The authors would like to acknowledge Matt Dee for supporting the experimental work, Matthew Anderson and Rod Shurtliff for instrumenting the pellet mill. This work was supported by the Department of Energy, Office of Energy Efficiency and Renewable Energy under the Department of Energy Idaho Operations Office Contract DE-AC07-05ID14517. Accordingly, the publisher, by accepting the article for publication, acknowledges that the U.S. government retains a nonexclusive, paid-up, irrevocable, worldwide license to publish or reproduce the published form of this manuscript, or allow others to do so, for U.S. government purposes.

NOTE: Corn stover bales were procured in the form of bales from agricultural farms in Iowa, USA. The procured bales were ground sequentially in two stages. In stage 1, the corn stover bales were ground using a grinder fitted with a 50.8-mm screen. In stage 2, the ground material from stage 1 was further ground by using a Bliss hammer mill fitted with a 4.8-mm screen. The material was tested for moisture content and bulk density and stored in an air tight container for further pelleting tests. Pure corn starch was procured from a local market and was measured for the moisture content and bulk density. The moisture content and bulk density of ground corn stover and corn starch binder are given Table 1.
<img alt="Table 1" src="/files/ftp_upload/54092/54092table1.jpg" /> 
Table 1. Moisture content and bulk density of ground corn stover and corn starch binder.
1. Pellet Mill
<ol>
	<li>Use a laboratory scale flat die pellet mill equipped with a 10 HP motor for carrying out the pelleting tests (Figure 1)21,28,38.</li>
</ol>
<img alt="Figure 1" src="/files/ftp_upload/54092/54092fig1.jpg" /> 
Figure 1. Schematic of a laboratory scale flat die pellet mill at Idaho National Laboratory (adapted from Tumuluru21).&#160;A flat die pellet mill was used to conduct the high moisture corn stover pelleting tests with and without binder addition. <a href="https://www-jove-com.bdigitaluss.remotexs.co/files/ftp_upload/54092/54092fig1large.jpg" target="_blank">Please click here to view a larger version of this figure.</a>
<ol start="2">
	<li>Place flexible heating tape on the surface of the hopper and screw feeder then insulate them with glass wool to prevent heat loss. Connect the heating tape to a temperature controller to preheat biomass to desired temperature in the range of 30-130 &#176;C.</li>
	<li>Equip the pellet mill with a variable frequency drive (VFD). Connect the VFD of the pellet mill to the pellet mill motor. The feeder motor controller is a direct current motor controller to vary the feeding rate to pellet mill.</li>
	<li>Connect a power meter to the pellet mill motor to record the power consumption. Manually choose a pellet die with an 8 mm diameter opening and a length to diameter (L/D) ratio of 2.6.</li>
	<li>Add a horizontal pellet cooler to the pellet mill to cool the warm pellets coming out of the pellet die. Connect the cooler to an exhaust system to circulate fresh air.</li>
</ol>
2. Feedstock Preparation
<ol>
	<li>Take 2-3 kg of corn stover ground using a 4.8 mm screen. Measure the corn stover moisture content (see step 4.1) and bulk density (see step 4.3) (see Table 2).</li>
	<li>Measure moisture content (see step 4.1) and bulk density (see step 4.3) of the pure (100%) corn starch binder procured from the local market.</li>
	<li>Add corn starch binder to the ground corn stover (see Table 2 for % binder addition)</li>
	<li>Calculate the amount of water to be added to adjust the moisture levels of ground corn stover and corn starch binder mix&#160;to 33, 36, and 39% (w.b.) using equation 1. 
	<img alt="Equation 1" src="/files/ftp_upload/54092/54092eq1.jpg" /> =<img alt="Equation 2" src="/files/ftp_upload/54092/54092eq2.jpg" /> (1) 
	NOTE: In equation 1, Ww is weight of water (g), Ws is weight of biomass sample (g), mf: percent final moisture content of the sample (w.b.), and mi: percent initial moisture content of the sample (w.b. %).</li>
	<li>Add the calculated water to the corn stover/corn starch binder mix and blend it in a laboratory scale ribbon blender.</li>
	<li>Store the moisture-adjusted corn stover/corn starch mix in a sealed container and place it in a refrigerator set at 4-5 &#176;C to allow moisture to equilibrate.</li>
</ol>
3. High Moisture Pelleting Process
<ol>
	<li>Take the corn stover/corn starch mix out of refrigerator and leave it at room temperature for about 1-2 hr to bring it to room temperature.</li>
	<li>Load the material into the feed hopper of the pellet mill. Run the pellet mill at 60 Hz (380 rpm) die speed.</li>
	<li>Feed the pellet mill uniformly by adjusting the feeding rate of the pellet mill to produce pellets in a steady state condition. Cool the pellets in the horizontal pellet cooler.</li>
	<li>Separate fines generated in the pelleting process using a 6.3 mm screen. 
	NOTE: Measure the moisture content and durability of the pellets after cooling21.</li>
	<li>Dry the cooled high-moisture pellets in a laboratory oven at 70 &#176;C for 3-4 hr to reduce the final moisture content of the pellets to less than 9% (w.b.). 
	NOTE: Measure the pellet moisture content, bulk density, and durability of the dried pellets21.</li>
	<li>Log the power data into a computer during the pelleting process. 
	NOTE: See Table 2 for pelleting test conditions and Figure 2 for pellets produced at 33, 36 and 39% moisture content and 4% corn starch binder addition.</li>
</ol>
<img alt="Table 1" src="/files/ftp_upload/54092/54092table2.jpg" /> 
Table 2. Experimental test conditions used in the present study.
<img alt="Figure 2" src="/files/ftp_upload/54092/54092fig2.jpg" /> 
Figure 2. Photograph of the corn stover pellets produced with 4% corn starch binder at different feedstock moisture contents. <a href="https://www-jove-com.bdigitaluss.remotexs.co/files/ftp_upload/54092/54092fig2large.jpg" target="_blank">Please click here to view a larger version of this figure.</a>
4. Pellet Properties and Specific Energy Consumption
NOTE: ASABE standards42 were used for measuring the moisture content, density, durability and percent fines of raw and pelleted materials.
<ol>
	<li>Place about 25-50 g of the ground and pelleted corn stover samples in a laboratory oven set at 105 &#176;C for 24 hr. Weigh the sample before and after drying. Calculate the moisture content using equation 2. Conduct the experiments in triplicate. 
	<img alt="Equation 3" src="/files/ftp_upload/54092/54092eq3.jpg" /> (2)</li>
	<li>Take a single pellet and smooth both the ends with Grit Utility Cloth. Measure the pellet diameter using Vernier calipers. Calculate the expansion ratio of the pellet using equation 328. Measure the diameter of the ten pellets. 
	Expansion ratio = <img alt="Equation 4" src="/files/ftp_upload/54092/54092eq4.jpg" />&#160; (3) 
	NOTE: In equation 3, D is the diameter of the pellet extruded (mm) and d is the diameter of the die (mm).</li>
	<li>Use a plexi glass cylinder with a height of 155 mm and a diameter of 120 mm. Pour the pellets into the cylinder until it overflows and level the top surface with a straight edge. Weigh the cylinder with the material. Divide the weight of the cylinder by&#160;the volume of the cylinder to calculate bulk density. Repeat the experiment three times.</li>
	<li>Hand sieve the pelleted material using a 6.3 mm screen. Weigh the material that has passed through the screen. Calculate the percent fines using equation 4. 
	Percent fines = <img alt="Equation 5" src="/files/ftp_upload/54092/54092eq5.jpg" />&#215; 100&#160; (4)</li>
	<li>Place approximately 500 g of the pellets without fines into each compartment of the pellet durability tester. Tumble the pellets at 50 rev/min for 10 min. Sieve the tumbled material using a 6.3 mm screen. Use equation 5 to calculate the percent durability of the pellets. 
	Durability = <img alt="Equation 6" src="/files/ftp_upload/54092/54092eq6.jpg" /> &#215; 100 (5) 
	Note: Green durability is the durability of the pellets measured after cooling, and cured durability is the durability measured after drying the pellets at 70 &#176;C for 3 hr.</li>
	<li>Log the pellet mill power consumption using data logging software. Record the no load power (kW) data of the pellet mill by running the pellet mill empty at 60-Hz die speed. Use equation 6 to calculate the specific energy consumption (SEC). 
	<img alt="Equation 7" src="/files/ftp_upload/54092/54092eq7.jpg" />&#160; (6)</li>
</ol>

No competing financial interests exist. This information was prepared as an account of work sponsored by an agency of the U.S. government. Neither the U.S. government nor any agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. References herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise, do not necessarily constitute or imply its endorsement, recommendation, or favouring by the U.S. government or any agency thereof. The views and opinions of the authors expressed herein do not necessarily state or reflect those of the U.S. government or any agency thereof.

