Experimental Study and Design of Biomass Co-Firing in a Full-Scale Coal-Fired Furnace with Storage Pulverizing System
by
Xuebin Wang
1, 
Zia Ur Rahman
1,
Zhaomin Lv
1,
Yiming Zhu
1,
Renhui Ruan
1,
Shuanghui Deng
1,
Lan Zhang
2 and
Houzhang Tan
1,* 1
MOE Key Laboratory of Thermo-Fluid Science and Engineering, Xi’an Jiaotong University, Xi’an 710049, China
2
Henan Province Boiler Pressure Vessel Safety Inspection Institute, Zhengzhou 450016, China
*
Author to whom correspondence should be addressed.
Agronomy 2021, 11(4), 810; https://doi.org/10.3390/agronomy11040810
Submission received: 17 March 2021
/
Revised: 13 April 2021
/
Accepted: 14 April 2021
/
Published: 20 April 2021
(This article belongs to the Special Issue Valorization of Agricultural Residues to Renewable Energy and Value-Added Products)
Abstract
:Co-firing coal and biomass in existing power plants facilitates influential advancement in the use of renewable energy resources and carbon emissions reduction. Biomass is intended as a CO2-zero net emission because, during its rise, it uses the same fraction of CO2 from the air as that released during its combustion. In addition, the content of nitrogen and sulfur in biomass is lower than in coal. Therefore, the emissions of NOx and SOx can be minimized by co-firing it with coal. In general, the effect of biomass direct co-firing on safety, pulverizing system performance, furnace efficiency, and NOx emission in full-scale furnaces is rarely studied. In this study, biomass direct co-firing was carried out in a 55 MW tangentially fired pulverized coal furnace. The effects of biomass co-firing on safety, the performance of the pulverizing system, furnace efficiency, and pollutant emissions (unburned carbon and NOx) are studied. The results show that the blending of biomass fuel with less than 20% of coal has no issue with respect to auto-ignition and safety. The performance of the pulverizing system is affected up to a certain limit due to the difficulty of grinding the biomass particles into required fineness. The biomass co-firing up to 20% is feasible, but greater than this percentage will severely affect the furnace efficiency. The co-firing of biomass enhanced the NOx reduction significantly and further improved the performance of the SNCR process. This study could provide guidance for the application of biomass co-firing in industrial furnaces.
1. Introduction
Coal is the world’s largest source of energy for electricity production [1]. Coal contributes more than 38% to the production of the world’s electricity. However, coal is the world’s prominent source of CO2 production [2]. Today, the world is facing major challenges in reducing greenhouse gas (GHG) pollution. All developed and developing countries are making heavy investments to replace conventional fuel with renewable energy resources.
Co-firing biomass has a vital role in achieving these new energy objectives, as it can reduce the potential environmental consequences of fossil fuels combustions [3,4,5,6]. In co-firing, greenhouse gasses, such as CO2, NOx, and SOx can be reduced when replacing a portion of coal with biomass [7,8,9,10,11]. Biomass is intended as a CO2-zero net atmospheric emission because, during its rise, it uses the same fraction of CO2 from the air as that released during its combustion. Despite the usefulness of biomass co-firing, it has a high alkali and chlorine content. Therefore, the burning of 100% biomass can lead to a severe complication of slagging and corrosion, and this can be circumvented sufficiently when co-firing biomass is used with coal [12,13].
Relatively rapid advances in co-firing have been carried out worldwide over the past decades, since the 1970s [14].
Several Asian countries, such as Japan, China, and South Korea, have already started co-firing technologies [2]. Wood pellets co-fired with coal are regarded in these regions as the primary source of electricity [15]; Nevertheless, a large part of the wood pellets remains unused for co-firing with biomass. Several concerns have been raised in relation to the production of biomass energy. Such issues include the stable supply of raw materials, the availability of wood products, and the establishment of a supply chain [2].
China is a rich biomass resourceful country, and the potential volume of biomass is about 5 billion tons of coal equivalent, nearly three times that of total current energy use [16]. The development of biomass power in China began in 2004; the first three biomass energy production projects were approved by the National Development and Reform Commission; developed in Shandong, Hebei, and Jiangsu provinces. At the end of 2006, in Dan County, Shandong Province, the project for the development of biomass energy (with a generating unit of 12.5 kW) was commissioned [14].
