the densification process. A displacement sensor (Model LWH-0200; Dongguan Risheng Technology Development Co., Ltd.; Dongguan, China) was fixed onto the frame to test the displacement with the reciprocating motion of the rolling bearing. A data acquisition system, including the above sensors, was designed to acquire the data at the same time from the pressure sensor (30 Hz) and the displacement sensor. Thus, the derived data on the force and the displacement was one to one correspondence.
Previous studies [13] have indicated that moisture, particle size, temperature, and material type all influence the densification pressure, pellet quality, and density. As the main purpose of this study was to investigate the effect of the temperature on the densification pressure and unit density of the corn straw, a series of experiments in the reciprocating state (intermittent compaction of the raw material) was performed to investigate the pressure and the displacement at different temperatures.

Force Analysis during Densification Process
The material densification stage can be roughly divided into compression, pushing, and conforming stages. The pressure rises rapidly on the stage of compression, which starts to decrease after reaching the maximum value. Before reaching the maximum pressure, the particles rearrange themselves and significantly increase the inter-particle density until the density of the pellet approaches the true density of the component ingredients. This stage mainly occurs in the front section of the die for a distance. After the maximum pressure is reached, the relative sliding between the material and the channel occurs, and the friction starts to be transformed into sliding friction. Meanwhile, the pressure decreases, and the compression enters into the pushing and shape-keeping stage. A schematic drawing of the pressure within the pressure channel of the die is shown in Figure 5.
Energies 2022, 15, x FOR PEER REVIEW The cylinder die was wrapped by a heating strip with a thermocouple to pre cylinder die to a certain temperature controlled by a temperature controller and a m A pressure sensor (Model SEF-5T; Dongguan Risheng Technology Development C Dongguan, China) was joined to the piston to test the required pressure in the de tion process. A displacement sensor (Model LWH-0200; Dongguan Risheng Tech Development Co., Ltd.; Dongguan, China) was fixed onto the frame to test the d ment with the reciprocating motion of the rolling bearing. A data acquisition sys cluding the above sensors, was designed to acquire the data at the same time f pressure sensor (30 Hz) and the displacement sensor. Thus, the derived data on t and the displacement was one to one correspondence.
Previous studies [13] have indicated that moisture, particle size, temperatu material type all influence the densification pressure, pellet quality, and density main purpose of this study was to investigate the effect of the temperature on th fication pressure and unit density of the corn straw, a series of experiments in th rocating state (intermittent compaction of the raw material) was performed to inv the pressure and the displacement at different temperatures.

Force Analysis during Densification Process
The material densification stage can be roughly divided into compression, p and conforming stages. The pressure rises rapidly on the stage of compression, whi to decrease after reaching the maximum value. Before reaching the maximum press particles rearrange themselves and significantly increase the inter-particle density u density of the pellet approaches the true density of the component ingredients. Th mainly occurs in the front section of the die for a distance. After the maximum pre reached, the relative sliding between the material and the channel occurs, and the starts to be transformed into sliding friction. Meanwhile, the pressure decreases, compression enters into the pushing and shape-keeping stage. A schematic drawin pressure within the pressure channel of the die is shown in Figure 5. At a certain temperature, the pressure within the pressure channel at a dis from the outlet can be calculated by Equation (1) where is the material Poisson's ration; 0 is the preload pressure, with a unit f is the friction coefficient between the biomass and the opening channel of the die distance between the calculated section and the die outlet, mm; r is the radius of inder die, mm. When x = l, is the pressure of the compaction at a certain tempe At a certain temperature, the pressure within the pressure channel at a distance x from the outlet can be calculated by Equation (1): [23] where µ is the material Poisson's ration; P N0 is the preload pressure, with a unit of MPa; f is the friction coefficient between the biomass and the opening channel of the die; x is the distance between the calculated section and the die outlet, mm; r is the radius of the cylinder die, mm. When x = l, P l is the pressure of the compaction at a certain temperature.

Densification Pressure Test
The material was fed into the hopper and stirred by a screw set up at the bottom of the hopper to ensure the uniform feed in front of the piston. The reciprocating speed of the piston was 50 rpm. Every experiment with different temperatures was conducted for 2 min. At a given moisture content of 10%, the temperature was controlled at 40, 60, 80, 100, 120, 140, 160, 180, and 200 • C, respectively. There was a maximum pressure in every single pouch, and the average densification pressure refers to the average number of all the maximum pressure values in each 2-min experiment. Each experiment in the same condition was repeated 3 times.

