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Organic matter removal and CH4 production performance recoveries and microbial community changes in upflow anaerobic biofilter after long term starvation
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作者 Jianmin Li Runyu Liu +2 位作者 Xiuhong Liu Qing Yang Shiyong Zhang 《Journal of Environmental Sciences》 2025年第10期735-746,共12页
The organic matter inmunicipal wastewater can be recovered by anaerobic biological treatment,making further resource utilization of municipal wastewater,which meets the requirements of sustainable development.An upflo... The organic matter inmunicipal wastewater can be recovered by anaerobic biological treatment,making further resource utilization of municipal wastewater,which meets the requirements of sustainable development.An upflow anaerobic biofilter(UAF)treating municipal wastewater was established.The performances of stable operation and recovery operation of UAF after long-term starvation(234 days)and the changes of microbial community structure were researched.By gradually reducing HRT from 10 h to 4 h,the UAF achieved the treatment performance of pre-starvation after only 50 days recovery operation,in which total COD and soluble COD removal efficiencies reached 66%and 69%,respectively,and the CH_(4) production rate was 0.21 L CH_(4)/g CODremoval.The recovery performance of UAF after long term starvation showed that the recovery sequence of three main anaerobic processes was hydrolytic acidification,hydrogen-acetate production and methanogenesis.High-throughput sequencing results indicated that dominant bacteria associated with hydrolytic acidification process changed from Moduliflexaceae and Trichococcus in stable operation stage to Trichococcus and Romboutsia in recovery stage.Besides,the dominant archaea changed from Methanosaeta(hydrotrophic methanogens)to Methanobacterium(acetotrophic methanogens),showing Methanobacterium was more resistant to starvation environment.Therefore,by using UAF for biological treatment of organic matter,even after a long period of starvation,the system would not be completely destroyed.Once it resumed operation,the treatment performance could be restored in a short period of time. 展开更多
关键词 Municipal wastewater upflow anaerobic biofilter STARVATION Performance recovery Microbial community structures
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Anammox transited from denitrification in upflow biofilm reactor 被引量:14
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作者 ZHANGShao-hui ZHENGPing HUAYu-mei 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2004年第6期1041-1045,共5页
Anammox was successfully transited from heterotrophic denitrification and autotrophic denitrification in two upflow biofilm reactors, respectively. The results showed that the volumetric loading rate and nitrogen remo... Anammox was successfully transited from heterotrophic denitrification and autotrophic denitrification in two upflow biofilm reactors, respectively. The results showed that the volumetric loading rate and nitrogen removal efficiency in the reactor transited from heterotrophic denitrification were higher than that in its counterpart. When the hydraulic retention time was 12 h or so, the total nitrogen loading rate was about 0.609 kg N/(m3·d), and the effluent ammonia and nitrite concentrations were less than 8.5 mg/L and 2.5 mg/L, respectively. The upflow anammox biofilm reactor was capable of keeping and accumulating the slow-growing bacteria efficiently. During operation of the reactor, the biomass color was gradually turned from brownish to red, and the ratio of ammonia consumption, nitrite consumption and nitrate production approached the theoretical one. These changes could be used as an indicator for working state of the reactor. 展开更多
关键词 ANAMMOX DENITRIFICATION TRANSITION upflow anammox biofilm reactor
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Anaerobic treatment of source-separated domestic bio-wastes with an improved upflow solid reactor at a short HRT 被引量:3
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作者 Hongliang Wang Shikun Zhu +2 位作者 Bo Qu Yu Zhang Bin Fan 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2018年第4期255-264,共10页
