# Carbothermal Reduction of Iron Ore in Its Concentrate-Agricultural Waste Pellets

Authors: Zhulin Liu; Xuegong Bi; Zeping Gao; Wei Liu
Journal: Advances in Materials Science and Engineering
 (2018)

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## Abstract

Carbon-containing pellets were prepared with the carbonized product of agricultural wastes and iron concentrate, and an experimental study on the direct reduction was carried out. The experimental results demonstrated that carbon-containing pellets could be rapidly reduced at 1200 to 1300°C in 15 minutes, and the proper holding time at high temperature was 15 to 20 min. The degree of reduction gradually increased with temperature rising, and the appropriate temperature of reducing pellets was 1200°C. The weight loss rate and reduction degree of pellets increased with the rise of carbon proportion, and the relatively reasonable mole ratio of carbon to oxygen was 0.9. A higher content of carbon and an appropriate content of volatile matters in biomass char were beneficial to the reduction of pellets. The carbon-containing pellets could be reduced at high speeds in the air, but there was some reoxidization phenomenon.


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## Body

## 1. Introduction

In recent years, the research of carbon-containing pellets has attracted great attention of metallurgists. The carbon-containing pellets are composed of iron-containing powders and carbonaceous additives (coke breeze, petro-coke, pulverized coal, peat moss, and charcoal) blended with appropriate binders [1]. They are carbon- and iron-containing pellets or cold/hot briquettes made through pelletizing in a balling disc or through briquetting in a molding machine after thorough mixing. Carbon-containing pellets were originally used for the production of high-quality sponge iron [2, 3], and they could also be fed into the blast furnace. Yokoyama et al. [4] prepared ore/coal briquettes with cement as the binder (blending ratio was 10-11 mass%) and conducted a 80 day 54 kg/t charge test at Oita BF No. 2. A substantial reduction of fuel rate was confirmed by this test. It was attempted to partially substitute biomass char from Japanese cedar for pulverized coal in the preparation of carbon-containing iron ore hot briquettes [5]. The difference of reactivity between wood charcoal, bamboo charcoal, and coal were also investigated [6]. The raw material source of biomass char is wide; however, in China, the forest resource is poor, but the agricultural waste output is great. Charcoal bars made with agricultural crops as raw materials gradually form market for home heating in winter.It was reported that the carbon content in wheat and corn crops is about 40% and exceeds 43% in rice hull. The derived biomass char contains less ash, and the content of impurities such as sulfur and phosphorus are also very low. To apply it for producing carbon-containing pellets will not only contribute to the solution of the puzzle of effectively using agricultural waste in large scale but also improve the quality of iron and steel products.Effect of several factors such as maximum carbonization temperature of Japanese cypress, reduction temperature, and heating profile on fractional reductionF (%) after 60 min was experimentally studied in the laboratory by Hirokazu et al. [7]. Effect of coal content on the apparent density and the cold crushing strength and melt-down temperature of coal composite iron ore hot briquettes was investigated by Hayashi [8]. Kunishi et al. [9] confirmed by the XRD analysis of the reduced pellets that the carbon composite iron oxide pellets using the semi-Newcastle blend coal-char at a lower maximum carbonization temperature (823 K) have the highest reducibility of the iron oxide. Ariyama et al. [10] prepared the composite composed of iron oxide and plastic wastes and confirmed the importance of the composite structure and temperature profile on the effective utilization of pyrolysis gas released from plastics.Also was studied the impact of residual volatile matters in semicharcoal biomass on the reduction performance of iron ore pellets [11]. Because the reactivity of biomass char outclasses coke, Ueda et al. [12] carried out a research on how biomass char improved the reactivity of carbon-containing pellets. The mole ratio of carbon to oxygen, represented as C/O ratio hereinafter, was selected as 1.0. Japanese cedar-derived biomass char, and iron ore powders with no binders were mixed uniformly and pressed in a 10 mm die at 9.8 MPa to form a tablet of the sample. The temperature inside the test furnace was increased to 1000°C at a rate of 0.167°C/s, simulating the blast furnace shaft condition. The following main results were obtained: (1) the gasification reaction rate of biomass char is faster than that of coke in a couple of dozen times; (2) the reduction of the composite begins at about 550°C, and the reactivity of the carbon iron ore composite with biomass char is remarkably faster than that with coke; and (3) the reaction rate of carbon iron ore composite with highlyreactive reducing agent is controlled from both reaction rate of carbon gasification and iron ore reduction.Takyu et al. [13] tried to understand the reduction mechanism of iron ore and carbon composite by volatile matters in biomass char at low temperature. The iron ore and carbon composite were heated at a constant rate to 1473 K, and the CO and CO2 concentrations in waste gases were analyzed by an infrared absorption analyzer. It was found that the reduction degree at 1100 K increased with the amount of volatile matters. By making a comparison between the sample mixed with Biomass char 3 and the sample mixed with coal char, the CO content was decreased at temperatures below 1000 K while it was increased at higher temperatures. As for the CO2 content, it was increased when the temperature exceeded 900 K and reached the maximum at about 950 K, implying the indirect reduction reaction was expedited.The reducing agents applied in the study of carbon-containing pellets in China and abroad were so far coal and biomass char derived from wood materials. In this paper, the local abundant resource of rice hull and peanut shell in Hunan Province was utilized as raw materials to prepare biomass char, which was used to replace pulverized coal for preparing carbon-containing pellets and to study in laboratory the improvement effect of biomass char on pellets reducibility.