The critical steps in the high moisture pelleting method to produce pellets with the desired durability at lower specific energy consumption are: 1) drying the high moisture corn stover to the desired moisture levels (33-39%, w.b.), 2) percent binder addition and 3) feeding high moisture biomass uniformly into the pellet mill. Feedstock moisture and percent binder are process variables that influenced the pellet properties (density and durability of the pellets before cooling and after drying) and specific energy consumption of the pelleting process. It is recommended to test the moisture content of the feedstock before it is used for pelleting studies. Feeding of high moisture corn stover at 33, 36 and 39% (w.b.) uniformly to the pellet mill has an impact on quality and energy consumption. Modifying the pellet mill feeder with a variable frequency drive was essential to feed the biomass uniformly to the pellet mill.
Results from the present study indicated that adding binder to the high moisture corn stover did reduce the bulk density of the pellets marginally, but improved the durability significantly. Adding a starch based binder increased the moisture content in the pellets after compression and extrusion, but the increase was found not to be statistically significant in almost all the cases studied. The loss of moisture during pelleting was about 3 to 4% at the addition of 4% binder, whereas it was higher (7-8%, w.b.) without the binder. The addition of a binder to the corn stover might have 1) reduced the residence time of the material in the die and 2) reduced the frictional resistances in the die, thereby reducing the die temperature, which might have resulted in less moisture loss during compression and extrusion in the pellet die.
There was an increase in the pellet diameter after it was extruded from the pellet die and dried (Figure 4). This increase was greater at higher feedstock moisture content and with starch binder addition. The bulk density of the pellets was in the range of 510-530 kg/m3 at 33% (w.b.) feedstock moisture content with and without a binder. Previous research has indicated that higher feedstock moisture content of about 38% (w.b.) results in lower bulk density, mainly due to expansion of the pellets as they exit through the die21,28. It is a common phenomenon that when high-moisture biomass material is extruded through the die under pressure it results in moisture flash-off12,21. The moisture flash-off gives way to the expansion of the pellet, both in the axial and diametrical direction. In general, the diametrical expansion is more prominent compared to axial expansion. Another reason for the expansion behavior of biomass after compression and extrusion through the pellet die could be that biomass fibers relax in the presence of moisture content. Ndiema et al.45 and Mani et al.18 indicated that release of the applied pressure in a die results in relaxation of the compressed biomass. The relaxation characteristics are dependent on many factors like particle size, feedstock moisture content and applied pressure. Also, in this study we have observed that the bulk density increases after drying, which could be due to fewer&#160;inter-particle liquid bridges that might have kept the particles closer and produced a less-open structure. Oginni45 observed that the bulk density of ground Loblolly pine decreased with increased moisture content.
Durability of the pellets was measured to understand the strength of the pellets. Generally, pellets are subject to shear and impact resistances during storage, transportation, and the handling process4,46. Kaliyan and Morey47 suggested that durability of pellets produced immediately after production (green strength) is different than durability of the pellets that are stored for a few days after production (cured strength). Pellets with lower durability values break and increase the risk of storage issues, such as off-gassing and spontaneous combustion that could cause revenue loss for pellet manufacturers. According to the European Committee for Standardization (CEN) and the United States Pellet Fuels Institute (PFI) the recommended values of the durability are &#62;96.5% for high quality or premium grade pellets31. In this study, the durability values increased to approximately 94-95% when pelleted with a starch binder at 39% moisture content compared to pellets made with no binder that had durability values in the range of 83-85% after drying. The pellets produced at 33% (w.b.) feedstock moisture content had durability values &#62;96.5% and meet the international standards.
Moisture has different functions during biomass pelleting, including: 1) solid bridge formation between the biomass particles due van der Waals forces, 2) activating natural binders like protein, starch and lignin present in the biomass, and 3) promoting starch and protein based reactions like gelatinization and denaturation that have a strong impact on the textural properties, such as hardness4-12. In the case of lignocellulosic biomass, the main binding agent is lignin (woody biomass: 27-33%, herbaceous biomass: 12-16%)4. Lignin content in corn stover was determined to average around 16% based on a review of composition data, including literature sources and feedstock databases48. Lignin molecules, which have higher mobility at higher moisture content, act as an adhesive and result in stronger binding; however, at very high levels the moisture will act more like a lubricant resulting in less binding. In the present study, at a very high moisture content of about 39% (w.b.) moisture might have acted more like a lubricant and resulted in low durability and more fines generation in the pellet production process. Higher durability values were observed by the addition of a binder at a higher feedstock moisture content of 36 and 39% (w.b.), which could be caused by gelatinization of starch in the presence of die temperature and feedstock moisture content. These gelatinization reactions can lead to the formation of cross linking of starch with the other biomass components.
The percent fines generated during the pelleting process is a good indicator for how well biomass will form pellets. Generation of fine particles during the pelleting process results in product and revenue loss to the pellet producer. Excessive fine generation during pelleting processes can also have an impact on quality attributes such as&#160;density and durability. The fines generation during the pellet production process is influenced by biomass composition (i.e., starch, protein, lignin, and waxes), pellet mill process variables i.e.,&#160;length to diameter ratio (L/D ratio), die rotational speed, steam condition, preheating), and feedstock variables (i.e., feedstock moisture content, particle size and feed rate) 4. The present results indicate that the addition of binder not only reduces the percent of fine particles generated, but also helps to improve the physical properties while reducing the specific energy consumption. Lower percent fines generated indicate that the biomass has a greater pelletability.
Tumuluru et al.4 in their review on densification systems suitable to make biomass into a commodity type product indicated that adding binder helps to reduce the extrusion energy, which results in reducing the specific energy consumption. Typically, length to diameter (L/D) ratio controls the residence time of the material in the die and helps the binding of the biomass. Also, L/D ratio controls the extrusion energy and the specific energy consumption. Higher L/D ratio increases the residence time, which improves the physical properties of the pellets, but increases the energy necessary for extrusion. Adding a binder to biomass can help bind the biomass at lower L/D ratio and reduce the extrusion energy. In this study, a constant length to diameter (L/D) ratio of (2.6) was selected. Future research is aimed at understanding the effect of L/D ratio of the pellet die and its interaction with feedstock moisture content on pellet quality attributes.
The experimental data on biomass preprocessing (grinding, drying and pelleting) obtained from the Biomass National User Facility (https://www.inl.gov/bfnuf/) located at INL and associated techno-economic analysis indicated that drying biomass from 30-10% (w.b.) consumes a large amount of energy (unpublished data). The high moisture pelleting process developed at INL can help reduce the pellet production cost compared to a conventional pellet production method24. The present study indicated that adding a starch-based binder to a high moisture pelleting process improved the durability of the pellets to &#62;92% after cooling at the feedstock moisture contents of 36 and 39% (w.b.), and it also reduced the specific energy consumption of the pelleting process by about 20-40%. Greater durability values of the pellets made at higher feedstock moisture is important as they can be handled efficiently by conveyors. Typically low durability pellets crumble to fines during handling and storage, which results in revenue loss for the pellet producers. In addition, fines generated in the process can result in safety hazards like spontaneous combustion and off-gassing28,41. The specific energy reduction by approximately 20-40% using a binder outweighs the cost of the binder. Also, based on this study we can conclude that some of the by-products&#160;from food processing industries could be used for biomass pelleting for bioenergy applications. Currently, the high-moisture pelleting process was demonstrated using a laboratory scale flat die pellet mill. The protocol described here for the laboratory-scale pellet mill will be the basis for developing scale-up models and for testing the process in pilot-scale and commercial-scale pellet mills.

