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SOLID WASTE COMPACTOR AND EJECTOR TRANSFER SYSTEM PERFORMANCE WITH BULK SWITCHGRASS

机译:固体废物压实机和喷射器传输系统性能与散装交换机

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A solid waste compactor and ejector transfer system provided alternative bulk compaction and hauling for switchgrass (SG) either field chopped with a forage harvester (FC) or with bales size-reduced with a tub grinder as coarse (CTG) and fine (FTG) materials. Bulk-compacted biomass was envisioned for an average depot-to-biorefinery transport distance of 56 km to take advantage of moderately increased bulk densities and efficient loading and unloading. The compactor increased bulk densities, although bulk densities were less than values reported for large packaged bales, either round or square. Maximum bulk densities observed were 168 kg m-3 (wet density) or 139 dry kg m(-3) (Dkg m(-3)). Bulk density differences were observed among SG materials, although the increased bulk density values for FC and FTG were statistically the same. Some variations were noted between bulk densities determined with ejector trailer loads and laboratory universal test machine measurements, which had a volumetric factor difference of over 33,000. Although bulk density values were less than those reported for bales, advantages were noted with bulk compaction loading and ejection unloading, such that FC loading a full over-the-road semi-trailer required a minimum of 24 min, as limited by the supply system, and unloading only required 5 min. If the supply to the compactor did not limit the compaction rate, a load time of 5 min was calculated for a theoretical maximum compaction rate (128.4 DMg h(-1)) of FC based on compactor displacement and FC "loose" dry bulk density of 124.8 Dkg m(-3). Volumetric efficiency and other factors would potentially reduce the theoretical maximum compaction rate in practice. Low energy requirements for bulk compaction and ejection indicated an economy of scale, with compaction and unloading ejection energies as low as 1.05 and 0.05 kWh DMg-1 for FC, respectively. Bulk compaction consumed energy that was orders of magnitude less than some agglutination techniques and offered a compromise to easily increase bulk density for moderate transport distances. Spillage between the compactor and ejector trailer should be addressed for commercial applications, especially for FC materials that flow well. Bulk compaction proved viable with off-the-shelf designs, and there is potential to improve designs with reduced-friction internal surfaces and integration of compaction and ejection functions into a dedicated vehicle.
机译:固体废物压实机和喷射器转移系统为切换(SG)提供了替代批量压实和拖运,其中型材用饲料收割机(FC)或用桶研磨机减少粗糙的尺寸 - 粗(CTG)和细(FTG)材料。设想了批量压实的生物量,以实现56公里的平均仓库到生物垃圾箱运输距离,以利用中度增加的散装密度和高效的装卸。压实机增加了堆积密度,尽管散装密度小于报告的大包装大包,无论是圆形还是正方形的值。所观察到的最大堆积密度为168 kg m-3(湿密密度)或139干kg m(-3)(dkg m(-3))。在SG材料中观察到批量密度差异,尽管Fc和FTG的增加的堆积密度值统计学相同。使用喷射器拖车负载和实验室通用测试机测量确定的堆积密度之间的一些变化,其具有超过33,000的容积因子差。尽管堆积密度值小于报告的包包,但是散装压实负载和喷射卸载的优点,使得FC装载全面的过度路半拖车至少24分钟,这是供应系统的限制并且只需要卸载5分钟。如果对压实机的电源没有限制压实率,则根据压实机位移和Fc“松动”干堆积密度,计算FC的理论最大压实速率(128.4dmg H(-1)),计算5分钟的负载时间124.8 dkg m(-3)。体积效率和其他因素可能会降低实践中的理论最大压实率。批量压实和喷射的低能量要求表明了规模经济,分别压实和卸下喷射能量,分别为1.05和0.05 kWh DMG-1。散装压实消耗的能量比某种凝集技术的数量级,并且提供了易于增加堆积密度的折衷以供中等运输距离。应解决压实机和喷射器拖车之间的溢出物,特别适用于商业应用,特别是对于流量良好的FC材料。散装压实证明了现成的设计可行,并且有可能改善具有减少摩擦内表面的设计以及将压实和喷射功能的集成到专用车辆中。

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