## 2. Materials and Methods

### 2.1. Experimental Materials

The concentrate for pellet preparation was provided by Xianggang Company, and the chemical composition is listed in Table1. The reducing agent was biomass chars prepared from rice husk and peanut shell through crushing, molding, and low temperature carbonization (300–350°C). In this work, two kinds of biomass chars with different chemical compositions were applied, aiming at studying the influence of char composition on reduction process of carbon-containing pellets. Their chemical compositions are given in Table 2. Bentonite was used as the binder, and its chemical composition is shown in Table 3.Table 1
Chemical composition of the concentrate (mass%).
T.Fe
S
P
FeO
SiO2
CaO
Al2O3
MgO
MnO
H2O∗
63.55
0.05
0.01
27.02
5.47
2.86
0.93
1.00
0.33
10.20
∗Free water content.Table 2
Approximate analysis of biomass chars (mass%).
Char
FCd
Vdaf
Ad
St,d
Mad
A
61.82
32.1
3.48
0.05
2.60
B
59.79
25.88
14.2
0.05
5.13
Note. Ad: air dry ash content; Vdaf: air dry and ash free volatile content; FCd: air dry fixed carbon content; St,d: air dry total sulfur content; Mad: internal water content.Table 3
Chemical component of bentonite (mass%).
Al2O3
CaO
MgO
SiO2
K2O
Na2O
I.L
Bentonite
12.65
1.02
4.19
53.25
0.43
0.3
14.39It is seen from Table1 that FeO content of the concentrate was 27.02%. The Fe2O3 content calculated from FeO% and the T.Fe% was 60.76%, and the corresponding total oxygen content was 24.23%, stating that this concentrate was a pure magnetite with T.Fe/FeO = 2.35.It can be seen from Table2 that the ash content and sulfur content in biomass char are low. Lower ash content benefits improving the blast furnace performance in terms of the reduction of flux consumption and the smelting of low silicon content pig iron. That the fixed carbon content is low and the volatile content is high is mainly because rather low carbonization temperatures were accepted in the preparation of biomass char, leading to an incomplete pyrolysis. But residual volatile matters will play the role of reduction in the reduction process of pellets because these materials begin to crack and generate H2 and C as temperature reaches nearly the maximum carbonization temperatures [11]. Also, the temperature range of the pyrolysis is much lower than that of starting reduction of iron oxide; it is therefore essential to design the composite structure and the temperature profile for realizing this temperature difference of the reactions simultaneously in the composite, in order to effectively utilize the pyrolysis gas as a reductant [10].