Biomass is one of the major energy resources in the world and is considered carbon neutral1. Bulk density of baled and ground agricultural biomass and chipped woody biomass is low. Low bulk densities of baled biomass (130-160 kg/m3), ground biomass (60-80 kg/m3) and chipped woody biomass (200-250 kg/m3) create storage, transportation, and handling issues2,3. Densifying or compressing the ground biomass by using pressure and temperature increases the bulk density by about 5 to 7 times, and helps to overcome transportation and storage limitations4. Pellet mills, briquette presses, and screw extruders are densification systems typically used for biomass4. Breakeven transportation distance analysis on baled and pelleted biomass feedstock indicated that pellets can be transported 1.6&#160;times farther than bales using a truck for the same cost5. The transportation efficiencies of pellets increase with other modes&#160;of transportation such as&#160;rail, since it is&#160;volume-limited compared to trucks that are limited by weight. Currently, in Europe the pellets produced from woody biomass are extensively used for bio-power generation. Canada and the United States are the major producers and suppliers of wood pellets to Europe6. Pellets produced from both woody and herbaceous biomass can be used for both thermochemical (cofiring, gasification, and pyrolysis) and biochemical conversion (ethanol) applications7-9.
The qualities of pellets (density and durability) and specific energy consumption of the pelleting process are dependent on the pellet mill process variables, such as die diameter, die speed and length to diameter ratio of the die and feedstock variables, such as feedstock moisture content and composition4. Both&#160;pellet mill process variables and feedstock variables influence the quality of the pellets and the specific energy used in the process. The die dimensions (i.e., length to diameter ratio) will influence the compression and extrusion pressure, and the die rotational speed controls the residence time of the material within the die. Moisture content is a feedstock variable that plays an important role by interacting with the biomass composition components (i.e., protein, starch, and lignin) due to high temperature and pressure encountered in the die. The presence of moisture increases the van der Waals forces, thereby increasing the attraction between the biomass particles10. In general, higher moisture in the biomass impacts the bulk density of the compressed product due to diametrical and lateral expansion as it exits the pellet mill or briquette press die10. Biomass composition, such as starch, protein, lignin, and other water-soluble carbohydrates, influences the binding behavior when subjected to pressure and temperature in densification equipment11. Some of the common composition reactions that are influenced by feedstock moisture, die temperature, and pressure are starch gelatinization, protein denaturation, and lignin glass transition. Generally, at temperatures of 100 &#176;C or greater and a feedstock moisture content of greater than 30%, starch in food and animal feed gets gelatinized and influences textural properties like hardness12. Typically, the starch reactions are gelatinization, pasting, and retrogradation. Among these reactions, gelatinization has the greatest influence on pellet properties13. Starch is often included in food and non-food applications as a binder. For example, in the pharmaceutical tablet formulation starch is used as filler4,14. Protein in the biomass undergoes denaturation and forms complex bonds due to the high temperature and pressure experienced in the densification process11. In general, higher amounts of protein in biomass will result in a more durable pellet15,16. For example, alfalfa, which has a higher amount of protein, results in durable pellets at higher feedstock moisture content. The fat in the biomass reduces the friction forces and the extrusion energy during pelleting or briquetting11,17. In lignocellulosic biomass, the presence of lignin within plant material helps to form pellets without adding any binders18. Woody biomass has higher lignin content (29-33%) when compared to a herbaceous biomass, which typically consists of 12-16% lignin4,19. At lower feedstock moisture contents of about 10-12% (w.b.), glass transition temperature of the lignin is greater than 140 &#176;C20; whereas, increasing the moisture content reduces the glass transition temperature21. According to Lehtikangas22, the glass transition temperature of lignin at 8-15% (w.b.) moisture content is about 100-135 &#176;C, but increasing the moisture content to &#62;25% (w.b.) reduces the glass transition temperature to &#60;90 &#176;C.
Herbaceous biomass is available at higher moisture content depending on the harvesting method and harvesting time. In the case of single pass harvesting method the harvested material will have a moisture content &#62;30% (w.b.)23. Biomass is typically dried to about 10% (w.b.) moisture content to make it aerobically stable and to prevent dry matter loss during storage. Lamers et al.24 indicated that to preprocess biomass at 30% moisture content the total cost for both grinding (stages 1 &#38; 2) and drying is about $43.60/dry ton, and about $15.00/dry ton is just for drying the biomass. Drying biomass takes about 65% of the total preprocessing energy, and pelleting takes about 8-9%24. Yancey et al.25 has corroborated the fact that drying is the major energy consumer in biomass preprocessing. The experimental data and techno-economic analysis indicated that efficient moisture management is critical for reducing the biomass preprocessing costs. One way to decrease the drying cost and manage the feedstock moisture more efficiently is to use a high-moisture pelleting process coupled with a low temperature drying method. In the high-moisture pelleting process developed at Idaho National Laboratory, the biomass is pelleted at moisture contents greater than 28% (w.b.); the partially dried pellets produced, which are still high in moisture, can be dried in energy efficient driers, such as grain or belt dryers21. One major advantage of high-moisture pelleting is that it helps reduce the drying cost, which in turn results in reduced total pellet production cost. Techno-economic analysis indicated that energy and production costs are reduced by about 40-50% using the high-moisture pelleting process compared to a conventional pelleting method24,26. The major reason for reduced pellet production cost is due to replacing a rotary dryer that operates at high temperatures of 160 to 180 &#176;C with a grain dryer that operates at lower temperatures of about 80 &#176;C or less21. The other advantages of replacing a rotary dryer with a belt or grain dryer are: 1) greater efficiency, 2) reduced fire hazard, 3) does not need high quality heat, 4) reduced volatile organic compound (VOC) emissions, 5) reduced particulate emissions, and 6) does not agglomerate high clay or sticky biomass27. The energy-intensive steam conditioning step in conventional pelleting, typically used to add moisture and activate some of the biomass components, is replaced with a short preheating step. This step helps reduce the feedstock moisture content as well as activate biomass components like lignin. The frictional heat developed in the pellet die also helps reduce the feedstock moisture content by about 5-8% (w.b.)21,28. In the high-moisture pelleting process, the pellet mill not only compresses the biomass, but also helps to reduce the moisture content during compression and extrusion. Many researchers have done experiments on pelleting of raw and chemically pretreated biomass at a wide range of moisture contents (7-45%, w.b.) using single, laboratory, pilot scale ring die and commercial continuous pelleting systems10,25,29-40,(Pace, D. 2015. Pelleting of municipal solid waste and ammonia fiber explosion (AFEX) pretreated corn stover in a pilot scale ring die pellet mill. Biofuels Department, Chief Engineer, Biomass National User Facility, Idaho National Laboratory (Unpublished data)). These researchers adjusted feedstock moisture content of the biomass to different desired levels to understand the effect of moisture content on quality attributes of the pellets.
Pellet quality attributes, bulk density and durability, are normative specifications according to the USA based Pellet Fuel Institute (PFI). However, according to the European Committee for Standardization (CEN) durability is a normative and bulk density is an informative specification41. Pellets with durability values &#62;96.5% and bulk density &#62;640 kg/m3 are designated as super premium pellets based on PFI standards, whereas pellets with durability values &#62;97.5% are designated as pellets with the highest grade. Both the CEN and PFI standards recommend pellets with different diameters. For example, PFI recommends a diameter in the range of 6.35-7.25 mm, whereas CEN recommends a diameter ranging from 6-25 mm and a pellet length less than or equal to 4 times the diameter41. Smaller diameter pellets (6 mm) are preferred for transporting longer distances considering they have higher packing densities28. For conventional pelleting processes, it is recommended to pellet biomass at low moisture contents to meet these density specifications desirable for transporting the pellets long distances41. Both CEN and PFI have additional pellet grades41. Tumuluru28 and Tumuluru and Conner40 indicated that high moisture pelleting processes developed at Idaho National Laboratory help to produce corn stover and wood pellets with different quality attributes (bulk density and durability) and specific energy consumption making them suitable for different transportation and logistics scenarios.
Most of the pelleting studies on biomass were done using a single pelleting system. Pelleting data on biomass using a continuous system at laboratory scale is limited. Studies on continuous pelleting systems will be useful to understand the effect of the pelleting process variables like die rotational speed, length to diameter ratio and die diameter on the quality attributes and specific energy consumption. The pelleting data on the continuous systems can be further used to scale up the process to pilot and commercial scale systems. In general, a flat die pellet mill is used for conducting pelleting studies on woody and herbaceous biomass in a laboratory4. The working principle of the laboratory scale flat die, pilot, and commercial scale ring die pellet mills are similar. All of these pellet mills have a perforated hard steel die with two or three&#160;rollers. By rotating the die, the rollers exert force on the feedstock and force it through the perforations of the die to form densified pellets4.
Our earlier studies on high-moisture pelleting of corn stover at feedstock moisture content of 28-38% (w.b.) without any binder addition resulted in lower durability values at higher feedstock moisture content21,28. Improving the durability of high moisture pellets after cooling and drying is important as it helps to prevent the disintegration of the pellets (loss of pellet quality) during handling, storage and transportation. The disintegration of pellets typically results in fines generation and loss of revenue for the pellet producers. Binders are typically used in the pelleting process to improve pellet quality, especially durability, and to reduce the specific energy consumption. Commonly used natural binders in the pelleting process are proteins and starch4,28. Starch undergoes gelatinization, whereas protein undergoes denaturation in the presence of heat, moisture, and pressure. Both of these reactions result in better binding and more durable pellets at lower energy consumption. The overall objective of this study was to develop and demonstrate a high-moisture pelleting process using corn stover with the addition of a binder to produce good quality pellets in terms of green durability (after cooling) and cured durability (after drying) at a lower specific energy consumption. The specific objectives for the study were to 1) conduct high-moisture pelleting of corn stover at different feedstock moisture contents (33, 36, and 39%, w.b.) and starch binder contents (0, 2, and 4%), 2) evaluate the physical properties (pellet moisture content, pellet diameter, expansion ratio, bulk density and durability (green and cured durability), and 3) evaluate specific energy consumption of the pelleting process.

