共查询到17条相似文献,搜索用时 93 毫秒
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煅烧过程中吸收剂的烧结现象和循环反应过程中的磨损及破碎现象是导致钙基吸收剂循环煅烧/碳酸化捕集CO2性能不稳定的主要原因.针对目前几种常用的提高钙基吸收剂循环捕集性能的方法进行了总结,并对钙基吸收剂顺序脱除SO2/CO2的方法进行解释. 相似文献
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依据相关标准,对邯郸地区A、B、C 3种石灰石样品的各组分含量、活性以及邦德可磨性指数进行试验测定,并分析了其对湿法脱硫效果的影响,为河北码头电厂脱硫系统的设计提供依据。 相似文献
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对糙皮侧耳B1(白腐真菌的一种)降解碱木素的动力学进行了研究.基于Logistic方程,建立了糙皮侧耳B1在纯培养条件和碱木素存在条件下的生长动力学模型.动力学模型参数分别为0.94d-1和0.90d-1.该模型能够较好地模拟体系中生物量的变化,平均相对误差分别为3.2%和3.4%.糙皮侧耳B1对低浓度碱木素的降解存在... 相似文献
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通过深入现场的调查、实验研究,对深圳老虎坑环境园的进场垃圾进行物理成分及理化特性分析.测定了进场垃圾的容重、物理组成、含水率、发热值等基础数据,为废弃物的减量化、无害化与资源化提供了依据.特别是通过垃圾的筛分实验,提出了80 mm、60 mm的筛上物进垃圾焚烧厂的优化处理方案. 相似文献
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A system to turn a potentially harmful stream of solid waste into a set of substreams with either commercial value or highly concentrated residual streams is presented. The waste which is considered is metal impregnated (in particular Chromated Copper Arsenate (CCA) treated) wood waste and timber, such as telephone poles, railway sleepers, timber from landscape and cooling towers, wooden silos, hop-poles, cable drums and wooden playground equipment. These waste streams sum up to several 100,000 tons of material per year currently to be dumped in every major country of the European Community (EC). Technologies need to be developed to reduce this CCA treated wood waste, such that all of the metals are contained in a marketable product stream, and the pyrolysis gases and/or pyrolysis liquid are used to their maximum potential with respect to energy recuperation. Pyrolysing the CCA treated wood waste may be a good solution to the growing disposal problem since low temperatures and no oxidising agents are used, which result in lower loss of metals compared to combustion. An experimental labscale pyrolysis system has been developed to study the influence of the pyrolysis temperature and the duration of the pyrolysis process on the release of metals and the mass reduction. The macrodistribution and microdistribution of the metals in the solid pyrolysis residue is studied using Inductively Coupled Plasma Mass Spectrometry (ICP–MS) and Scanning Electron Microscopy coupled with Energy Dispersive X-ray Analysis (SEM–EDXA). Furthermore, a complete mass balance is calculated over the pyrolysis system. Based on these results a semi-industrial pyrolysis system (pilot plant scale) has been developed consisting of three stages: grinding, packed bed pyrolysis and metal separation. Special types of equipment have been developed to carry out the three stages. A new grinding system has been developed, based on a crushing mechanism rather than a cutting mechanism. The crushed wood is introduced by means of a screw feeding system into a reaction column. In this pyrolysis reactor the wood is heated by subjecting it to a flow of hot gases. This causes an adiabatic pyrolysis, which results in volatilisation of the volatile compounds whereas the mineral compounds (containing the metals) remain entrapped in a coal-type residue which is very rich in carbon. The condensable compounds in the pyrolysis gas condense while leaving the reaction zone due to the inverse temperature gradient. The pyrolysis gas leaving the reactor is used as fuel for the hot gas generator. The charcoal which is extracted at the bottom of the reactor, is cooled, compressed, removed and stored, ready to feed the subsequent stage. A specially developed grinder is used to remove the metal particles from the charcoal and the separation between metal and charcoal particles is accomplished in a pneumatic centrifuge as a result of the difference in density. Using this system the ultimate waste is less than 3% of the initial wood mass. Results obtained with a semi-industrial scale prototype confirm the effectiveness of the process. 相似文献
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Holmström Sara J. M. Riise Gunnhild Strand Line Tau Geibe Christine Van Hees Patrick A. W. Wu Qinglan Lundström Ulla S. 《Water, Air, & Soil Pollution: Focus》2003,3(4):97-120
Dissolved organic carbon (DOC) fractions and different low molecular weight organic acids (LMWOAs) were determined in soil solutions from two lime or ash treated Norway spruce sites in the south of Sweden. At Hasslöv, 3.45 t ha-1 or 8.75 t ha-1 dolomite were applied 15 years before sampling. Horröd was treated with 4.28 t ha-1 ash and 3.25 t ha-1 dolomite and sampled four years later. Propionate (7–268 M) and malonate (2–34 M) were the LMWOAsfound in the highest concentrations at Hasslöv. Two other LMWOAs dominated at Horröd, namely citrate (18–64 M)and fumarate (5–31 M). The differences in concentration of most of the determined LMWOAs at Hasslöv were significantly increased due to treatment. The LMWOAs comprised between 1.1–6.3% of the DOC at Hasslöv and 4.5–17.6% at Horröd. At Hasslöv normally 3–10% of the total acidity (TA) was due to LMWOAs and the average specific buffer capacity was 74 ± 22 mmol mol-1C.The total DOC concentration in the mor layer solution was 16 mM for the dolomite treated plots compared to 10 mM at the untreated plot. A major part of the increase in DOC at the treated plots apparently had a hydrophobic character and was of high molecular weight corresponding to 3–10 kDa. The concentration of DOC < 1 kDa in the control and treated plots was similar. 相似文献
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水解-好氧联合处理难降解有机废水的试验研究 总被引:1,自引:0,他引:1
介绍了水解-好氧工艺在污水处理领域的应用。水解和好氧处理工艺各有优缺点,而水解-好氧联合处理工艺可以发挥单一工艺的优点,尤其在难降解污水的处理中有其独特的优势,试验结果表明:在23-32℃.HRT=15-28h时,该联合处理工艺对中药加工废水的COD去除率在85%以上。 相似文献
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采用聚乙烯亚胺(PEI)改性氨基化锆基金属有机骨架材料(UiO-66-NH2)制备了UiO-66-NH2/PEI,利用XRD、SEM和FTIR对产物进行了表征,并将其用于吸附水中的U(Ⅵ)。考察了UiO-66-NH2/PEI吸附U(Ⅵ)的影响因素,并研究了吸附动力学和等温线。实验结果表明:UiO-66-NH2/PEI对U(Ⅵ)具有良好的吸附效果,PEI与UiO-66-NH2质量比为30%、溶液pH为6、吸附剂投加量为80 mg/L、吸附时间为120 min、初始U(Ⅵ)质量浓度为10 mg/L时,UiO-66-NH2/PEI对U(Ⅵ)的去除率达98.2%(303 K下);UiO-66-NH2/30%PEI对U(Ⅵ)的吸附在60 min内达到平衡,吸附过程符合准二级动力学模型和Langmuir模型,最大吸附量达452.49 mg/g。 相似文献