However, the market for the production of biomass power in China is still limited, and the laws and regulations for the production of biomass power are incomplete. Due to scattered materials and long logistics chain, high production costs, outdated equipment, technical immaturity, inadequate raw materials, and extreme investment shortages, the cost of generating biomass energy is higher than that of generating thermal power and hydroelectric power. Consequently, the development of biomass energy in China requires further policy support [16]. Biomass electricity generation involves biomass collection, processing, transport, storage, combustion equipment adaptability, process management, etc. Particularly because it is challenging to design and produce biomass boilers, the investment in imported and domestic equipment is approximately USD 1545.21/kWh and USD 1236.17/kWh, respectively, whereas the investment in thermal power equipment accounts for only 50% [17].
Several studies have been conducted on the co-firing of biomass with coal and the power trade of biomass. Anes Kazagic et al. [18] assessed the reasonable expectation that under actual operating conditions of a PC large boiler, tested coal/woody biomass/Miscanthus blends could be effectively co-fired without major ash-related issues. However, by increasing the biomass ratio above 15% the UBC ratio in the ash slag may increase. Larry Baxter [19] presented biomass-coal co-combustion as a short-term, low-risk, low-cost, clean, renewable energy solution promising to minimize competitive CO2 emissions, lower SOx and often NOx emissions, and many social benefits. Although, it has some technical problems, such as fuel supply, processing problems with oxidation, reduced overall performance, and ash deposition. Minsung Choi et al. [20] evaluated the 0–30% ratio of woody biomass and bituminous coal combustion using woody biomass, and it was found that woody biomass co-fired flames had a higher overall temperature than pure bituminous fuel flames. Rui Luo and Qulan Zhou [21] investigated the impact of carbon ash content, mixing ratio, and oxygen concentration on the biomass–coal interaction. It has been shown that mixtures of coal and biomass burning energy variability are influenced by carbon ash content, and biomass mixing will help to efficiently burn coal with low ash content.
However, some major unresolved issues still need to be addressed, such as co-firing biomass modes, pulverizing methods, safety, storage, economy, pollutant emissions, and the most important is efficiency. Since an efficient, safe, and economic co-firing mode of biomass remains the main requirement for the large-scale use of biomass in China. The aim of this paper is to test the most economical direct mode of co-firing biomass in a full-scale coal-fired power plant of 55 MW. Primarily focused on the effect of biomass co-firing on the operating safety of pulverizing and fuel storage systems, the efficiency, and pollutant emissions of power plants. This study could provide guidance for the application of biomass co-firing in industrial furnaces.
2. Distribution of Biomass Resource around the Power Plant
To cope, one of the main challenges, which is very crucial for a productive and sustainable operation of biomass co-firing, is the availability of biomass resources around the plant area. In this study, the distribution of biomass resources is surveyed in a 100 km area around the power plant location, as shown in Figure 1. The plant is located in Baishui County, which covers Weinan, Yan’an, Tongchuan, and Xi’an. It mainly includes 16 counties and districts, such as Baishui, Huanglong, Fuping, Hancheng, Chengcheng, Heyang, Dali, Hua, Huangling, Luochuan, Fuxian, Yijun, Wangyi, Yintai, Yaozhou, and Yanliang. Baishui County, located in the northeast of Shaanxi province, is in the transition zone between Guanzhong plain and the northern Shaanxi plateau. It is the key point connecting Guanzhong and northern Shaanxi and is named for the Baishui River within the territory. The county has an arable land area of 48,000 hectares, a grain planting area of 34,596 hectares (including spring and autumn), and an apple planting area of 36,666 hectares, earning the reputation of “China’s apple town”. The capacity of biomass resources is summarized in Table 1. The agricultural statistical data in Table 1 are collected from the government of several counties. When the 55 MW power plant is operated with 100% coal, it required 0.5 million tons per year. By calculating the biomass requirement for 20% co-firing with coal, it will be required 0.1 million ton per year while the biomass resources available in 100 km area around the plant are up to 4 million ton, which is ten times greater than the required resources for co-firing. Furthermore, the heating values and proximate analysis of available biomass resources are portrayed in Table 2.