<table><tbody><tr><td>Flat die pellet mill</td><td>Colorado Mill Equipment, Canon City, CO, USA</td><td>ECO-10 pellet mill</td><td></td></tr><tr><td>Heating tapes</td><td>BriskHeat, Columbus, OH, USA</td><td>Silicon Rubber Heater, Etched foil elements</td><td></td></tr><tr><td>Thermocouples</td><td>Watlow, Burnaby, BC, Canada</td><td>J-type</td><td></td></tr><tr><td>Variable frequency drive</td><td>Schneider Electric, Palatine, IL, USA</td><td>Altivar 71</td><td></td></tr><tr><td>Pellet cooler</td><td>Colorado Mill Equipment, Canon City, CO, USA</td><td>CME ECO-HC6&amp;nbsp;</td><td></td></tr><tr><td>Data logging software</td><td>National Instruments Corporation, Austin, TX, USA</td><td>Labview software</td><td></td></tr><tr><td>Durability tester</td><td>Seedburo Equipment Co., Des Plaines, IL, USA</td><td>Pellet durability tester</td><td></td></tr><tr><td>Hammer mill&amp;nbsp;</td><td>Bliss Industries&amp;nbsp;</td><td>CME ECO-HC6&amp;nbsp;</td><td></td></tr><tr><td>Grinder</td><td>Vermeer</td><td>HG200</td><td></td></tr><tr><td>Horizontal mixer</td><td>Colorado Mill Equipment, Canon City, CO, USA</td><td>ECO-RB 500</td><td></td></tr><tr><td>Blue grit utilty cloth</td><td>3M</td><td>Part No.05107-150J grade</td><td></td></tr><tr><td>Insulation materail</td><td>McMaster Carr</td><td>Flexible fiberglass insulation</td><td></td></tr><tr><td>Feeder controller</td><td>KB Electornics, INC</td><td>KBIC-DC-MTR direct current motor controller</td><td></td></tr><tr><td>Dust exhaust system</td><td>Delta</td><td>Model No: 50-763, Serial No: 2010 11OI1415</td><td></td></tr><tr><td>Vernier calipers</td><td>VWR&amp;reg; Digital Calipers</td><td>Part Number:&amp;nbsp;12777-830</td><td></td></tr><tr><td>Binder</td><td>ACH Food Companies Inc., Memphis, TN, USA</td><td>ARGO 100% pure corn starch</td><td></td></tr><tr><td>Corn stover</td><td>Harvested in Iowa and procurred in bale form</td><td></td><td></td></tr></tbody></table>

method to produce durable pellets at lower energy consumption using high moisture corn stover and a corn starch binder in a flat die pellet mill

A major challenge in the production of pellets is the high cost associated with drying biomass from 30 to 10% (w.b.) moisture content. At Idaho National Laboratory, a high-moisture pelleting process was developed to reduce the drying cost. In this process the biomass pellets are produced at higher feedstock moisture contents than conventional methods, and the high moisture pellets produced are further dried in energy efficient dryers. This process helps to reduce the feedstock moisture content by about 5-10% during pelleting, which is mainly due to frictional heat developed in the die. The objective of this research was to explore how binder addition influences the pellet quality and energy consumption of the high-moisture pelleting process in a flat die pellet mill. In the present study, raw corn stover was pelleted at moistures of 33, 36, and 39% (w.b.) by addition of 0, 2, and 4% pure corn starch. The partially dried pellets produced were further dried in a laboratory oven at 70 &#176;C for 3-4 hr to lower the pellet moisture to less than 9% (w.b.). The high moisture and dried pellets were evaluated for their physical properties, such as bulk density and durability. The results indicated that increasing the binder percentage to 4% improved pellet durability and reduced the specific energy consumption by 20-40% compared to pellets with no binder. At higher binder addition (4%), the reduction in feedstock moisture during pelleting was &#60;4%, whereas the reduction was about 7-8% without the binder. With 4% binder and 33% (w.b.) feedstock moisture content, the bulk density and durability values observed of the dried pellets were &#62;510 kg/m3 and &#62;98%, respectively, and the percent fine particles generated was&#160;reduced to &#60;3%.

