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低渗致密气藏基质酸化产能评价及特征分析 被引量:6
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作者 方文超 姜汉桥 孙彬峰 《大庆石油地质与开发》 CAS CSCD 北大核心 2014年第1期106-110,共5页
为准确评价低渗致密气藏基质酸化后的气井产能,指导酸化施工方案设计,依据酸化规模建立了2种典型酸化后地层模型,在分析渗流模式的基础上采用分流动区域的方法分别推导出2种模型的气井产能评价公式,并分析了基质酸化后气井产能特征。对... 为准确评价低渗致密气藏基质酸化后的气井产能,指导酸化施工方案设计,依据酸化规模建立了2种典型酸化后地层模型,在分析渗流模式的基础上采用分流动区域的方法分别推导出2种模型的气井产能评价公式,并分析了基质酸化后气井产能特征。对于低渗致密气藏,当酸化规模较小时,增加酸液有效作用距离比增加酸化带渗透率增产效果更明显,此时酸化工作液应着重考虑缓速酸体系。当酸化规模较大时,若储层含较多的酸蚀矿物,增大酸液有效作用距离更利于增产;但若储层较难酸蚀,则增加酸化带渗透率更利于增产,此时工作液应着重考虑强酸体系或易返排的泡沫酸体系。 展开更多
关键词 低渗致密气藏 基质 产能评价 产能特征 酸化规模 有效作用距离 缓速 泡沫
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Treatment of flotation wastewater using biological activated carbon 被引量:10
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作者 董颖博 林海 +1 位作者 刘泉利 霍汉鑫 《Journal of Central South University》 SCIE EI CAS 2014年第9期3580-3587,共8页
A laboratory scale up-flow biological activated carbon(BAC) reactor was constructed for the advanced treatment of synthetic flotation wastewater. Biodegradation of a common collector(i.e., ethyl xanthate) for non-ferr... A laboratory scale up-flow biological activated carbon(BAC) reactor was constructed for the advanced treatment of synthetic flotation wastewater. Biodegradation of a common collector(i.e., ethyl xanthate) for non-ferrous metallic ore flotation was evaluated. The results show that the two stages of domestication can improve microbial degradation ability. The BAC reactor obtains a chemical oxygen demand(COD) reduction rate of 82.5% for ethyl xanthate and its effluent COD concentration lowers to below 20 mg/L. The kinetics equation of the BAC reactor proves that the activated carbon layers at the height of 0 mm to 70 mm play a key role in the removal of flotation reagents. Ultraviolet spectral analysis indicates that most of the ethyl xanthate are degraded by microorganisms after advanced treatment by the BAC reactor. 展开更多
关键词 flotation wastewater biological activated carbon BIODEGRADATION chemical oxygen demand
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Effect of galvanic contact on the flotability of galena in the presence and absence of a collector 被引量:2
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作者 M.B.Eslami Andargoli S.Jannesar Malakooti +1 位作者 F.Doulati Ardejani H.Abdollahi 《International Journal of Mining Science and Technology》 SCIE EI 2012年第5期629-632,共4页
In this paper,the effect of various electrochemical environments in the galena flotation is investigated.The electrochemical environments consisted of a ball mill for grinding of galena ore and a Denver flotation cell... In this paper,the effect of various electrochemical environments in the galena flotation is investigated.The electrochemical environments consisted of a ball mill for grinding of galena ore and a Denver flotation cell for flotation of galena in the laboratory scale.In order to achieve the maximum recovery with sodium hyposulfite,the concentrations of 0.06 and 0.12 M of air and nitrogen gases have been used to control the pulp potential in the Denver flotation cell.The galena sample was from the ''Era mine'' which is located in the Kiyasar area,north of Iran.This mine contains:Galena(PbS) at least 22%,Fluorite(CaF 2) 73.37%,Quartz(SiO 2) 2.54% and other minerals such as Cerussite(PbCO 3) and Kaolinite(Al 2 Si 2 O 5(OH) 4).Flotation of Galena was conducted in a 0.12 M of sodium hyposulfite solution.It was found that the amount of recovery by this process was 85% and 63% in the presence and absence of potassium amyl xanthate(KAX) and at an estimated potential of 280 to 350 mV respectively while the recovery was 70% and 52% at an approximate potential of 175 to 210 mV in water in the presence and absence of collector(KAX). 展开更多
关键词 Flotation Collector Galena Electrochemical Galvanic interactions
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