3. Research Method
3.1. Biomass Co-Firing System
The experimental setup of the mentioned biomass co-firing power plant is shown in Figure 2. First, the pulverized coal and biomass powder are mixed, which form a fuel mixture, and then are stored in the fuel tank. After this, it is supplied to the ball mill, where it is ground into a fine powder. Then it is passed through a coarse powder separator where the fine powder is sent into the fine powder separator while the coarse particles are recycled into the ball mills. The heavy particles from the fine powder separator are stored in the powder storehouse while the light particles are fed into the furnace through tertiary air. The induced draft fans are connected to the powder storehouse, which deliver the fine fuel particles to the furnace through primary air. Secondary air is also provided as an alternative to the primary air so to enhance combustion. In addition, separated over-fire air is supplied in the last section, as shown in Figure 2, to complete the combustion of remained unburned carbon and hydrocarbon radicles. The clear distribution pattern of different types of air is illustrated in Figure 2b.
3.2. Fuel Properties
The fuel properties of biomass co-firing fuel sampled from the storehouse are investigated by proximate analysis, ultimate analysis, and calorific value at different test conditions given in Table 3. The contents of N, C, and S of biomass are lower while H and O are higher, respectively, than that of pure pulverized coal. Moreover, biomass fuel’s moisture and volatiles are much higher than pulverized coal, whereas the ash content is significantly lower than pulverized coal. Further, with the increase in biomass mixing ratio, the moisture content increased slightly. The small proportion of biomass mixing did not significantly increase the volatiles, but when the mixing balance reached 20%, the volatiles increased significantly. Besides, the calorific value of biomass is substantially lower than that of coal. However, with the increase in the biomass-mixing ratio, the calorific value of the fuel from the pulverizing system (silo) only slightly reduced. The analysis revealed that the properties of fuel powder in co-firing cases are not significantly changes than that of 100% coal case, as shown in Table 3. Since it seemed that due to the low density of biomass particles, most biomass particles are separated in the fine-powder separator and passed into the furnace through the tertiary airports.
3.3. Experimental Procedure
In the test, the pulverizing system, i.e., ball mill and powder storehouse, were running under negative pressure to feed the biomass and pulverized (co-fired fuel) into the furnace for combustion. Overall, four groups of tests were conducted:(1) pure pulverized coal combustion; (2) 5% biomass mixing; (3) 10% biomass mixing; (4) 20% biomass mixing. First, the pure pulverized coal combustion test (1) was carried out and then followed by tests (2)–(4). Each test group was run twice; one with ammonia supply and the other without ammonia, to evaluate the efficiency of the SNCR process for NOx emission control. During experiments (1)–(4), the boiler operating load and other parameters kept stable. All of the test conditions are summarized in Table 4. The measured parameters were the coal mill outlet temperature, fineness of the mixed fuel (coal + biomass) powder, the temperature of the different location in the powder storehouse, the temperature of the primary air, CO at the outlet of the mill and in the powder storehouse, unburned carbon in fly ash and slag, boiler efficiency, NOx emission, and the effect of co-firing on SNCR. Air staging was applied to analyze its impact on ignition, combustibility, and NOx emission. The design parameters of primary, secondary, and tertiary air are illustrated in Table 5. Mastersizer 2000 (Malvern Instrument Ltd., Malvern, UK) was used to measure the size distribution of the pulverized biomass particles from the outlet of mill F. Testo 350 (Testo Ltd., Lenzkirch, Germany) was used to detect the emission of gaseous emissions. An infrared thermometer 3iLRL3 (Raytek Ltd., Ashington, UK) was used to measure the furnace temperature.
4. Results and Discussion
This section will present the results of the safety study on biomass co-firing pulverizing and powder-storage systems, as well as the effects of biomass co-firing on the pulverizing system, furnace efficiency, and NOx efficiency, respectively.
4.1. Safety Analysis on Pulverizing and Powder-Storage System Used for Biomass Co-Firing
Two key parameters, namely carbon monoxide (CO) concentration and temperature, were analyzed at different locations of the pulverizing device, powder storehouse, and in the primary air to assess the safety of pulverizing and powder-storage systems used for biomass co-firing. CO is a readily combustible gas that can easily be generated in fuel-rich conditions, while temperature is the primary determinant of fuel autoignition. In this regard, the CO concentration at different points in the pulverizing system, i.e., at the outlet of the coal mill, the upper space of the powder storehouse, and in the primary air, respectively, were tested, and the results are shown in Figure 3a,b respectively. In addition, the temperatures at three locations in the powder storehouse and in the primary air were measured to evaluate the safety status of the pulverizing system after mixing the biomass with coal; the results are summarized in Figure 4a,b respectively. The locations of different measurement points are shown in Figure 2a. It can be seen from the test results that, despite the addition of biomass fuel, the CO concentration at the outlet of the coal mill and the upper part of the powder bin is still very low (the highest is only 6 ppm, Figure 3a). Further, the CO concentration in hot primary air is in the range of 115–173 ppm, which is comparable with the value of 130 ppm in a 100% coal case (Figure 3b). Moreover, the powder bin’s temperature at all three points, the top, middle, and bottom, decreased with the increase of the biomass mixing proportion, and the maximum temperature was less than 75 °C, as illustrated in Figure 4a. Similarly, the temperature of the primary air-coal mixture and secondary air at the left and right side of the furnace depicted in Figure 4b is also less than the temperature of 100% coal stream.