### 2.2. Carbon Proportioning

Three molar ratios of carbon to oxygen in pellets were selected for this study, that is, 0.8, 0.9, and 1.0. The corresponding amount of biomass char required for 1 kg iron ore concentrate, blend ratio of biomass char and carbon content in pellets could be calculated based on the mass balance of carbon and oxygen elements.Uniformly mix the concentrate, biomass char and bentonite (additional 6 mass%) weighed, pelletize the mixture in a balling disc and sift out the 8–12 mm section. In order to prevent pellets from breaking due to thermal stress in the preheating stage, it is needed to preheat green balls at 105°C for 2 h.


### 2.3. Equipment and Procedure

By applying the thermogravimetry technique (TG), carbon-containing pellets were heated and reduced in a MoSi2 bar electric resistant furnace, and the test apparatus is shown in Figure 1. The temperature of the furnace was measured with a Pt-30%Rh/Pt-6%Rh thermocouple, and the sample weight was measured with a 1 kg electronic balance of 0.001 g precision. The upper Fe–Cr–Mo wire basket with 30 mm ID and 100 mm height was connected with the electronic balance. Ten pellets of 25–30 g total weight with similar diameter were selected for one test, and before use, they were dried at 105°C for 2 h. The furnace heated up at 10°C/min as it was below 200°C while the heating rate was changed to 15°C/min as it was beyond 200°C. When the specified experimental temperature was reached, a N2 gas flow was purged at a rate of 3 L/min. The temperature was kept constant for 5 min, then the basket was quickly put into the furnace together with the sample, and its weight was continuously recorded.Figure 1
The schematic diagram of experimental apparatus. (1) Computer; (2) temperature controller; (3) electronic balance; (4) Mo wire; (5) MoSiO2 bar; (6) basket and samples; (7) atmosphere controller; (8) thermocouple.The experiment was conducted isothermally, the reduction temperature was respectively 1000, 1100, 1200, and 1300°C, and reduction time was respectively 5, 10, 15, and 20 min. After reduction, the sample was quickly taken out from the furnace and put into a tubular furnace purged with nitrogen for cooling to the room temperature.


### 2.4. Test Parameter Calculation

For usual iron ores, the degree of reduction can be calculated directly from the weight loss. In the weight loss of carbon-containing pellets, apart from oxygen loss, the carbon loss, the amount of volatile matters separated, and remaining water vaporized are also included. Most researchers made estimation according to the chemically analyzed value of total iron, metallic iron, and FeO contents in the reduced sample, this method can only obtain the final result of the degree of reduction and could not describe the reduction process. In this paper, the modified weight loss approach was utilized, that is, by taking carbon-containing alumina balls as a reference, to indirectly measure the separation ratio of volatile matters and water and to evaluate the degree of reduction with Equation (1), which originated from a reference and was modified in this work.(1)R=47MOfΣ−fA−PW×100%,where MO is oxygen amount in iron oxides, g; fΣ is the percentage of total weight loss, %; fA−P is the percentage of weight loss of volatile matters and moisture in carbon-containing alumina balls, %; and W is the weight of carbon-containing pellets, g.It is found in the experiment that release of volatiles is basically terminated at 5 min. The observed values offA−P at various temperatures and C/O ratios are shown in Table 4.Table 4
f
A−P value of carbon-containing alumina balls under different conditions (%).
Temperature, °C
Molar ratio of carbon to oxygen, −
f
A
−
P, %
1000
0.8
5.76
0.9
6.17
1.0
6.74
1100
0.8
6.30
0.9
6.64
1.0
7.35
1200
0.8
6.32
0.9
6.65
1.0
7.49
1300
0.8
6.33
0.9
6.66
1.0
7.49


