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991.
详细地探讨、优化了在密闭容器内微波消解制备铁矿石样品溶液的条件,对来自各国的大部分矿石进行消解试验。结果表明,在0.20 g样品量、15 mL盐酸、2 mL氯化亚锡、100psi(1 psi=6.894 76 kPa)的消解压力、25 min消解时间、10 min压力保持时间的条件下,大多数矿种均能完全溶解,只有少数难溶铁矿,例如秘鲁铁精矿,需将溶样酸改成10 mL硫酸-磷酸(2+8),消解压力变成10 psi,其他条件不变的情况下才能完全溶解。分析结果与常规方法相比具有一致性。 相似文献
992.
提出了微波密闭快速消解难分解的KAu(CN)2,KAu(CN)4,Pt(NH3)2(NO2)2,K2[Pt(NO2)4],Pt(NH3)2Cl2,Pt(NH3)4Cl2,(NH4)2PtCl6,K2PtCl4,Pt(C5H7O2)2等化合物的方法。比较了微波密闭消解法与传统分解法的条件;采用精密电化学滴定法分析了Au和Pt的含量,并与传统分析方法BS5658法(H2SO4发烟重量法)、火试金法和湿法重量法进行了结果对照。结果表明:以HCl-H2O2,HCl-HNO3分别为Au和Pt类化合物的消解试剂,于优 相似文献
993.
城市生活垃圾厌氧消化处理技术的应用研究进展 总被引:8,自引:0,他引:8
总结了国内外可生物降解有机城市生活垃圾(BOFMSW)厌氧消化处理技术的应用和发展概况。详细分析了垃圾成分、碳氮比、接种物、温度、pH 值、总固体含率、有机负荷率以及搅拌对BOFMSW厌氧消化的影响。介绍了国内外厌氧消化法处理可降解有机垃圾的几种工艺,比较各种工艺类型的特点,并辅以实例分析。最后指出我国利用厌氧消化技术处理BOFMSW,以及城市生活垃圾综合利用两个层面存在的问题,并给出了我国城市生活垃圾的厌氧消化技术研究和应用的发展方向。 相似文献
994.
995.
以开氏法测定氮的方法为例,着重介绍了煤中氮测定的实际意义及测定原理。介绍了实际工作中的相关注意事项,立志于煤中氮的更准确的测定。 相似文献
996.
Hydrogen is a clean energy carrier which can be used as fuel in fuel cells. Today, hydrogen is produced mainly by steam reforming of fossil fuels like natural gas or oil. But only hydrogen produced by renewable sources can be called clean energy production. One possibility for hydrogen production is the biological fermentation of biogenous wastes by hydrogen producing bacteria. For the experimental setup four 30-L-working-volume reactors were constructed for continuous biohydrogen production. As inoculum, heat-treated sludge of a wastewater treatment plant was used. Different hydraulic retention times (HRT) were tested and an organic loading rate (OLR) of 2–14 kg VS/m3*d. As starting substrate, waste sugar medium was used. The pH and other parameters were observed to find boundary conditions for a stable continuous process with a minimum of online-control measurements. The high concentration of organic acids in the reactor led to a very low pH, which was controlled manually and online > 4 up to 5.5, otherwise the biohydrogen production decreased rapidly. The gas amount varied with the different OLRs, but could be stabilised on a high level as well as the hydrogen concentration in the gas with 44–52%. No methane was detected in the gas. It turned out, that continuous biohydrogen production with stable gas amounts and qualities could be achieved at different operation conditions. The results showed, that the operation of a continuous biohydrogen reactor has to be observed very carefully to ensure a constant gas production, and that pH-control is necessary to ensure stable operation conditions. 相似文献
997.
This paper presents a comparative energy system analysis of different technologies utilising organic waste for heat and power production as well as fuel for transport. Technologies included in the analysis are second-generation biofuel production, gasification, fermentation (biogas production) and improved incineration. It is argued that energy technologies should be assessed together with the energy systems of which they form part and influence. The energy system analysis is performed by use of the EnergyPLAN model, which simulates the Danish energy system hour by hour. The analysis shows that most fossil fuel is saved by gasifying the organic waste and using the syngas for combined heat and power production. On the other hand, least greenhouse gases are emitted if biogas is produced from organic waste and used for combined heat and power production; assuming that the use of organic waste for biogas production facilitates the use of manure for biogas production. The technology which provides the cheapest CO2 reduction is gasification of waste with the subsequent conversion of gas into transport fuel. 相似文献
998.
R.S. Prakasham P. Brahmaiah T. Sathish K.R.S. Sambasiva Rao 《International Journal of Hydrogen Energy》2009
Glucose and xylose are the dominant monomeric carbohydrates present in agricultural materials which can be used as potential building blocks for various biotechnological products including biofuels production. Hence, the imperative role of glucose to xylose ratio on fermentative biohydrogen production by mixed anaerobic consortia was investigated. Microbial catabolic H2 and VFA production studies revealed that xylose is a preferred carbon source compared to glucose when used individually. A maximum of 1550 and 1650 ml of cumulative H2 production was observed with supplementation of glucose and xylose at a concentration of 5.5 and 5.0 g L−1, respectively. A triphasic pattern of H2 production was observed only with studied xylose concentration range. pH impact data revealed effective H2 production at pH 6.0 and 6.5 with xylose and glucose as carbon sources, respectively. Co-substrate related biohydrogen fermentation studies indicated that glucose to xylose ratio influence H2 and as well as VFA production. An optimum cumulative H2 production of 1900 ml for 5 g L−1 substrate was noticed with fermentation medium supplemented with glucose to xylose ratio of 2:3 at pH 6. Overall, biohydrogen producing microbial consortia developed from buffalo dung could be more effective for H2 production from lignocellulosic hydrolysates however; maintenance of glucose to xylose ratio, inoculum concentration and medium pH would be essential requirements. 相似文献
999.
1000.