4.2. Effect of Biomass Co-Firing on Pulverizing System
In this experiment, biomass co-firing affected the performance of the pulverizing system to a certain degree. This power plant pulverizing system is comprised of two main raw mills, R90 and R200. The names are given based on the particle size produced by each mill, such that R90 and R200 pulverizing raw fuel into 90 and 200 micrometers (µm) sizes, respectively. By increasing the biomass co-firing ratio from 0 to 20 wt.%, the values of fuel powder fineness produced by R90 and R200 increased from 17.5% and 1.0% to 19% and 4%, respectively, as shown in Figure 5a. Likewise, the particle size at the outlet of D50 and D90 increased from 30 μm and 100 μm to 40 μm and 160 μm, respectively, as illustrated in Figure 5b.
4.3. Effect of Biomass Co-Firing on Furnace Efficiency
It was observed during the experiment that the blending of biomass had a certain effect on the burnout of the fuel. As shown in Table 6 with the increase in the biomass co-firing ratio from 0 to 20 wt.%, the unburned carbon content (UBCs) in fly ash and slag rose. The rise in UBCs was due to the drop-in furnace temperature, as can be seen from the exhaust temperature in Table 6. Consequently, the furnace efficiency is slightly reduced with the increasing blending ratio of biomass with co-firing coal.
4.4. Effect of Biomass Co-Firing on NOx Emissions
The effect of biomass co-firing on NOx emissions was studied, and the results are illustrated in Figure 6. The tests were conducted on the four condition types (coal, 5% biomass, 10% biomass, and 20% biomass) with and without supplying ammonia (SNCR process). It was observed that the co-firing of biomass was beneficial for reducing NOx even without applying the SNCR process. As shown in Figure 6a, at 20 wt.% biomass co-firing ratios, the NOx emission before the De-NOx system decreased by 24.5%, as compared to the 100% coal combustion. It can also be seen from Figure 6a that NOx reduction further increased by providing ammonia (SNCR process) [22]. As shown in Figure 6b, the overall de-NOx efficiency by using the SNCR in co-firing biomass steadily increased from 56% to 71%, as the biomass fraction increased from 0% to 20%.
5. Discussion
Co-firing biomass with coal raises some safety issues that involve the additional potential for fire and explosion. Biomass is much more reactive than the majority of coal, pet coke, and anthracite. It is therefore important to evaluate the risk of explosion for such mixtures. Two main parameters, i.e., CO and temperature, were evaluated to ensure safety with respect to fire and explosion. Results in Section 3.1 illustrate that the CO concentration in the coal mill and powder storage was still in the safe zone even with the different percentages of biomass co-firing with coal. Moreover, the temperature fell by increasing the mixing proportion of biomass in the co-firing system. There are two main reasons for this phenomenon: the relatively high moisture content in the mixed biomass and the low calorific value of the biomass as compared to pure coal [12]. This means that there is no risk of auto-ignition by mixing the biomass with coal up to 20%, and it has no risk regarding safety when operated with biomass co-firing.
The size of the pulverized biomass particles depends primarily on the type of mill used, and it is costly to manufacture small fibrous biomass particles. As a consequence, it is expected that the large particles present in the biomass supply would influence the dynamics of combustion [23]. Results from Section 3.2 portray that the particle size from the pulverizing system continuously increased with the increasing blending ratio of biomass with coal co-firing. The increase in size, with the increasing biomass proportion, is due to the tenacious fibrous and non-friable nature of biomass [24]. Due to the difficulty of grinding the biomass particles into required fineness, it rarely decreased the output performance of the pulverizing system. Based on the experiment results, it is suggested that mixing biomass up to 20% is appropriate in terms of the fineness of the co-firing fuel. However, if the blending ratio exceeds 20%, the pulverizing system’s performance will suffer.