## 2.1. Experimental Materials

The concentrate for pellet preparation was provided by Xianggang Company, and the chemical composition is listed in Table1. The reducing agent was biomass chars prepared from rice husk and peanut shell through crushing, molding, and low temperature carbonization (300–350°C). In this work, two kinds of biomass chars with different chemical compositions were applied, aiming at studying the influence of char composition on reduction process of carbon-containing pellets. Their chemical compositions are given in Table 2. Bentonite was used as the binder, and its chemical composition is shown in Table 3.Table 1
Chemical composition of the concentrate (mass%).
T.Fe
S
P
FeO
SiO2
CaO
Al2O3
MgO
MnO
H2O∗
63.55
0.05
0.01
27.02
5.47
2.86
0.93
1.00
0.33
10.20
∗Free water content.Table 2
Approximate analysis of biomass chars (mass%).
Char
FCd
Vdaf
Ad
St,d
Mad
A
61.82
32.1
3.48
0.05
2.60
B
59.79
25.88
14.2
0.05
5.13
Note. Ad: air dry ash content; Vdaf: air dry and ash free volatile content; FCd: air dry fixed carbon content; St,d: air dry total sulfur content; Mad: internal water content.Table 3
Chemical component of bentonite (mass%).
Al2O3
CaO
MgO
SiO2
K2O
Na2O
I.L
Bentonite
12.65
1.02
4.19
53.25
0.43
0.3
14.39It is seen from Table1 that FeO content of the concentrate was 27.02%. The Fe2O3 content calculated from FeO% and the T.Fe% was 60.76%, and the corresponding total oxygen content was 24.23%, stating that this concentrate was a pure magnetite with T.Fe/FeO = 2.35.It can be seen from Table2 that the ash content and sulfur content in biomass char are low. Lower ash content benefits improving the blast furnace performance in terms of the reduction of flux consumption and the smelting of low silicon content pig iron. That the fixed carbon content is low and the volatile content is high is mainly because rather low carbonization temperatures were accepted in the preparation of biomass char, leading to an incomplete pyrolysis. But residual volatile matters will play the role of reduction in the reduction process of pellets because these materials begin to crack and generate H2 and C as temperature reaches nearly the maximum carbonization temperatures [11]. Also, the temperature range of the pyrolysis is much lower than that of starting reduction of iron oxide; it is therefore essential to design the composite structure and the temperature profile for realizing this temperature difference of the reactions simultaneously in the composite, in order to effectively utilize the pyrolysis gas as a reductant [10].


## 2.2. Carbon Proportioning

Three molar ratios of carbon to oxygen in pellets were selected for this study, that is, 0.8, 0.9, and 1.0. The corresponding amount of biomass char required for 1 kg iron ore concentrate, blend ratio of biomass char and carbon content in pellets could be calculated based on the mass balance of carbon and oxygen elements.Uniformly mix the concentrate, biomass char and bentonite (additional 6 mass%) weighed, pelletize the mixture in a balling disc and sift out the 8–12 mm section. In order to prevent pellets from breaking due to thermal stress in the preheating stage, it is needed to preheat green balls at 105°C for 2 h.


## 2.3. Equipment and Procedure

By applying the thermogravimetry technique (TG), carbon-containing pellets were heated and reduced in a MoSi2 bar electric resistant furnace, and the test apparatus is shown in Figure 1. The temperature of the furnace was measured with a Pt-30%Rh/Pt-6%Rh thermocouple, and the sample weight was measured with a 1 kg electronic balance of 0.001 g precision. The upper Fe–Cr–Mo wire basket with 30 mm ID and 100 mm height was connected with the electronic balance. Ten pellets of 25–30 g total weight with similar diameter were selected for one test, and before use, they were dried at 105°C for 2 h. The furnace heated up at 10°C/min as it was below 200°C while the heating rate was changed to 15°C/min as it was beyond 200°C. When the specified experimental temperature was reached, a N2 gas flow was purged at a rate of 3 L/min. The temperature was kept constant for 5 min, then the basket was quickly put into the furnace together with the sample, and its weight was continuously recorded.Figure 1
The schematic diagram of experimental apparatus. (1) Computer; (2) temperature controller; (3) electronic balance; (4) Mo wire; (5) MoSiO2 bar; (6) basket and samples; (7) atmosphere controller; (8) thermocouple.The experiment was conducted isothermally, the reduction temperature was respectively 1000, 1100, 1200, and 1300°C, and reduction time was respectively 5, 10, 15, and 20 min. After reduction, the sample was quickly taken out from the furnace and put into a tubular furnace purged with nitrogen for cooling to the room temperature.