Pellet Density Test
The pellet density was calculated by measuring the length and the diameter of the pellet using an electronic caliper and by measuring the mass of the pellet using an electronic balance. In order to obtain an accurate volume, the edges of the pellets have been smoothed. The pellet density was calculated by dividing the individual mass by its volume and calculated on the basis of its length and diameter [24]. Ten randomized samples were measured and their properties documented. Figure 6 shows the surface quality of the pellets produced with the corn straw particles at a moisture content of 10% and particle size under 4 mm in different temperatures from 40 to 200 • C. The pellets show a good surface quality below the temperature of 120 • C, all of which are with a smooth surface. However, when the temperature was above 140 • C, cracks and deformations appeared on the surface of the pellets. That may be due to the higher temperature brought about the inner heat of the pellets. Subsequently, the steam exploded the pellets. The type of pellet damage indicated that the material had not been uniformly moisturized, and pellet destruction occurred where the moisture content of the material was high. In this case, when the pellets had a non-uniform shape, the measurement of geometry may cause measurement errors, and the high accuracy of measurement cannot be guaranteed. In future experiment, other methods of density measurements should be adopted to acquire high accuracy.

Densification Pressure Test
The material was fed into the hopper and stirred by a screw set up at the bottom of the hopper to ensure the uniform feed in front of the piston. The reciprocating speed of the piston was 50 rpm. Every experiment with different temperatures was conducted for 2 min. At a given moisture content of 10%, the temperature was controlled at 40, 60, 80, 100, 120, 140, 160, 180, and 200 °C, respectively. There was a maximum pressure in every single pouch, and the average densification pressure refers to the average number of all the maximum pressure values in each 2-min experiment. Each experiment in the same condition was repeated 3 times.

Pellet Density Test
The pellet density was calculated by measuring the length and the diameter of the pellet using an electronic caliper and by measuring the mass of the pellet using an electronic balance. In order to obtain an accurate volume, the edges of the pellets have been smoothed. The pellet density was calculated by dividing the individual mass by its volume and calculated on the basis of its length and diameter [24]. Ten randomized samples were measured and their properties documented. Figure 6 shows the surface quality of the pellets produced with the corn straw particles at a moisture content of 10% and particle size under 4 mm in different temperatures from 40 to 200 °C. The pellets show a good surface quality below the temperature of 120 °C, all of which are with a smooth surface. However, when the temperature was above 140 °C, cracks and deformations appeared on the surface of the pellets. That may be due to the higher temperature brought about the inner heat of the pellets. Subsequently, the steam exploded the pellets. The type of pellet damage indicated that the material had not been uniformly moisturized, and pellet destruction occurred where the moisture content of the material was high. In this case, when the pellets had a non-uniform shape, the measurement of geometry may cause measurement errors, and the high accuracy of measurement cannot be guaranteed. In future experiment, other methods of density measurements should be adopted to acquire high accuracy.

Densification Pressure of Every Single Pouch
A graph of the densification pressure versus displacement in a single pouch of the palletization process was plotted by the data acquisition system on the computer. To obtain more accurate experiment results, each experiment was conducted for 2 min. In view of the graph of every pouch in the densification process was similar, only one pouch in the experiment was depicted in Figure 7. It was explicitly shown that the compression process could be divided into three different stages.

Densification Pressure of Every Single Pouch
A graph of the densification pressure versus displacement in a single pouch of the palletization process was plotted by the data acquisition system on the computer. To obtain more accurate experiment results, each experiment was conducted for 2 min. In view of the graph of every pouch in the densification process was similar, only one pouch in the experiment was depicted in Figure 7. It was explicitly shown that the compression process could be divided into three different stages. At the AB stage, the piston started to pouch; the raw material was fed in front of the piston. Due to the very low bulk density of the corn straw, the pressure nearly did not change with the displacement of 0 to 24 mm.
At the compression stage (BC), the feedstock between the piston and the die was compressed by the piston and entered the opening channel of the die. With the reciprocating motion of the piston, the pressure to compact the pellets was gradually built up by the friction between the feedstock and the channel. Then the material was pressed into the channel, and the pellet density increased. Meanwhile, the compression pressure was increasing sharply to a large value (shown in Figure 7, more than 90 MPa) with a short displacement from 24 to 27 mm.
At the extrusion stage (CD), the piston continued to move forward while the densification pressure did not increase at all. The pellets started to be extruded out of the die and the maximum force reached a relatively stable range which overcame the friction on the surface between the opening channel and the compacted pellet inside. This densification process is similar to the experiment carried out by Wu [16].