Pellet Moisture Content
The moisture content of the biomass was reduced by about 5-8% (w.b.) after pelleting. This reduction is mainly attributed to frictional heat developed in the die, and preheating temperature and cooling of the high moisture pellets. Also, binders had an impact on the amount of moisture lost. At 0% binder, the loss of moisture was about 7-8%, which agrees with our earlier studies21,28; whereas, at 4% binder, the loss of moisture in the feedstock during pelleting was about 3-5% (Figure 3). The binder added to the biomass might have acted as a lubricating agent. This may have reduced the frictional resistances and reduced the residence time of the material in the die channel causing the decrease in moisture loss. In previous studies die temperature measured immediately after pelleting using an infrared thermometer (Fluke, Model 561, Fluke Corporation, Everett, WA, USA) reached to about 100-110 &#176;C21. Increasing the binder percentage reduced the moisture loss as the moisture might have been tightly bound to the starch granules. The high moisture pellets that were further dried in a laboratory oven at 70 &#176;C for 3-4 hr had moisture contents &#60;9% (w.b.), and these pellets were used to measure other physical properties like pellet diameter, expansion ratio, bulk density and durability. Statistical analysis of the pellet moisture content data indicated that there was an interactive effect of feedstock moisture content and binder addition on the pellet moisture content (Table 3). For pellets with no binder and 2% binder, an increase in feedstock moisture content caused an increase in pellet moisture content (Tukey&#39;s p&#60;0.05), but this trend was not statistically significant at 4% binder (Tukey&#39;s p&#8805;0.05; Figure 3).
<img alt="Figure 3" src="/files/ftp_upload/54092/54092fig3.jpg" /> 
Figure 3. Effect of feedstock moisture content (FMC) and starch binder on pellet moisture content after cooling (mean&#177;1SD; n=3). Pelleting tests conducted without binder resulted in higher feedstock moisture content loss compared to tests conducted with binder. Different letters indicate significant differences using post hoc Tukey HSD tests (p&#60;0.05). <a href="https://www-jove-com.bdigitaluss.remotexs.co/files/ftp_upload/54092/54092fig3large.jpg" target="_blank">Please click here to view a larger version of this figure.</a>
Pellet Diameter
The diameter of the pellets at 33% moisture content with and without binder addition was in the range of 8.4-8.7 mm after cooling (data not shown). Increasing the feedstock moisture content to 36 and 39% (w.b.) with added binder increased the pellet diameter to a maximum value&#160;of 9.3 mm (data not shown). These pellets were further dried in a laboratory oven at 70 &#176;C for about 3-4 hr. Drying resulted in a decrease in pellet diameter of&#160;about 0.3-0.4 mm. The major reason for a decrease in diameter after drying was due to contraction of the pellets. There was a statistically significant effect of the interaction between feedstock moisture content and binder addition on pellet diameter after drying (Table 3). At 33% feedstock moisture content the pellet diameter after drying was in the range of 8.3 to 8.5 mm, whereas increasing the feedstock moisture content to 36% or 39% increased the pellet diameter to about 8.7 mm (Figure 4). This increase was only statistically significant between 33% and 39% when no binder was used (Tukey&#39;s p&#60;0.05), likely because of the high deviations in the measurements.
<img alt="Figure 4" src="/files/ftp_upload/54092/54092fig4.jpg" /> 
Figure 4. Effect of feedstock moisture content (FMC) and corn starch binder on pellet diameter after drying (mean&#177;1SD; n=10). Pellet diameter increased with an increase in feedstock moisture content and starch addition. Different letters indicate significant differences using post hoc Tukey HSD tests (p&#60;0.05). <a href="https://www-jove-com.bdigitaluss.remotexs.co/files/ftp_upload/54092/54092fig4large.jpg" target="_blank">Please click here to view a larger version of this figure.</a>
Expansion Ratio
Expansion ratio is calculated using the pellet diameter (equation 3). The expansion ratio values were higher for the pellets after cooling compared to after drying (data not shown). At 33% moisture content without and with binder addition, the expansion ratio values after cooling were in the range of 1.16-1.20. Further increasing the moisture content to 36 and 39% without binder addition increased the expansion ratio values to 1.35. The dried pellets had lower expansion ratios, which was mainly due to contraction of the pellets both diametrically and laterally. At 33% feedstock moisture content the expansion ratio values with and without binder addition were in the range of 1.11-1.07 (Figure 5). Increasing the feedstock moisture content to 36 and 39% further increased the expansion ratio values to 1.10-1.18 (Figure 5); however, this was only statistically significant for 33% compared to 39% moisture content with no binder addition (Tukey&#39;s p&#60;0.05; Table 3). In the case of pellet diameter and expansion ratio, adding a starch based binder increased these values at all of the feedstock moisture contents, but these differences were not statistically significant (Tukey&#39;s p&#8805;0.05). The expansion ratio results after drying corroborate the findings of earlier studies, where increasing feedstock moisture increased the expansion ratio and further decreased the bulk density values28.
<img alt="Figure 5" src="/files/ftp_upload/54092/54092fig5.jpg" /> 
Figure 5. Effect of feedstock moisture content (FMC) and starch based binder on the expansion ratio of pellets after drying (n=10). Expansion ratio of pellets increased with an increase in feedstock moisture content&#160;without and with binder addition. Different letters indicate significant differences using post hoc Tukey HSD tests (p&#60;0.05). <a href="https://www-jove-com.bdigitaluss.remotexs.co/files/ftp_upload/54092/54092fig5large.jpg" target="_blank">Please click here to view a larger version of this figure.</a>
Bulk Density
The bulk density of the pellets made with a feedstock moisture content of 33% with and without binder and measured after cooling was in the range of 464-514 kg/m3 (data not shown). At 36 and 39% feedstock moisture content without binder the bulk density values were in the range of 437-442 kg/m3. Adding binder at these feedstock moisture contents reduced bulk density to &#60;400 kg/m3. Drying the high-moisture pellets in a laboratory oven at 70 &#176;C for about 3 hours reduced the moisture contents of the pellets to less than 9% (w.b.). There was a slight increase in the bulk density values by about 50 kg/m3 after drying. The&#160;increase in bulk density after drying could be due to fewer&#160;inter-particle liquid bridges, which might have kept the particles closer with less-open structure. Oginni44 observed that the bulk density of ground Loblolly pine decreased with an increase in moisture content. For pellets made with a feedstock moisture content of 33% with and without the binder addition, the bulk density of the pellets was in the range of 520-530 kg/m3 (Figure 6). At higher feedstock moisture contents of 36 and 39% (w.b.), the bulk density of the dried pellets significantly decreased to &#60;434 kg/m3 and &#60;437 kg/m3, respectively. There was a statistically significant effect of the interaction between feedstock moisture content and binder addition on bulk density (Table 3). In general, bulk density decreased with an increase in starting feedstock moisture content. In addition, there is some indication that bulk density decreased with an increase in starch content (Figure 6).
<img alt="Figure 6" src="/files/ftp_upload/54092/54092fig6.jpg" /> 
Figure 6. Effect of feedstock moisture content (FMC) and starch binder on the bulk density of pellets after drying (mean&#177;1SD; n=3). Lower feedstock moisture content of 33% (w.b.) and no binder resulted in the highest bulk density. Adding 2 and 4% binder at different feedstock moisture contents resulted in lower bulk density values. Different letters indicate significant differences using post hoc Tukey HSD tests (p&#60;0.05). <a href="https://www-jove-com.bdigitaluss.remotexs.co/files/ftp_upload/54092/54092fig6large.jpg" target="_blank">Please click here to view a larger version of this figure.</a>
Durability (%)
After Cooling 
Green Durability
Figure 7 shows the durability of pellets after cooling (green strength) and after drying in an oven at 70 &#176;C for 3-4 hours (cured strength). Higher durability values of high moisture pellets are desirable as it will result in less breakage during handling and storage due to shear and impact resistances. For the ANOVA, the interaction was significant between feedstock moisture content, binder percent, and drying (Table 3). The durability values of the pellets after cooling increased with an increase in binder content (Table 3; Tukey&#39;s p&#60;0.05). At 33% (w.b.) feedstock moisture content, the durability values without binder were about 87.2%; whereas, with the addition of a 2 and 4% starch binder, the durability values increased to 93.2 and 96.1% (Figure 7). The trend was similar for the other feedstock moisture contents of 36 and 39% (w.b.). Without binder the durability values were about 80%; however, adding binder to the biomass increased the durability values. The durability increased to about 90% when pellets were made with a feedstock moisture content of 36% and 4% starch binder. At even higher feedstock moisture content of 39% (w.b.) the trend was similar, but the overall durability values decreased compared to the other feedstock moisture contents.
<img alt="Figure 7" src="/files/ftp_upload/54092/54092fig7.jpg" /> 
Figure 7. Effect of feedstock moisture content (FMC) and starch binder on durability after cooling and after drying (mean&#177;1SD; n=3). Durability values of high moisture corn stover pellets produced at 33, 36 and 39% (w.b.) feedstock moisture content increased with binder addition both after cooling and after drying. Different letters indicate significant differences using post hoc Tukey HSD tests (p&#60;0.05). <a href="https://www-jove-com.bdigitaluss.remotexs.co/files/ftp_upload/54092/54092fig7large.jpg" target="_blank">Please click here to view a larger version of this figure.</a>
After Drying 
Cured Durability
Drying of the high-moisture pellets in a laboratory oven at 70 &#176;C for 3-4 hours resulted in curing of the pellets, thereby increasing the durability of the pellets. The durability values of the pellets made at 33, 36 and 39% (w.b.) feedstock moisture content increased to &#62;92% (Figure 7). The durability values at 33% feedstock moisture content increased to about 98% after drying (Figure 7). These results match closely with earlier work21,28. The durability values of the pellets made using a binder increased after drying (Tukey&#39;s p&#60;0.05). At 33% feedstock moisture content and 4% binder, the final durability values observed were about 98%. The trend was similar at 36 and 39% feedstock moisture content, where the binder had a positive impact on the durability values (Tukey&#39;s p&#60;0.05). At 39% feedstock moisture content with a binder addition of 2 and 4%, the durability values increased to about 94-95%.
Percent Fines
In the present study, the percent fines generated during pelleting were higher at 36 and 39% (w.b.) compared to 33% (w.b.) feedstock moisture content. Adding binders resulted in lowering the percent fines generated at all feedstock moisture contents when compared to tests with no binder addition (Figure 8). Pelleting tests conducted with no binder showed the highest percent fines of about 11% at 39% (w.b.) feedstock moisture content. Adding 2 and 4% binder to the corn stover, decreased the percent fines generated during pelleting for 33% and 36% (w.b.) compared to pellets with no binder added. The lowest percent fines observed in this study were at 4% binder addition and 33% (w.b.) feedstock moisture content (approximately 3%).
<img alt="Figure 8" src="/files/ftp_upload/54092/54092fig8.jpg" /> 
Figure 8. Effect of feedstock moisture content and starch binder on the percent fines produced from the pelleted material. At feedstock moisture contents of 33, 36 and 39 % (w.b.) addition of binder reduced the percent fines in the pelleted material. <a href="https://www-jove-com.bdigitaluss.remotexs.co/files/ftp_upload/54092/54092fig8large.jpg" target="_blank">Please click here to view a larger version of this figure.</a>
Specific Energy Consumption
The specific energy consumption was influenced by binder addition (Figure 9). With no binder, the specific energy at 33, 36, and 39% feedstock moisture content was between 118-126 kWhr/ton. Adding a 2% binder reduced the specific energy consumption to about 75-94 kWhr/ton. Further increasing the binder percentage to 4% further reduced the specific energy consumption to about 68-75 kWhr/ton for all feedstock moisture contents that were tested. Adding the binder at 2 and 4% reduced the specific energy consumption by about 20-40%.
<img alt="Figure 9" src="/files/ftp_upload/54092/54092fig9.jpg" /> 
Figure 9. Effect of feedstock moisture content and starch binder on the specific energy consumption of the high moisture pelleting process. Specific energy consumption of the high moisture corn stover pelleting process was reduced by about 20-40% with addition of 2 and 4% starch based binder. <a href="https://www-jove-com.bdigitaluss.remotexs.co/files/ftp_upload/54092/54092fig9large.jpg" target="_blank">Please click here to view a larger version of this figure.</a>
Statistical Analysis
Statistical analysis was completed in JMP 1043. A two-way ANOVA was used to determine the effects of feedstock moisture content (33, 36, 39%) and corn starch binder (0, 2, 4%) on pellet moisture content (n=3), pellet diameter (n=10), expansion ratio (n=10), and bulk density (n=3). A three-way ANOVA was used to determine the effects of moisture content (33, 36, 39%), corn starch binder (0, 2, 4%), and drying (before drying, after drying) on durability (n=3). Residuals met the ANOVA assumptions for normality and homogeneity of variance. To meet these assumptions, pellet moisture content was transformed by raising the data to the 4th power. If the factors tested in the ANOVA were significant at p&#60;0.05, Tukey HSD tests were used for post hoc pairwise comparisons.
<img alt="Table 3" src="/files/ftp_upload/54092/54092table3.jpg" /> 
Table 3. Statistical significance of the process variables based on analysis of variance (ANOVA).