## 2.4. Test Parameter Calculation

For usual iron ores, the degree of reduction can be calculated directly from the weight loss. In the weight loss of carbon-containing pellets, apart from oxygen loss, the carbon loss, the amount of volatile matters separated, and remaining water vaporized are also included. Most researchers made estimation according to the chemically analyzed value of total iron, metallic iron, and FeO contents in the reduced sample, this method can only obtain the final result of the degree of reduction and could not describe the reduction process. In this paper, the modified weight loss approach was utilized, that is, by taking carbon-containing alumina balls as a reference, to indirectly measure the separation ratio of volatile matters and water and to evaluate the degree of reduction with Equation (1), which originated from a reference and was modified in this work.(1)R=47MOfΣ−fA−PW×100%,where MO is oxygen amount in iron oxides, g; fΣ is the percentage of total weight loss, %; fA−P is the percentage of weight loss of volatile matters and moisture in carbon-containing alumina balls, %; and W is the weight of carbon-containing pellets, g.It is found in the experiment that release of volatiles is basically terminated at 5 min. The observed values offA−P at various temperatures and C/O ratios are shown in Table 4.Table 4
f
A−P value of carbon-containing alumina balls under different conditions (%).
Temperature, °C
Molar ratio of carbon to oxygen, −
f
A
−
P, %
1000
0.8
5.76
0.9
6.17
1.0
6.74
1100
0.8
6.30
0.9
6.64
1.0
7.35
1200
0.8
6.32
0.9
6.65
1.0
7.49
1300
0.8
6.33
0.9
6.66
1.0
7.49


## 3. Results and Analysis

### 3.1. Effect of C/O Ratio on Reduction of Carbon-Containing Pellets

The plot of reduction degree of carbon-containing pellets with different C/O molar ratios at 1200°C against time are depicted in Figure2.Figure 2
Variation of reduction degree of carbon-containing pellets of different C/O ratios with time at 1200°C.As shown in Figure2, the C/O ratio influences the reduction rate and the degree of reduction at 20 min. As the C/O ratio was increased from 0.8 to 0.9, the reduction was accelerated before 10 min, and it was more obviously accelerated as the C/O ratio was further increased to 1.0. The degree of reduction at 20 min was increased by 5.88% when the C/O ratio was increased from 0.8 to 0.9, but it almost did not change at all when the C/O ratio was further increased to 1.0, stating that it is reasonable to control the C/O ratio at a level of 0.9.It was experienced that too high C/O ratios will deteriorate the ballability of pelletizing mixture and the strength of product pellets, which would also justify the use of 0.9 C/O ratio.


### 3.2. Effect of Temperature on Reduction of Carbon-Containing Pellets

The plot of the degree of reduction of carbon-containing pellets (C/O = 0.9) against time at different temperatures is shown in Figure3.Figure 3
Reduction degree of carbon-containing pellets with C/O ratio of 0.9 at different temperatures.It is known from Figure3 that when temperature is lower than 1200°C, increasing temperature can substantially promote reduction, and the degree of reduction at 1200°C could reach 92.17%, 7.37% higher than at 1100°C and 24.83% higher than at 1000°C, and that the effect of increasing temperature on reduction improvement was little when it exceeded 1200°C. It is known that during reduction of carbon-containing iron ore pellets, direct reduction as well as indirect reduction takes place simultaneously. Equilibrium concentration of CO of C + CO2 = 2CO is greater at higher temperatures, and consequently, an increase in temperature contributes to the improvement of indirect reduction of pellets from the view point of reaction kinetics. The direct reduction is an endothermic reaction, stating that an increase in temperature contributes to the improvement of direct reduction of pellets from the view point of reaction thermodynamics. Also, an increase in temperature will bring about a more complete escaping and pyrolysis of volatile matters in biomass char. As a result, the degree of reduction was increased with temperature increasing.When temperature was over 1200°C, however, the benefit of these aspects reached the maximum, and the effect of further increasing temperature would thus not be substantial.