Average Densification Pressure Affected by the Die Temperature
It was shown in Figure 8 that the average pressure of the compaction (P) decreased as the temperature increased from 40 to 120 °C . That was because, with the higher temperature, the lignin on the surface of the pellet reached its glass transition temperature which could act as a lubricant to reduce the friction between the biomass and the opening channel of the die. When the temperature reached 140 °C , the steam resulted in the expansion of the pellets and the requirement of higher compaction force; therefore, the densification pressure increased a little with the rise of the temperature. Subsequently, the pressure decreased as the temperature rose from 160 to 200 °C . This was most likely caused by the inner steam explosion, which pushed the pellet out of the die instead of the throughout by the piston. However, the pressure during this densification process decreased sharply; the particles almost could not be densified to a pellet. At the AB stage, the piston started to pouch; the raw material was fed in front of the piston. Due to the very low bulk density of the corn straw, the pressure nearly did not change with the displacement of 0 to 24 mm.
At the compression stage (BC), the feedstock between the piston and the die was compressed by the piston and entered the opening channel of the die. With the reciprocating motion of the piston, the pressure to compact the pellets was gradually built up by the friction between the feedstock and the channel. Then the material was pressed into the channel, and the pellet density increased. Meanwhile, the compression pressure was increasing sharply to a large value (shown in Figure 7, more than 90 MPa) with a short displacement from 24 to 27 mm.
At the extrusion stage (CD), the piston continued to move forward while the densification pressure did not increase at all. The pellets started to be extruded out of the die, and the maximum force reached a relatively stable range which overcame the friction on the surface between the opening channel and the compacted pellet inside. This densification process is similar to the experiment carried out by Wu [16].

Average Densification Pressure Affected by the Die Temperature
It was shown in Figure 8 that the average pressure of the compaction (P) decreased as the temperature increased from 40 to 120 • C. That was because, with the higher temperature, the lignin on the surface of the pellet reached its glass transition temperature, which could act as a lubricant to reduce the friction between the biomass and the opening channel of the die. When the temperature reached 140 • C, the steam resulted in the expansion of the pellets and the requirement of higher compaction force; therefore, the densification pressure increased a little with the rise of the temperature. Subsequently, the pressure decreased as the temperature rose from 160 to 200 • C. This was most likely caused by the inner steam explosion, which pushed the pellet out of the die instead of the throughout by the piston. However, the pressure during this densification process decreased sharply; the particles almost could not be densified to a pellet. the lignin in biomass, which could lead to the change of physicochemical prop biomass material and the friction coefficient f as well. Given that the variab temperature was not introduced in Equation (1), this paper combined theoret and experimental results in order to provide the reference values of friction c different temperatures. Assuming 0 = 9MPa, = 0.2 [25], the reference values of the friction between the opening channel and biomass feedstocks at different temperatur moisture content of corn straw was 10%, and the length-to-diameter ratio w calculated by Equation (1), and the results are shown in Figure 9. According to Figure 9, the friction coefficient f and temperature T were lin It could be concluded from Figure 9 that f tends to decrease gradually with th the temperature from 40 to 200 °C. The values at 120 and 140 °C have deviatio due to the measurement or other experiment reasons, and this phenomenon w to be investigated in future studies. It was shown in Figure 8 that the maximum pressure of the compaction (P l ) is a constant value at different temperatures, according to Equation (1), which obviously contradicts the result of the experiment. High temperature and pressure resulted in softening the lignin in biomass, which could lead to the change of physicochemical properties of the biomass material and the friction coefficient f as well. Given that the variable related tp temperature was not introduced in Equation (1), this paper combined theoretical analysis and experimental results in order to provide the reference values of friction coefficient at different temperatures.
Assuming P N0 = 9 MPa, µ = 0.2 [25], the reference values of the friction coefficient between the opening channel and biomass feedstocks at different temperatures when the moisture content of corn straw was 10%, and the length-to-diameter ratio was 4.5, were calculated by Equation (1), and the results are shown in Figure 9.
dicts the result of the experiment. High temperature and pressure resu the lignin in biomass, which could lead to the change of physicochemica biomass material and the friction coefficient f as well. Given that the v temperature was not introduced in Equation (1), this paper combined th and experimental results in order to provide the reference values of fric different temperatures. Assuming 0 = 9MPa, = 0.2 [25], the reference values of the f between the opening channel and biomass feedstocks at different tempe moisture content of corn straw was 10%, and the length-to-diameter ra calculated by Equation (1), and the results are shown in Figure 9. According to Figure 9, the friction coefficient f and temperature T w It could be concluded from Figure 9 that f tends to decrease gradually w the temperature from 40 to 200 °C. The values at 120 and 140 °C have de due to the measurement or other experiment reasons, and this phenome According to Figure 9, the friction coefficient f and temperature T were linearly fitted. It could be concluded from Figure 9 that f tends to decrease gradually with the increase of the temperature from 40 to 200 • C. The values at 120 and 140 • C have deviations probably Energies 2022, 15, 842 9 of 11 due to the measurement or other experiment reasons, and this phenomenon will continue to be investigated in future studies.

