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11.
N,N,N-三甲基-2,3-二(硬脂酰氧基)丙基氯化铵(CDESA)的生物降解性 总被引:1,自引:0,他引:1
采用活性环氧中间体失水甘油基三甲基氯化铵合成了一种阳离子双酯表面活性剂——N,N,N-三甲基-2,3-二(硬脂酰氧基)丙基氯化铵(CDESA),来代替传统的难降解的表面活性剂型柔软剂,如目前国内仍在大量使用的双十八烷基二甲基氯化铵(D1821)。对CDESA的好氧降解性能进行了研究:以天然环境中的生活沉降污泥作为微生物源,用河水稀释,经培养、驯化后用于测试降解时间和半衰期,并与D1821的好氧降解性能作了对比。结果表明,CDESA的半衰期为3 d,容易降解,而D1821半衰期为7 d,较难降解,CDESA生物降解性能优于D1821。 相似文献
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探讨采用先进的A/O(厌氧菌 /好氧菌 )生物脱氮技术对己内酰胺生产废水进行处理的工作机理和工艺设计方法 ,分析了温度、溶解氧、pH值、进水碳氮比等参数对生物脱氮工艺过程的影响 ,并对其关键技术进行了研究 相似文献
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A novel nucleation apparatus is presented for the production of narrow sized nuclei from various powder and binder liquid combinations. Mono-sized binder liquid droplets are produced by a specially designed mono-disperse droplet generator. The droplet generator is positioned above a conveyor belt, transporting a powder bed through the spray zone of the droplet generator. By nucleating powder on a conveyer belt, the nucleation mechanism is completely separated from all other granulation mechanisms due to the lack of relative motion between primary particles and/or formed nuclei. Nucleation tests were performed using chalcopyrite and limestone powders with water as the binder liquid. At all operating conditions, the formed nuclei were found to originate from multiplicities of drops that merged on the powder bed surface. Investigation of the dynamics of nuclei formation showed that powder-binder liquid combinations with fast penetration dynamics result in less variation in the number of droplets from which nuclei originate. Smaller and more narrowly distributed nuclei were also achieved by increasing powder speed through the spray zone. 相似文献
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本文分析了当前流行的仿石瓷质砖包裹颗粒制造方法的弊端,并通过改进设备和采用新的工艺方法,研制出仿石效果更佳的产品,这样既提高了颗粒的包裹效率,又降低了生产成本。 相似文献
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Catherine J Watson 《Nutrient Cycling in Agroecosystems》1987,14(3):193-204
The15N isotope was used to study the mode of action of individual nitrogen sources in a 30% urea:30% ammonium nitrate: 10% ammonium sulphate:30% filler (w/w) granular fertilizer for perennial ryegrass in a greenhouse pot experiment. The fertilizer consisted of two types of granules, one containing 80% urea and 20% filler and the second containing 48% ammonium nitrate (AN), 16% ammonium sulphate (AS) and 36% filler. In addition the effect of dolomite compared with silica as the filler was investigated on nitrogen recovery from the 30:30:10:30 formulation.Dolomite adversely affected the recovery of nitrate N from the system and evidence suggested that MgCO3 was the active component. Granules containing dolomite resulted in a lower dry-matter yield than those containing silica, however the difference was not significant as nitrate contributed only 20% of the N in the formulation. AN gave the greatest DM yield and urea the lowest with AS being intermediate. The15N budget in shoots, roots and soil indicated that only 65% of the N from urea was recovered at the end of the experiment compared with 86% for AN and 91% for AS. The dry-matter yield of the 30:30:10:30 formulation using silica as the filler was intermediate between urea and AN; however, the apparent N recovery was significantly higher than expected from the sum of the individual components. The use of15N labelling indicated that using separate granules for ammonium N and urea the recovery of urea was improved by 11% in the triple N mixture when both AN and AS were present in the second granule compared to the recovery on its own. The enhanced recovery of urea appeared to be a function of AN and AS acting together as neither source in double combination with urea had any effect on urea N recovery.Urea enhanced the recovery of nitrate N by 10% but decreased the recovery of AS by 6% (in the 30:30:10:30 formulation) in comparison with the single sources on their own. The results indicate that interactions can occur between N sources even when they are physically separated by being in different granules. 相似文献
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UASB-接触氧化处理高浓度有机废水试验研究 总被引:7,自引:0,他引:7
本文主要通过UASB 接触氧化生化处理模型对某化工厂废水的试验研究,探索运用UASB法处理高浓度有机废水的可行性。同时还探讨了废水的CODcr及含盐量对UASB处理效率的影响,以及关键参数的选用。 相似文献
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仓式静态连续好氧堆肥发酵工艺的水气研究 总被引:2,自引:0,他引:2
采用仓式静态连续好氧堆肥发酵工艺,通过建立水平衡体系,系统地研究了水分对整个发酵工艺的影响,得出了仓式静态连续好氧堆肥发酵具有工艺简便,热交换快,水气蒸发量大等特点;好氧堆肥发酵过程中发酵温度保持在65℃左右,含水量控制在45%~55%有利于有机物降解,垃圾堆肥可在40~50d腐熟;静态连续好氧一次堆肥发酵物料的含水量需控制在35%以下,机械自动分选(类)筛分效率高,筛分率在90%~95%,垃圾减容在50%~60%.二次堆肥发酵物料的含水量需控制在25%~30%,机械除杂(碎石、碎玻璃等)效果好,有机肥中杂质含量低于0.8%.静态好氧二次堆肥发酵可以用垃圾渗沥水补充水分,达到资源循环再利用,可实现污水零排放. 相似文献