Watch this Scientific Journal Video about Method to Produce Durable Pellets at Lower Energy Consumption Using High Moisture Corn Stover and a Corn Starch Binder in a Flat Die Pellet Mill at JoVE.com

Method to Produce Durable Pellets at Lower Energy Consumption Using High Moisture Corn Stover and a Corn Starch Binder in a Flat Die Pellet Mill

In this study, a protocol was developed to produce good quality pellets using a flat die pellet mill at reduced specific energy consumption testing high-moisture corn stover and a starch based binder. The results indicated that adding a corn starch binder improved the pellet durability, reduced percent fines and decreased specific energy consumption.

A major challenge in the production of pellets is the high cost associated with drying biomass from 30 to 10% (w.b.) moisture content. At Idaho National ...

method-to-produce-durable-pellets-at-lower-energy-consumption-using

Universidad San Sebastian

Research

JoVE Journal

Environment

20.9K Views.  Idaho National Laboratory. In this study, a protocol was developed to produce good quality pellets using a flat die pellet mill at reduced specific energy consumption testing high-moisture corn stover and a starch based binder. The results indicated that adding a corn starch binder improved the pellet durability, reduced percent fines and decreased specific energy consumption.

Video: Method to Produce Durable Pellets at Lower Energy Consumption Using High Moisture Corn Stover and a Corn Starch Binder in a Flat Die Pellet Mill

Evaluation of Integrated Anaerobic Digestion and Hydrothermal Carbonization for Bioenergy Production

Lignocellulosic biomass is one of the most abundant yet underutilized renewable energy resources. Both anaerobic digestion (AD) and hydrothermal carbonization (HTC) are promising technologies for bioenergy production from biomass in terms of biogas and HTC biochar, respectively. In this study, the combination of AD and HTC is proposed to increase overall bioenergy production. Wheat straw was anaerobically digested in a novel upflow anaerobic solid state reactor (UASS) in both mesophilic (37 &#176;C) and thermophilic (55 &#176;C) conditions. Wet digested from thermophilic AD was hydrothermally carbonized at 230 &#176;C for 6 hr for HTC biochar production. At thermophilic temperature, the UASS system yields an average of 165 LCH4/kgVS&#160;(VS: volatile solids) and 121 L CH4/kgVS&#160;at mesophilic AD over the continuous operation of 200 days. Meanwhile, 43.4 g of HTC biochar with 29.6 MJ/kgdry_biochar was obtained from HTC of 1 kg digestate (dry basis) from mesophilic AD. The combination of AD and HTC, in this particular set of experiment yield 13.2 MJ of energy per 1 kg of dry wheat straw, which is at least 20% higher than HTC alone and 60.2% higher than AD only.

A novel Upflow Anaerobic Solid State (UASS) reactor was used for biogas production from fibrous feedstock. Digestate from UASS reactor was hydrothermally carbonized into HTC biochar in a pressurized batch reactor. The integration of the two bioenergy concepts was applied in this study to increase overall bioenergy production.

Lignocellulosic biomass is one of the most abundant yet underutilized renewable energy resources. Both anaerobic digestion (AD) and hydrothermal ...

Manufacturing Of Robust Natural Fiber Preforms Utilizing Bacterial Cellulose as Binder

A novel method of manufacturing rigid and robust natural fiber preforms is presented here. This method is based on a papermaking process, whereby loose and short sisal fibers are dispersed into a water suspension containing bacterial cellulose. The fiber and nanocellulose suspension is then filtered (using vacuum or gravity) and the wet filter cake pressed to squeeze out any excess water, followed by a drying step. This will result in the hornification of the bacterial cellulose network, holding the loose natural fibers together.
Our method is specially suited for the manufacturing of rigid and robust preforms of hydrophilic fibers. The porous and hydrophilic nature of such fibers results in significant water uptake, drawing in the bacterial cellulose dispersed in the suspension. The bacterial cellulose will then be filtered against the surface of these fibers, forming a bacterial cellulose coating. When the loose fiber-bacterial cellulose suspension is filtered and dried, the adjacent bacterial cellulose forms a network and hornified to hold the otherwise loose fibers together.
The introduction of bacterial cellulose into the preform resulted in a significant increase of the mechanical properties of the fiber preforms. This can be attributed to the high stiffness and strength of the bacterial cellulose network. With this preform, renewable high performance hierarchical composites can also be manufactured by using conventional composite production methods, such as resin film infusion (RFI) or resin transfer molding (RTM). Here, we also describe the manufacturing of renewable hierarchical composites using double bag vacuum assisted resin infusion.