Pellet Density Affected by the Die Temperature
It is clearly found in Figure 10 that the density decreases from 1.2 to 0.75 g/cm 3 as the temperature increases from 40 to 140 • C. With the increase of temperature, the coefficient of friction between the pellet surface and the inner die surface is reduced by the increase of the moisture, which is transferred from inside the pellet to outside the surface, which may be the reason for the decrease of the density of the pellets. When the temperature reached 160 • C, the density of the pellets increased. This was probably because with the increase of the temperature, the lignin inside the pellet started to glassify, which could lead to the easier adherence between the particles of the corn straw. Changes in density at higher temperatures may also be caused by moisture, but it is difficult to prove this by analyzing the results for only one moisture in this article. When the temperature reached 200 • C, the moisture existing in the pellets started to change to steam, which led to the explosion of the extrusion pellets, and then the density of the pellets decreased. However, the main reason for the density decrease in this experiment was a pressure drop caused by a decrease in the friction coefficient, whose value depended on the temperature. As a result, it was the temperature that caused a decrease in the density of the pellet obtained.

Pellet Density Affected by the Die Temperature
It is clearly found in Figure 10 that the density decreases from 1.2 t temperature increases from 40 to 140 °C. With the increase of temperat of friction between the pellet surface and the inner die surface is reduc of the moisture, which is transferred from inside the pellet to outside may be the reason for the decrease of the density of the pellets. Whe reached 160 °C, the density of the pellets increased. This was probably increase of the temperature, the lignin inside the pellet started to gla lead to the easier adherence between the particles of the corn straw. Cha higher temperatures may also be caused by moisture, but it is difficu analyzing the results for only one moisture in this article. When the tem 200 °C, the moisture existing in the pellets started to change to steam explosion of the extrusion pellets, and then the density of the pellets dec the main reason for the density decrease in this experiment was a pre by a decrease in the friction coefficient, whose value depended on the result, it was the temperature that caused a decrease in the density of th

Conclusions
A mechanical extruder was designed and manufactured. The pis reciprocate to ensure that the corn straw could be squeezed into and ou the die, whose ratio of the length to the inside diameter is 4.5. Crushed particle size under 4 mm and with a given moisture content of 10% wa pacted by the extruder.
With the increasing die temperature, the value of densification p which means lower energy consumption in the densification process. H ity of pellets was not good, and the unit density was not qualified comp ards.
The friction coefficient between the corn straw and the die tended temperature increased from 40 to 200 °C, and the reference values of the at different temperatures were provided.

Conclusions
A mechanical extruder was designed and manufactured. The piston was forced to reciprocate to ensure that the corn straw could be squeezed into and out of the channel of the die, whose ratio of the length to the inside diameter is 4.5. Crushed corn straw with a particle size under 4 mm and with a given moisture content of 10% was used to be compacted by the extruder.
With the increasing die temperature, the value of densification pressure decreases, which means lower energy consumption in the densification process. However, the quality of pellets was not good, and the unit density was not qualified compared to the standards.
The friction coefficient between the corn straw and the die tended to decrease as the temperature increased from 40 to 200 • C, and the reference values of the friction coefficient at different temperatures were provided.
The proper temperature for corn straw densification was 100 • C, which led to decreasing nearly half of the required densification pressure, and the value of the unit density was above 1.0 g/cm 3 . Meanwhile, the surface quality of the pellet was comparatively good. Due to measurement or other experiment reasons, the effect of heating on the friction coefficient and the unit density will be further studied.