Section 3.3 concludes that the furnace efficiency slightly decreased with the increasing blending ratio of biomass with coal co-firing. The volatile content in the biomass compared to pure coal is significantly larger. In addition, the inherent fibrous structure, the irregular biomass particle shape, higher aspect ratio, the lower energy density, and lower calorific value were all main causes of UBCs and lower temperature [25]. With the biomass co-firing method, the rise in UBCs and a slight decrease in exhaust temperature contributed to a decline in furnace efficiency of up to 7.0 wt.%. A similar result was also noticed by Y. Huang et al. [26], who portrayed that the net furnace efficiency had declined with the increase of biomass fraction as a co-firing with coal. They concluded that the efficiency on thermal bases decreased by up to 2.3%, with the biomass fraction rising from 0% to 40% relative to the base case (100% coal). Therefore, it is concluded that the fraction of biomass in co-firing up to 20% is feasible, but greater than this percentage; it would severely affect the performance of the furnace [7,13,27].
It is illustrated in Section 4.4 that co-firing biomass with coal is very beneficial in reducing the NOx. There are various potential explanations for the reduction of NOx when biomass is co-fired with coal. The first one is generally the low contents of nitrogen in the biomass as compared to pure coal [28]. The second is the high content of volatile in biomass as compared to pure coal. Furthermore, at the beginning of biomass combustion, oxygen is rapidly consumed by a large quantity of volatiles produced during the devolatilization phase, which generates a reduced environment that is very suitable for the reduction of NOx. In addition, radicals such as CHi have been produced in large quantities due to the high content of volatiles in biomass, and these radicals have been highly efficient in the reduction of NO to N2 [28,29]. In addition, air staging is also one of the main reasons for the reduction of NOx. The basic principle of air staging for NOx control is to generate a fuel-rich condition in the primary section of the furnaces, where the hydrocarbon radicles can easily consume the oxygen of NOx and reduced it into the N2 [30]. Then staged over-fire air is supplied above the primary zone to complete burnout of the remaining traces of fuel.
Further, the de-NOx efficiency of the SNCR process is enhanced by increasing the biomass blending ratio from 0% to 20%. This is due to the synergistic effect of both the co-fired biomass and the SNCR process leading to a better de-NOx efficiency [31]. In addition, the biomass also contains high alkali metals, such as potassium, calcium, and sodium, which could have a catalytic effect in enhancing the performance of the SNCR [32,33]. J. Hoa et al. [34] illustrated in their experimental work that the Na/K additive had a prominent enhancement effect in NOx reduction by SNCR and that the enhancement effect was in the order of Na2CO3 > KCl > NaCl. The promotional effect of alkali metal is explained by the fact that it accelerates the production of more reactive OH radicles during the SNCR process, which improves the SNCR performance by mainly increasing the production rate of NH2 radicals [35].
6. Conclusions
In this study, biomass direct co-firing was carried out in a 55 MW tangentially fired pulverized coal furnace. The effects of biomass co-firing on safety, the performance of the pulverizing system, furnace efficiency, and pollutant emissions were studied. The main conclusions are:
- CO and temperature were measured at different plant locations for the safety purposes of the biomass co-fired process. Both parameters were safe and concluded that the blending of biomass fuel with less than 20% of coal has no issue with respect to auto-ignition.
- The pulverized size of the co-fired fuel was increasing with the increasing biomass co-firing ratio due to the tenacious fibrous and non-friable nature of biomass. Due to the difficulty of grinding the biomass particles into required fineness, it rarely decreased the output performance of the pulverizing system.
- The increase in UBCs and the slight decrease in exhaust temperature contributed to a decrease in furnace efficiency of up to 7.0 wt.% with the biomass co-firing method. It is concluded that up to 20% of the fraction of biomass in co-firing is feasible, but greater than this percentage will severely affect the furnace efficiency.
- The co-firing of biomass is supportive in the enhancement of the NOx reduction and could significantly increase the thermal de-NOx efficiency.