We present a novel method of manufacturing rigid and robust short natural fiber preforms using a papermaking process. Bacterial cellulose acts simultaneously as the binder for the loose fibers and provides rigidity to the fiber preforms. These preforms can be infused with a resin to produce truly green hierarchical composites.

A novel method of manufacturing rigid and robust natural fiber preforms is presented here. This method is based on a papermaking process, whereby loose ...

Bioengineering

Reducing Willow Wood Fuel Emission by Low Temperature Microwave Assisted Hydrothermal Carbonization

Biomass is a sustainable fuel, as its CO2 emissions are reintegrated in biomass growth. However, the inorganic precursors in the biomass cause a negative environmental impact and slag formation. The selected short rotation coppice (SRC) willow wood has a high ash content (<img alt="Equation 1" src="/files/ftp_upload/58970/58970eq1.jpg" /> = 1.96%) and, therefore, a high content of emission and slag precursors. Therefore, the reduction of minerals from SRC willow wood by low temperature microwave assisted hydrothermal carbonization (MAHC) at 150 &#176;C, 170 &#176;C, and 185 &#176;C is investigated. An advantage of MAHC over conventional reactors is an even temperature conductance in the reaction medium, as microwaves penetrate the whole reactor volume. This allows a better temperature control and a faster cooldown. Therefore, a succession of depolymerization, transformation and repolymerization reactions can be analyzed effectively. In this study, the analysis of the mass loss, ash content and composition, heating values and molar O/C and H/C ratios of the treated and untreated SCR willow wood showed that the mineral content of the MAHC coal was reduced and the heating value increased. The process water showed a decreasing pH and contained furfural and 5-methylfurfural. A process temperature of 170 &#176;C showed the best combination of energy input and ash component reduction. The MAHC allows a better understanding of the hydrothermal carbonization process, while a large-scale industrial application is unlikely because of the high investment costs.

A protocol for the emission precursor depletion from low quality biomass by low temperature microwave assisted hydrothermal carbonization treatment is presented. This protocol includes the microwave parameters and the analysis of the biocoal product and process water.

Biomass is a sustainable fuel, as its CO2 emissions are reintegrated in biomass growth. However, the inorganic precursors in the biomass cause a negative ...

Chemistry

Transformation of Organic Household Leftovers into a Peat Substitute

A two-step procedure is described for the synthesis of a carbon material with a similar composition and properties as peat. The produced hydrochar is made suitable for agricultural applications by removing plant growing inhibitory substances. Wet household waste such as fruit peel, coffee grounds, inedible vegetable parts, or wet lignocellulosic material in general, are treated in presence of water at 215 &#x00B0;C and 21 bar in an autoclave, i.e., by hydrothermal carbonization. All these leftovers have a considerable water content of up to 90 weight % (wt%). Adding water extends the procedure to drier materials such as nutshells or even garden prunings and compostable polymers, i.e., the plastic bag for collection of the leftovers.
Usually, the resulting carbon material, called hydrochar, produces a negative effect on plant growth when added to soil. It is supposed that this effect is caused by adsorbed phytotoxic compounds. A simple post-treatment under inert atmosphere (absence of oxygen) at 275 &#x00B0;C removes these substances. Therefore, the raw hydrochar is placed on a glass frit of a vertical tubular quartz reactor. A nitrogen gas flow is applied in down-flow direction. The tube is heated to the desired temperature by means of a heating mantle for up to one hour.
The success of the thermal treatment is easily quantified by thermogravimetry (TG), carried out in air. A weight loss is determined when the temperature of 275 &#x00B0;C is reached, since volatile content is desorbed. Its amount is reduced in the final material, in comparison to the untreated hydrochar.
The two-step treatment converts household leftovers, including compostable bags employed for their collection, into a carbon material that may serve as plant growth promoter and, at the same time, as a carbon sink for climate change mitigation.

A protocol for hydrothermal carbonization of vegetable food waste in an autoclave is presented, with subsequent dry thermal treatment at 275 &#x00B0;C in a continuous flow reactor desorbing volatile organic substances. The aim is to produce a carbon material suitable as soil amendment product or substrate component.

A two-step procedure is described for the synthesis of a carbon material with a similar composition and properties as peat. The produced hydrochar is made ...

Fabrication and Design of Wood-Based High-Performance Composites

Delignified densified wood is a new promising and sustainable material that possesses the potential to replace synthetic materials, such as glass fiber reinforced composites, due to its excellent mechanical properties. Delignified wood, however, is rather fragile in a wet state, which makes handling and shaping challenging. Here we present two fabrication processes, closed-mold densification and vacuum densification, to produce high-performance cellulose composites based on delignified wood, including an assessment of their advantages and limitations. Further, we suggest strategies for how the composites can be re-used or decomposed at the end-of-life cycle. Closed-mold densification has the advantage that no elaborate lab equipment is needed. Simple screw clamps or a press can be used for densification. We recommend this method for small parts with simple geometries and large radii of curvature. Vacuum densification in an open-mold process is suitable for larger objects and complex geometries, including small radii of curvature. Compared to the closed-mold process, the open-mold vacuum approach only needs the manufacture of a single mold cavity.

Delignified densified wood represents a new promising lightweight, high-performance and bio-based material with great potential to partially substitute natural fiber reinforced- or glass fiber reinforced composites in the future. We here present two versatile fabrication routes and demonstrate the possibility to create complex composite parts.

Delignified densified wood is a new promising and sustainable material that possesses the potential to replace synthetic materials, such as glass fiber ...

Engineering

Techniques for the Evolution of Robust Pentose-fermenting Yeast for Bioconversion of Lignocellulose to Ethanol

Lignocellulosic biomass is an abundant, renewable feedstock useful for production of fuel-grade ethanol and other bio-products. Pretreatment and enzyme saccharification processes release sugars that can be fermented by yeast. Traditional industrial yeasts do not ferment xylose (comprising up to 40% of plant sugars) and are not able to function in concentrated hydrolyzates. Concentrated hydrolyzates are needed to support economical ethanol recovery, but they are laden with toxic byproducts generated during pretreatment. While detoxification methods can render hydrolyzates fermentable, they are costly and generate waste disposal liabilities. Here, adaptive evolution and isolation techniques are described and demonstrated to yield derivatives of the native Scheffersomyces stipitis strain NRRL Y-7124 that are able to efficiently convert hydrolyzates to economically recoverable ethanol despite adverse culture conditions. Improved individuals are enriched in an evolving population using multiple selection pressures reliant on natural genetic diversity of the S. stipitis population and mutations induced by exposures to two diverse hydrolyzates, ethanol or UV radiation. Final evolution cultures are dilution plated to harvest predominant isolates, while intermediate populations, frozen in glycerol at various stages of evolution, are enriched on selective media using appropriate stress gradients to recover most promising isolates through dilution plating. Isolates are screened on various hydrolyzate types and ranked using a novel procedure involving dimensionless relative performance index (RPI) transformations of the xylose uptake rate and ethanol yield data. Using the RPI statistical parameter, an overall relative performance average is calculated to rank isolates based on multiple factors, including culture conditions (varying in nutrients and inhibitors) and kinetic characteristics. Through application of these techniques, derivatives of the parent strain had the following improved features in enzyme saccharified hydrolyzates at pH 5-6: reduced initial lag phase preceding growth, reduced diauxic lag during glucose-xylose transition, significantly enhanced fermentation rates, improved ethanol tolerance and accumulation to 40 g/L.

Adaptive evolution and isolation techniques are described and demonstrated to yield derivatives of Scheffersomyces stipitis strain NRRL Y-7124 that are able to rapidly consume hexose and pentose mixed sugars in enzyme saccharified undetoxified hydrolyzates and to accumulate over 40 g/L ethanol.

Lignocellulosic biomass is an abundant, renewable feedstock useful for production of fuel-grade ethanol and other bio-products. Pretreatment and enzyme ...