### 3.3. Composition of Biomass Char

The carbon-containing pellets blended with char B was reduced isothermally at 1200°C, and the variation of the degree of reduction with time is depicted in Figure4. Also in this figure, the reduction experiment results of the carbon-containing pellets blended with char A was shown.Figure 4
Plot of reduction degree of pellets blended with different biomass chars at 1200°C against time.It can be seen from Figure4 that, in the primary 5 minutes, the reduction behavior of these two kinds of pellets were basically the same, but soon afterwards, the reduction velocity of pellets blended with char B became more and more slowly, the difference with pellets blended with char A enlarged, and at 20 min the degree of reduction of this couple differed by 4.82%. The ratio of Vdaf to FCd of char A is 0.5192 while that of char B is 0.4328; it can thus be understood that at a same C/O ratio, the amount of volatile matters in pellets blended with char B is less than that in pellets blended with char A, meaning that the role played by volatile matters in pellet reduction is less. Furthermore, the escape of volatile matters during reduction will generate vacancies which are favorable for the quick diffusion of CO gas within pellets, contributing to the pellet reduction. The reason from these two aspects brings about that the degree of reduction of pellets blended with char B is not as high as that of pellets blended with char A, and the first reason is the prime.


### 3.4. Atmospheric Condition

The curve of reduction degree of pellets with 0.9 C/O ratio under air and N2 atmospheres at 1200°C are shown in Figure 5.Figure 5
Plot of reduction degree of pellets under different atmospheres at 1200°C against time.It can be seen from Figure5 that, at 1200°C, pellets can be reduced at high speeds under the atmosphere of nitrogen and air, and the reduction speed under air atmosphere within the first 10 minutes is even faster. The blend ratio of biomass char in the 0.9 C/O ratio pellets was 18.60%, and char fines were surrounded by iron ore particles, implying the condition of combustion of char fines is poorer and that the weight loss caused by combustion of carbon would be small. Therefore, it is presumed that the promoted reduction in air would be mainly because CO gas generated from reduction reacts with oxygen in air and releases heat, supplying the heat consumed by the direct reduction, and that the generated CO2 gas can also impede the reoxidation of iron. Till the final phases of reaction, however, the degree of reduction of pellets gradually decreases, resulted from that along with the combustion of carbon element, the amount of CO2 that plays the role of protection becomes less and less, and part of iron will be reoxidized.


## 3.1. Effect of C/O Ratio on Reduction of Carbon-Containing Pellets

The plot of reduction degree of carbon-containing pellets with different C/O molar ratios at 1200°C against time are depicted in Figure2.Figure 2
Variation of reduction degree of carbon-containing pellets of different C/O ratios with time at 1200°C.As shown in Figure2, the C/O ratio influences the reduction rate and the degree of reduction at 20 min. As the C/O ratio was increased from 0.8 to 0.9, the reduction was accelerated before 10 min, and it was more obviously accelerated as the C/O ratio was further increased to 1.0. The degree of reduction at 20 min was increased by 5.88% when the C/O ratio was increased from 0.8 to 0.9, but it almost did not change at all when the C/O ratio was further increased to 1.0, stating that it is reasonable to control the C/O ratio at a level of 0.9.It was experienced that too high C/O ratios will deteriorate the ballability of pelletizing mixture and the strength of product pellets, which would also justify the use of 0.9 C/O ratio.


## 3.2. Effect of Temperature on Reduction of Carbon-Containing Pellets

The plot of the degree of reduction of carbon-containing pellets (C/O = 0.9) against time at different temperatures is shown in Figure3.Figure 3
Reduction degree of carbon-containing pellets with C/O ratio of 0.9 at different temperatures.It is known from Figure3 that when temperature is lower than 1200°C, increasing temperature can substantially promote reduction, and the degree of reduction at 1200°C could reach 92.17%, 7.37% higher than at 1100°C and 24.83% higher than at 1000°C, and that the effect of increasing temperature on reduction improvement was little when it exceeded 1200°C. It is known that during reduction of carbon-containing iron ore pellets, direct reduction as well as indirect reduction takes place simultaneously. Equilibrium concentration of CO of C + CO2 = 2CO is greater at higher temperatures, and consequently, an increase in temperature contributes to the improvement of indirect reduction of pellets from the view point of reaction kinetics. The direct reduction is an endothermic reaction, stating that an increase in temperature contributes to the improvement of direct reduction of pellets from the view point of reaction thermodynamics. Also, an increase in temperature will bring about a more complete escaping and pyrolysis of volatile matters in biomass char. As a result, the degree of reduction was increased with temperature increasing.When temperature was over 1200°C, however, the benefit of these aspects reached the maximum, and the effect of further increasing temperature would thus not be substantial.


