工业侧流试验高温脱硫剂的性能测试

通过混合法制备的高温煤气脱硫剂在放大的工厂侧流装置上于高温、高压固定床反应器、强还原性的真实煤气中进行了16次循环、1200h的脱硫 再生测试.结果表明,该脱硫剂具有良好的抗磨损性、稳定的反应性能和较高硫容(累计硫容300.49%);饱和后的脱硫剂可用含1%～3%O2的水蒸汽完全再生.取得的结果为优化新型脱硫剂以适用于更大规模的示范项目提供了可靠依据.     

CO2对石灰石脱硫剂的活化作用

在间歇式鼓泡反应器的烟气脱硫实验装置中,研究了CO2气体活化处理对石灰石脱硫剂浆液烟气脱硫效率的影响. 依据脱硫过程中石灰石脱硫剂浆液pH值随脱硫反应时间的变化规律,初步分析了CO2对石灰石脱硫剂的活化作用及活化后石灰石脱硫剂的烟气脱硫过程机理. 结果表明,CO2气体的活化处理促进了石灰石在水溶液中的溶解,进而改善了石灰石脱硫剂浆液的烟气脱硫反应活性,使处理后的石灰石脱硫剂浆液的烟气脱硫效率和脱硫剂的利用率提高. 基于流化床反应器连续过程的实验结果,证实了CO2对石灰石脱硫剂的活化作用. 为提高石灰石在烟气脱硫中的反应活性提供了一种新的工艺,可用于烟气脱硫中对石灰石脱硫剂浆液的活化.     

用于低温干法催化氧化所吸附苯酚的CuO-CeO2/AC吸附-催化剂

对CuO-CeO2/AC(活性炭载氧化铜和氧化铈)吸附-催化剂低温干法催化氧化所吸附苯酚的行为进行了研究. 结果表明,CeO2的引入促进了CuO/AC对吸附苯酚的低温催化氧化活性,苯酚初始催化氧化温度降低约30℃;连续吸附-催化氧化循环过程中的苯酚吸附量平均提高6%左右,苯酚脱附量平均减少77%. 铈掺杂的促进作用可能在于提高了表面化学吸附态的氧含量,进而减少了催化氧化过程中在吸附-催化剂表面形成的残留物量.     

Evaluation of polyaromatic hydrocarbon removal from aqueous solutions using activated carbon and hyper‐crosslinked polymer (Macronet MN200)

BACKGROUND: Sorption of polycyclic aromatic hydrocarbons (PAHs) on activated carbon and the Macronet polymeric sorbent MN200 was investigated to determine the effectiveness of each sorbent for removal of pollutants from aqueous solution and their possible use as sorbent materials for groundwater. Experiments were carried out to determine the loading capacities of a family of PAHs (acenaphthene, anthracene, fluoranthene, fluorene, naphthalene and pyrene). RESULTS: Activated carbon was the more effective sorbent, with maximum loadings of PAHs between 90 and 230 g kg^?1, while MN200 resin showed values of 25–160 g kg^?1. Loading isotherms based on the Langmuir, Freundlich and Redlich–Peterson models were determined. The hydrophobic character of the pollutants appeared as an important parameter related to the sorption process. Equilibrium and kinetic parameters were used to determine the retardation factors for each PAH. CONCLUSION: The calculated values for the simulation of barrier thickness using both sorbents, taking into account EU requirements for PAHs in groundwater effluent, were perfectly reasonable as a first estimate. The better kinetic properties of MN200 are evident in lower hydraulic residence times and consequently in a lower barrier thickness. Copyright © 2008 Society of Chemical Industry     

钇钡铜氧在气体纯化和空分方面应用初探

采用自制的钇钡铜氧 (YBa2 Cu3 O7- x)样品和动态吸附实验装置研究了该材料在气体纯化和空分方面应用的可能性及条件。实验表明 ,该材料对氧有强烈的选择吸附性 ,并且可以再生 ,可以把 YBCO做为除氧分子筛。     

Laboratory simulated slipstream testing of novel sulfur removal processes for gasification application

The Wabash River Integrated Methanol and Power Production from Clean Coal Technologies (IMPPCCT) project is investigating an Early Entrance Coproduction Plant (EECP) concept to evaluate integrated electrical power generation and methanol production from coal and other carbonaceous feedstocks. Research, development and testing (RD&T) that is currently being conducted under the project is evaluating cost effective process systems for removing contaminants, particularly sulfur species, from the generated gas which contains mainly synthesis gas (syngas), CO₂ and steam at concentrations acceptable for the methanol synthesis catalyst. The RD&T includes laboratory testing followed by bench-scale and field testing at the SG Solutions Gasification Plant located in West Terre Haute, Indiana. Actual synthesis gas produced by the plant was utilized at system pressure and temperature for bench-scale field testing.     