Fast Pyrolysis of Biomass Residues in a Twin-screw Mixing Reactor

Fast pyrolysis is being increasingly applied in commercial plants worldwide. They run exclusively on woody biomass, which has favorable properties for conversion with fast pyrolysis. In order to increase the synergies of food production and the energetic and/or material use of biomass, it is desirable to utilize residues from agricultural production, e.g., straw. The presented method is suitable for converting such a material on an industrial scale. The main features are presented and an example of mass balances from the conversion of several biomass residues is given. After conversion, fractionated condensation is applied in order to retrieve two condensates &#8212; an organic-rich and an aqueous-rich one. This design prevents the production of fast pyrolysis bio-oil that exhibits phase separation. A two phase bio-oil is to be expected because of the typically high ash content of straw biomass, which promotes the production of water of reaction during conversion.
Both fractionated condensation and the use of biomass with high ash content demand a careful approach for establishing balances. Not all kind of balances are both meaningful and comparable to other results from the literature. Different balancing methods are presented, and the information that can be derived from them is discussed.

A procedure for thermochemical conversion of biomass residues is presented that aims at maximizing the yield of liquid products (fast pyrolysis). It is based on a technology proven on an industrial scale and especially suitable for treating a straw type of biomass.

Fast pyrolysis is being increasingly applied in commercial plants worldwide. They run exclusively on woody biomass, which has favorable properties for ...

Twin-Screw Extrusion Process to Produce Renewable Fiberboards

A versatile twin-screw extrusion process to provide an efficient thermo-mechano-chemical pre-treatment on lignocellulosic biomass before using it as source of mechanical reinforcement in fully bio-based fiberboards was developed. Various lignocellulosic crop by-products have already been successfully pre-treated through this process, e.g., cereal straws (especially rice), coriander straw, shives from oleaginous flax straw, and bark of both amaranth and sunflower stems.
The extrusion process results in a marked increase in the average fiber aspect ratio, leading to improved mechanical properties of fiberboards. The twin-screw extruder can also be fitted with a filtration module at the end of the barrel. The continuous extraction of various chemicals (e.g., free sugars, hemicelluloses, volatiles from essential oil fractions, etc.) from the lignocellulosic substrate, and the fiber refining can, therefore, be performed simultaneously.
The extruder can also be used for its mixing ability: a natural binder (e.g., Organosolv lignins, protein-based oilcakes, starch, etc.) can be added to the refined fibers at the end of the screw profile. The obtained premix is ready to be molded through hot pressing, with the natural binder contributing to fiberboard cohesion. Such a combined process in a single extruder pass improves the production time, production cost, and may lead to reduction in plant production size. Because all the operations are performed in a single step, fiber morphology is better preserved, thanks to a reduced residence time of the material inside the extruder, resulting in enhanced material performances. Such one-step extrusion operation may be at the origin of a valuable industrial process intensification.
Compared to commercial wood-based materials, these fully bio-based fiberboards do not emit any formaldehyde, and they could find various applications, e.g., intermediate containers, furniture, domestic flooring, shelving, general construction, etc.

A versatile twin-screw extrusion process to provide an efficient thermo-mechano-chemical pretreatment on lignocellulosic biomass was developed, which leads to an increased average fiber aspect ratio. A natural binder can also be added continuously after fiber refining, leading to bio-based fiberboards with improved mechanical properties after hot pressing of the obtained extruded material.

A versatile twin-screw extrusion process to provide an efficient thermo-mechano-chemical pre-treatment on lignocellulosic biomass before using it as ...

Film Extrusion of Crambe abyssinica/Wheat Gluten Blends

Crambe abyssinica is a plant with potential for use in industrial (non-food) plant oil production. The side stream from this oil production is a high-protein crambe meal that has limited value, as it is not fit for food or feed use. However, it contains proteins that could potentially make it a suitable raw material for higher-value products. The purpose of this study was to find methods of making this side stream into extruded films, showing that products with a higher value can be produced. The study mainly considered the development of material compositions and methods of preparing and extruding the material. Wheat gluten was added as a supportive protein matrix material, together with glycerol as a plasticizer and urea as a denaturant. The extrudate was evaluated with respect to mechanical (tensile testing) and oxygen barrier properties, and the extrudate structure was revealed visually and by scanning electron microscopy. A denser, more homogeneous material had a lower oxygen transmission rate, higher strength, and higher extensibility. The most homogeneous films were made at an extruder die temperature of 125-130 &#176;C. It is shown here that a film can be extruded with promising mechanical and oxygen barrier properties, the latter especially after a final compression molding step.

Film Extrusion of Crambe abyssinica/Wheat Gluten Blends

The side stream from plant oil production of Crambe abyssinica has limited value. The purpose of this study was to find methods for extruding materials based on this side stream, demonstrating that products with a higher value can be produced. The extrudates were found to have promising properties.

Crambe abyssinica is a plant with potential for use in industrial (non-food) plant oil production. The side stream from this oil production is a ...

Forming Micro-and Nano-Plastics from Agricultural Plastic Films for Employment in Fundamental Research Studies

Microplastics (MPs) and nanoplastics (NPs) dispersed in agricultural ecosystems can pose a severe threat to biota in soil and nearby waterways. In addition, chemicals such as pesticides adsorbed by NPs can harm soil organisms and potentially enter the food chain. In this context, agriculturally utilized plastics such as plastic mulch films contribute significantly to plastic pollution in agricultural ecosystems. However, most fundamental studies of fate and ecotoxicity employ idealized and poorly representative MP materials, such as polystyrene microspheres.
Therefore, as described herein, we developed a lab-scale multi-step procedure to mechanically form representative MPs and NPs for such studies. The plastic material was prepared from commercially available plastic mulch films of polybutyrate adipate-co-terephthalate (PBAT) that were embrittled through either cryogenic treatment (CRYO) or environmental weathering (W), and from untreated PBAT pellets. The plastic materials were then treated by mechanical milling to form MPs with a size of 46-840 &#181;m, mimicking the abrasion of plastic fragments by wind and mechanical machinery. The MPs were then sieved into several size fractions to enable further analysis. Finally, the 106 &#181;m sieve fraction was subjected to wet grinding to generate NPs of 20-900 nm, a process that mimics the slow size reduction process for terrestrial MPs. The dimensions and the shape for MPs were determined through image analysis of stereomicrographs, and dynamic light scattering (DLS) was employed to assess particle size for NPs. MPs and NPs formed through this process possessed irregular shapes, which is in line with the geometric properties of MPs recovered from agricultural fields. Overall, this size reduction method proved efficient for forming MPs and NPs composed of biodegradable plastics such as polybutylene adipate-co-terephthalate (PBAT), representing mulch materials used for agricultural specialty crop production.

We show the formation and dimensional characterization of micro- and nanoplastics (MPs and NPs, respectively) using a stepwise process of mechanical milling, grinding, and imaging analysis.

Method to Produce Durable Pellets at Lower Energy Consumption Using High Moisture Corn Stover and a Corn Starch Binder in a Flat Die Pellet Mill

Summary

Explore More Videos

Chapters in this video

Evaluation of Integrated Anaerobic Digestion and Hydrothermal Carbonization for Bioenergy Production

Manufacturing Of Robust Natural Fiber Preforms Utilizing Bacterial Cellulose as Binder

Reducing Willow Wood Fuel Emission by Low Temperature Microwave Assisted Hydrothermal Carbonization

Transformation of Organic Household Leftovers into a Peat Substitute

Fabrication and Design of Wood-Based High-Performance Composites

Techniques for the Evolution of Robust Pentose-fermenting Yeast for Bioconversion of Lignocellulose to Ethanol

Fast Pyrolysis of Biomass Residues in a Twin-screw Mixing Reactor

Twin-Screw Extrusion Process to Produce Renewable Fiberboards

Film Extrusion of Crambe abyssinica/Wheat Gluten Blends

Forming Micro-and Nano-Plastics from Agricultural Plastic Films for Employment in Fundamental Research Studies