## 3.3. Composition of Biomass Char

The carbon-containing pellets blended with char B was reduced isothermally at 1200°C, and the variation of the degree of reduction with time is depicted in Figure4. Also in this figure, the reduction experiment results of the carbon-containing pellets blended with char A was shown.Figure 4
Plot of reduction degree of pellets blended with different biomass chars at 1200°C against time.It can be seen from Figure4 that, in the primary 5 minutes, the reduction behavior of these two kinds of pellets were basically the same, but soon afterwards, the reduction velocity of pellets blended with char B became more and more slowly, the difference with pellets blended with char A enlarged, and at 20 min the degree of reduction of this couple differed by 4.82%. The ratio of Vdaf to FCd of char A is 0.5192 while that of char B is 0.4328; it can thus be understood that at a same C/O ratio, the amount of volatile matters in pellets blended with char B is less than that in pellets blended with char A, meaning that the role played by volatile matters in pellet reduction is less. Furthermore, the escape of volatile matters during reduction will generate vacancies which are favorable for the quick diffusion of CO gas within pellets, contributing to the pellet reduction. The reason from these two aspects brings about that the degree of reduction of pellets blended with char B is not as high as that of pellets blended with char A, and the first reason is the prime.


## 3.4. Atmospheric Condition

The curve of reduction degree of pellets with 0.9 C/O ratio under air and N2 atmospheres at 1200°C are shown in Figure 5.Figure 5
Plot of reduction degree of pellets under different atmospheres at 1200°C against time.It can be seen from Figure5 that, at 1200°C, pellets can be reduced at high speeds under the atmosphere of nitrogen and air, and the reduction speed under air atmosphere within the first 10 minutes is even faster. The blend ratio of biomass char in the 0.9 C/O ratio pellets was 18.60%, and char fines were surrounded by iron ore particles, implying the condition of combustion of char fines is poorer and that the weight loss caused by combustion of carbon would be small. Therefore, it is presumed that the promoted reduction in air would be mainly because CO gas generated from reduction reacts with oxygen in air and releases heat, supplying the heat consumed by the direct reduction, and that the generated CO2 gas can also impede the reoxidation of iron. Till the final phases of reaction, however, the degree of reduction of pellets gradually decreases, resulted from that along with the combustion of carbon element, the amount of CO2 that plays the role of protection becomes less and less, and part of iron will be reoxidized.


## 4. Conclusions

Carbon-containing pellets were produced with agricultural waste-derived biomass chars, and the influence of factors such as C/O ratio, temperature, and char chemical composition on the pellets reduction was experimentally studied, reaching the following conclusions:(1)
The appropriate C/O ratio is 0.9 and lower than 1.0, which is due to the occurrence of indirect reduction and that the volatile content in the biomass char is higher and the CO and H2 gases generated by the pyrolysis of volatile materials during reduction also take part in the reduction of iron oxides.(2)
As lower than 1200°C, increasing temperature could substantially promote reduction, the degree of reduction at 1200°C could reach 92.17%, when temperature exceeds 1200°C; however, increasing temperature has little effect on reduction reaction.(3)
The chemical composition of biomass char has an important impact on the reducing properties of carbon-containing pellets, and higher carbon contents and biggerVdaf/FCd ratios will promote the reduction reaction.(4)
Carbon-containing pellets could be quickly reduced even in the air atmosphere, in comparison with the reduction tests in the nitrogen atmosphere, and the reduction speed during the first 10 minutes is even higher and the maximum degree of reduction is bigger, but when the carbon blended is essentially completely consumed, the secondary oxidation phenomenon will take place.



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*Source: 2138268-2018-01-17.xml*