Multi-stage ammonia production for sorption selective catalytic reduction of NOx

Sorption selective catalytic reduction of nitrogen oxides (NO_x) (sorption-SCR) has ever been proposed for replacing commercial urea selective catalytic reduction of NO_x (urea-SCR), while only the single-stage sorption cycle is hitherto adopted for sorption-SCR. Herein, various multi-stage ammonia production cycles is built to solve the problem of relative high starting temperature with ammonia transfer (AT) unit and help detect the remaining ammonia in ammonia storage and delivery system (ASDS) with ammonia warning (AW) unit. Except for the single-stage ammonia production cycle with MnCl₂, other sorption-SCR strategies all present overwhelming advantages over urea-SCR considering the much higher NO_x conversion driven by the heat source lower than 100°C and better matching characteristics with low-temperature catalysts. Furthermore, the required mass of sorbent for each type of sorption-SCR is less than half of the mass of AdBlue for urea-SCR. Therefore, the multifunctional multi-stage sorption-SCR can realize compact and renewable ammonia storage and delivery with low thermal energy consumption and high NO_x conversion, which brings a bright potential for efficient commercial de-NO_x technology.     

用吸附处理工艺去除饮用水中阴离子表面活性物质的实验研究

采用活性炭、沸石和硅藻土三种常用吸附剂,通过静态实验和动态实验对饮用水中低浓度阴离子表面活性物质(LAS)的去除进行了考察.静态实验结果表明,用吸附法可有效地去除LAS,并且在通常条件下受温度、pH影响不显著,但在有机物如腐殖酸浓度较高的情况下LAS的吸附明显受到抑制.动态实验比较了不同LAS浓度、不同吸附剂对流出曲线的影响,并求出LAS的孔扩散系数和液膜扩散系数.考察LAS和腐殖酸双组分溶液穿透时间及饱和分数的结果表明,腐殖酸为控制化合物,因此实际应用中只需要考虑腐殖酸的去除即可满足LAS的去除要求.     

Benefication technology for lithium-containing hydrogenic mineral products

A technology of reagentless sorption benefication is developed for lithium-containing hydrogenic mineral products of calcium chloride and magnesium chloride type. By the technology, it is possible to obtain lithium concentrates at a ratio of the summed Mg and Ca concentration to Li concentration less than 15, which is 12–25 times lower than in the primary brines. __________ Translated from Fiziko-Teknicheskie Problemy Razrabotki Poleznykh Iskopaemykh, No. 6, pp. 89–99, November–December, 2005.     

Facile regeneration vitreous microfibrous entrapped supported ZnO sorbent with high contacting efficiency for bulk H2S removal from reformate streams in fuel cell applications

In this study, a microfibrous carrier consisting of 3 vol.% of 8 μm (diameter) glass fibers is used to entrap 45 vol.% of 150 to 250 μm (diameter) SiO₂ support particulates. ZnO is then nanodispersed onto the support by impregnation at the loading of 17 wt.%. At equivalent bed volumes, ZnO/SiO₂-entrapped materials provide twofold longer breakthrough times for H₂S (with a 67% reduction in sorbent loading) compared with packed beds of 1 to 2 mm commercial extrudates. Five-log reductions in H₂S concentration with up to 75% ZnO utilization at breakthrough are achieved. H₂S concentrations from 60 to 2000 parts per million in volume (ppmv) can be reduced to as little as 0.6 ppmv at 400°C in 30% H₂O at a face velocity of 1.7 cm/s for layers as thin as 1.0 mm. At 500 to 600°C, ZnO/SiO₂-entrapped materials provide much higher regenerability in air than do 1 to 2 mm commercial extrudates. The use of glass fibers permits greater than 50 regeneration cycles. This paper was presented at the ASM Materials Solutions Conference & Show held October 18–21, 2004 in Columbus, OH.