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531.
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锅炉烟气脱硫技术发展综述 总被引:4,自引:0,他引:4
在调查研究的基础上,论述国内外烟道气脱硫技术的发展与前景,提出开发生产适合我国国情的烟气脱硫技术势在必行。还简要介绍了最为普遍的石灰/石灰石法脱硫基本原理。 相似文献
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曹国庆 《再生资源与循环经济》2014,(4):34-38
废铅蓄电池是再生铅主要原料,铅蓄电池产量、进出口量、社会消费保有量,以及铅蓄电池消费使用领域与废铅蓄电池产生量有关。预测2015年废铅蓄电池产生量,并讨论我国再生铅产能规模,供再生铅产业结构调整与区域布局调整作参考。 相似文献
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Photocatalytic ozonation of phenol and oxalic acid (OA) was conducted with a Ag^+/TiO2 catalyst and different pathways were found for the degradation of different compounds. Ag^+ greatly promoted the photocatalytic degradation of contaminants due to its role as an electron scavenger. It also accelerated the removal rate of OA in ozonation and the simultaneous process for its complex reaction with oxalate. Phenol could be degraded both in direct ozonation and photolysis, but the TOC removal rates were much higher in the simultaneous processes due to the oxidation of hydroxyl radicals resulting from synergetic effects. The sequence of photo-illumination and ozone exposure in the combined process showed quite different effects in phenol degradation and TOC removal. The synergetic effects in different combined processes were found to be highly related to the properties of the target pollutants. The color change of the solution and TEM result confirmed that Ag+ was easily reduced and deposited on the surface of Tit2 under photo-illumination, and dissolved again into solution in the presence of ozone. This simple cycle of enrichment and distribution of Ag^+ can greatly benefit the design of advanced oxidation processes, in which the sequences of ozone and photo-illumination can be varied according to the needs for catalyst recycling and the different properties of pollutants. 相似文献
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UV-catalytic treatment of spent caustic from ethene plant with hydrogen peroxide and ozone oxidation 总被引:1,自引:0,他引:1
YU Zheng-zhe SUN De-zhi LI Chang-hai SHI Peng-fei DUAN Xiao-dong SUN Guo-rong LIU Jun-xin 《环境科学学报(英文版)》2004,16(2):270-275
The performance of UV/H2O2, UV/O3 and UV/H2O2/O3 oxidation systems for treating spent caustic from an ethylene plant was investigated, in UV/H2O2 system, with the increase of H202 dosage, removal efficiencies of COD and the ratio of biochemical oxygen demand(BOD) to chemical oxygen demand(COD) of the effluent were increased and a better performance was obtained than the H2O2 system alone. In UV/H2O2 system, removal efficiency of COD reach 68% under the optimum condition, and BOD/COD ratio was significantly increased from 0.22 to 0.52. In UV/O3 system, with the increase of O3 dosage, removal efficiency of COD and BOD/COD ratio were increased, and a better performance was obtained than the O3 system alone. Under the optimum condition, removal efficiency of COD was 54%, and BOD/COD ratio was significantly increased from 0.22 to 0.48. In UV/H2O2/O3 system, COD removal efficiency was found to be 22.0% higher than UV/O3 system. 相似文献
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