Author Contributions
Conceptualization, X.W., Z.U.R., and H.T.; methodology, X.W., Z.U.R., and H.T.; validation, X.W., Z.U.R., Z.L., Y.Z., and H.T.; formal analysis, X.W., Z.U.R., Z.L., Y.Z., R.R., S.D., L.Z., and T.H; investigation, X.W., Z.U.R., Z.L., Y.Z., R.R., S.D., L.Z., and H.T.; resources, X.W., and H.T.; writing—original draft preparation, X.W. and Z.U.R.; writing—review and editing, X.W. and Z.U.R.; supervision, X.W. and H.T.; project administration, X.W., and H.T.; funding acquisition, X.W., L.Z., and H.T. All authors have read and agreed to the published version of the manuscript.
Funding
This research was funded by the National Key Research and Development Program of China (No. 2020YFC1910000), the National Natural Science Foundation of China (Nos. 51761125012), the Key Scientific and Technological Projects in Henan Province (182102410053) and the Natural Science Basic Research Plan in Shaanxi Province of China (2021JC-03).
Institutional Review Board Statement
Not applicable.
Informed Consent Statement
Not applicable.
Data Availability Statement
Data reported within the article.
Acknowledgments
The authors gratefully acknowledge the National Key Research and Development Program of China (No. 2020YFC1910000), the National Natural Science Foundation of China (Nos. 51761125012), the Key Scientific and Technological Projects in Henan Province (182102410053) and the Natural Science Basic Research Plan in Shaanxi Province of China (2021JC-03).
Conflicts of Interest
The authors declare no conflict of interest.
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Figure 1.
Power plant location and biomass collection area.
Figure 2.
(a) Biomass co-firing system (b) burner port layout.
Figure 3.
CO concentration in (a) pulverizing, powder storage, and (b) transporting system.
Figure 4.
Temperatures in (a) powder-storage and (b) transporting system.
Figure 5.
Particle sizes at different biomass co-firing ratios; (a) fuel fineness %, and (b) average particle sizes.
Figure 5.
Particle sizes at different biomass co-firing ratios; (a) fuel fineness %, and (b) average particle sizes.
Figure 6.
Effect of biomass co-firing on (a) NOx emission and (b) de-NOx efficiency.
Table 1.
Available biomass resources in the area with collection diameter 100 km (unit: ×1000 ton).
| County Name | Food Crop Biomass (×1000 ton) | Fruit Tree Biomass (×1000 ton) | Others (×1000 ton) | Total (×1000 ton) |
|---|---|---|---|---|
| Baishui | 181.7 | 192.5 | 34.6 | 408.7 |
| Fuping | 420.0 | 63.0 | 40.3 | 523.3 |
| Hancheng | 147.0 | 35.7 | - | 182.7 |
| Chengcheng | 225.4 | 171.4 | 7.7 | 404.5 |
| Henyang | 315.0 | 182.0 | 35.0 | 532.0 |
| Dali | 217.0 | 140.0 | 117.6 | 474.6 |
| Huaxian | 151.7 | 21.0 | 113.4 | 286.1 |
| Huangling | 67.9 | 87.5 | - | 155.4 |
| Huanglong | 63.4 | 11.2 | - | 74.6 |
| Luochuan | 64.1 | 178.5 | - | 242.6 |
| Fuxian | 89.6 | 140.0 | - | 229.6 |
| Yijun | 136.5 | 122.5 | - | 259.0 |
| Wangyi | - | 7.0 | - | 7 |
| Yanliang | 99.2 | - | - | 99.2 |
| Pucheng | 231.0 | 141.8 | - | 372.8 |
| Total | 2409.4 | 1494.0 | 348.6 | 4252.0 |
Note: the available biomass resource is calculated by “Planting area (unit: acre)” ×0.5 ton/acre ×0.7, where 0.5 ton/acre means per acre planting area can produce 0.5-ton biomass, and 0.7 is the collection efficiency.
Table 2.
Proximate analysis and heating values of available biomass fuels.
| Biomass | Wad/% | Aar/% | Var/% | FCar/% | Qnet.ar MJ/Kg |
|---|---|---|---|---|---|
| Bean stalk | 3.99 | 3.55 | 75.56 | 16.12 | 14.52 |
| Sorghum stalk | 3.39 | 5.55 | 75.48 | 16.02 | 12.89 |
| Corncob | 3.09 | 0.95 | 76.14 | 17.66 | 10.55 |
| Locust tree branch | 3.77 | 1.73 | 77.01 | 15.60 | 15.37 |
| Apple tree branch (wet) | 3.03 | 2.43 | 76.11 | 17.62 | 15.28 |
| Apple tree branch (dry) | 3.49 | 1.24 | 76.01 | 16.76 | 10.21 |
ad: air-dry base.
Table 3.
Proximate and ultimate analysis of fuel used in biomass co-firing test.
| Condition | Proximate Analysis (%) | Ultimate Analysis (%) | Qgr, d/ MJ.Kg−1 | |||||||
|---|---|---|---|---|---|---|---|---|---|---|
| Mad | Vad | FCad | Aad | Cd | Hd | Od | Nd | Sd | ||
| 100% coal | 0.81 | 17.15 | 49.5 | 32.5 | 55.3 | 2.97 | 3.84 | 1.15 | 3.4 | 22.69 |
| 5% biomass | 0.89 | 16.22 | 48.9 | 33.9 | 54.2 | 2.87 | 3.26 | 1.14 | 3.5 | 23.18 |
| 10% biomass | 1.10 | 17.92 | 48.4 | 32.5 | 54.4 | 2.95 | 4.60 | 1.14 | 3.3 | 22.32 |
| 20% biomass | 1.05 | 23.9 | 43.0 | 32.0 | 55.5 | 2.99 | 4.03 | 1.14 | 3.1 | 22.55 |
| 100% biomass | 3.94 | 67.6 | 15.8 | 12.5 | 42.3 | 4.78 | 35.1 | 0.75 | 0.5 | 16.68 |
Table 4.
Test conditions.
| Condition | Biomass Ratio (wt.%) | Primary Air Temperature (°C) | Secondary Air Temperature (°C) | Tertiary Air (On/Off) | Ammonia (On/Off) | |
|---|---|---|---|---|---|---|
| Left | Right | |||||
| 1 | 0 | 240 | 356 | 354 | On | Off |
| 2 | 0 | 240 | 356 | 354 | On | On |
| 3 | 5 | 224 | 349 | 348 | On | Off |
| 4 | 5 | 224 | 349 | 348 | On | On |
| 5 | 10 | 232 | 346 | 345 | On | Off |
| 6 | 10 | 232 | 346 | 345 | On | On |
| 7 | 20 | 224 | 342 | 345 | On | Off |
| 8 | 20 | 224 | 342 | 345 | On | On |
Table 5.
Designed parameters of primary, secondary, and tertiary air.
| Air Type | Primary Air (with Coal) | Secondary Air | Tertiary Air |
|---|---|---|---|
| Air ratio (%) | 25 | 56 | 19 |
| Air velocity (m/s) | 25 | 45 | 55 |
| Temperature (°C) | 263 | 335 | 120 |
Table 6.
Effects of biomass co-firing on boiler efficiency.
| Conditions | 1UBC in Fly Ash (%) | UBC in Bottom Slag (%) | Exhaust Temperature (°C) | Furnace Efficiency (%) |
|---|---|---|---|---|
| 100% coal | 4.71 | 11.48 | 138.4 | 90.88 |
| 5% biomass | 4.68 | 14.06 | 139.2 | 90.82 |
| 10% biomass | 5.77 | 15.96 | 135.5 | 90.09 |
| 20% biomass | 5.16 | 15.99 | 134.1 | 90.11 |
1UBC: unburned carbon content.
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Wang, X.; Rahman, Z.U.; Lv, Z.; Zhu, Y.; Ruan, R.; Deng, S.; Zhang, L.; Tan, H. Experimental Study and Design of Biomass Co-Firing in a Full-Scale Coal-Fired Furnace with Storage Pulverizing System. Agronomy 2021, 11, 810. https://doi.org/10.3390/agronomy11040810
AMA Style
Wang X, Rahman ZU, Lv Z, Zhu Y, Ruan R, Deng S, Zhang L, Tan H. Experimental Study and Design of Biomass Co-Firing in a Full-Scale Coal-Fired Furnace with Storage Pulverizing System. Agronomy. 2021; 11(4):810. https://doi.org/10.3390/agronomy11040810
Chicago/Turabian StyleWang, Xuebin, Zia Ur Rahman, Zhaomin Lv, Yiming Zhu, Renhui Ruan, Shuanghui Deng, Lan Zhang, and Houzhang Tan. 2021. "Experimental Study and Design of Biomass Co-Firing in a Full-Scale Coal-Fired Furnace with Storage Pulverizing System" Agronomy 11, no. 4: 810. https://doi.org/10.3390/agronomy11040810
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