Anaerobic treatment is the core technology for resource and energy recovery from source-separated domestic bio-wastes. The higher efficiency of an improved upflow solid reactor(IUSR) designed in this study was demon... Anaerobic treatment is the core technology for resource and energy recovery from source-separated domestic bio-wastes. The higher efficiency of an improved upflow solid reactor(IUSR) designed in this study was demonstrated in the treatment of concentrated black water and kitchen waste. The highest methane production of 48 L/person/day was achieved at the hydraulic retention time(HRT) of 7 days, while the other measures of performance at the HRT of 8.3 days were better than at the HRT of 7 or 10 days, achieving a methane production of 43 L/person/day, removal of total chemical oxygen demand(TCOD)of 89%, removal of soluble chemical oxygen demand(SCOD) of 92%, and conversion of chemical oxygen demand(COD) to methane of 71%. It is not recommended to decrease HRT lower than 7 days due to the instability of the initial period. The concentrations of volatile fatty acids(VFAs) in the IUSR were less than 10 mg/L, indicating that the anaerobic process was stable. Sludge bed development showed that sludge bed with high microbial activity was formed in the bottom and that the precipitation zone of effluents formed should preferably occupy 30% of the height of the IUSR. The effluents of the IUSR could be used for irrigation in agriculture in combination with a settling tank accompanied by disinfection to remove solids and pathogens. 展开更多
关键词 Sustainable sanitation Anaerobic treatment Source-separated domestic bio-wastes Improved upflow solid reactor
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R&D and Application of Catalyst for Resid Hydrotreating in Upflow Reactor
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作者 Niu Chuanfeng Hu Dawei +1 位作者 Dai Lishun Yang Qinghe (Research Institute of Petroleum Processing, Beijing 100083) 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2008年第2期5-10,共6页
In order to extend the operating cycle of the upflow reactor for resid hydrotreating, the Re- search Institute of Petroleum Processing taking into account the specifics of resid hydrotreating upflow reactor has develo... In order to extend the operating cycle of the upflow reactor for resid hydrotreating, the Re- search Institute of Petroleum Processing taking into account the specifics of resid hydrotreating upflow reactor has developed the high-performance RUF series of catalysts suitable for operation in the upflow reactor. The results of commercial application of catalysts revealed that this RUF series of catalysts loaded after optimized grading could effectively remove metals, sulfur and carbon residue from the re-siduum to provide improved oil for the following fixed-bed reactor. In the meantime, the RUF series of catalysts have excellent stability to reach an operating cycle of 1.5 years, resulting in minimization of losses caused by refinery downtime. 展开更多
关键词 resid hydrotreating upflow reactor CATALYST operating cycle
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Experimental Investigation of Pressure Drop Hysteresis in a Cocurrent Gas-Liquid Upflow Packed Bed 被引量:1
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作者 徐红彬 毛在砂 《过程工程学报》 CAS CSCD 北大核心 2001年第3期239-242,共4页
Extensive experimental work on hysteresis in a c℃urrent gas-liquid upflow packed bed was carried out with three kinds of packings and the air-water system. However, only when packed with small glass beads ((1.4 mm) w... Extensive experimental work on hysteresis in a c℃urrent gas-liquid upflow packed bed was carried out with three kinds of packings and the air-water system. However, only when packed with small glass beads ((1.4 mm) was the bed pressure drop hysteresis observed. Two more liquids with different liquid properties were employed to further examine the influence of parameters on pressure drop hysteresis. The similarity of pressure drop hysteresis in packed beds was concluded in combination of experimental evidence reported in literature. 展开更多
关键词 气液固填充塔 同向上流固定 压力降滞 试验
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不同流向下浊质特性对砂过滤效能及流阻分布影响
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作者 贺维鹏 罗天昊 +3 位作者 施周 南军 马晶伟 孙祥辉 《中国给水排水》 北大核心 2025年第19期22-28,共7页
关于待滤水中浊质特性(如形态和带电性)对不同流向过滤过程的影响机制尚缺乏系统认识,为此,以聚氯化铝(PAC)为混凝剂,采用混凝调控的方式制备含有不同特性浊质颗粒的待滤水,然后通过中试对比研究下向流和上向流过滤在截污效能、流阻分... 关于待滤水中浊质特性(如形态和带电性)对不同流向过滤过程的影响机制尚缺乏系统认识,为此,以聚氯化铝(PAC)为混凝剂,采用混凝调控的方式制备含有不同特性浊质颗粒的待滤水,然后通过中试对比研究下向流和上向流过滤在截污效能、流阻分布等方面的差异性,继而系统探讨两种流向条件下的过滤机理。结果表明,相对于下向流过滤,PAC投加量相同时上向流过滤更快地进入稳定阶段,并且随着PAC投加量的增加,上向流过滤的穿透阶段出水浊度增长更快、末期浊度更高;在两种流向条件下,滤后水UV_(254)值均随PAC投加量的增加而减小,但相同PAC投加量时上向流过滤的UV_(254)值高于下向流过滤,即上向流过滤对腐殖酸的协同去除效果要差;上向流过滤比下向流过滤的水头损失均匀,且总水头损失增速低。 展开更多
关键词 上向流过滤 下向流过滤 滤后水浊度 水头损失分布 协同除污
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三级升流式水解酸化污泥膨胀床处理焦化废水的中试研究
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作者 张爽 谢海松 +2 位作者 唐尧 陶一通 梁镇 《工业水处理》 北大核心 2025年第3期198-205,共8页
采用三级升流式水解酸化污泥膨胀床+A^(2)O中试装置处理焦化废水,研究升流式水解酸化污泥膨胀床对污染物的去除率及抑制来水污染物浓度波动的效果,并对比研究了中试全流程生化系统与现有系统对焦化废水的处理效果和系统各反应器中微生... 采用三级升流式水解酸化污泥膨胀床+A^(2)O中试装置处理焦化废水,研究升流式水解酸化污泥膨胀床对污染物的去除率及抑制来水污染物浓度波动的效果,并对比研究了中试全流程生化系统与现有系统对焦化废水的处理效果和系统各反应器中微生物的分布。中试结果显示,系统稳定运行后,三级升流式水解酸化污泥膨胀床平均COD去除率为57.72%,最高为66.67%,出水COD波动量为进水COD波动量的29.85%,中试全流程生化系统平均COD去除率为91.38%,最大COD去除率为95.73%,平均氨氮去除率为97.20%。特征污染物分析显示,系统稳定运行后,氰化物和硫化物平均去除率分别为81.53%和92.07%。微生物高通测序显示中试装置中具有更丰富的微生物群落,尤其在富集去除特定污染物的微生物方面优势明显。三级升流式水解酸化污泥膨胀床+A^(2)O中试工艺流程在更短停留时间内取得了更优的处理效果,为焦化废水处理提供了新的工艺方向。 展开更多
关键词 焦化废水 水解酸化 中试研究 升流式水解酸化污泥膨胀床
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Effect of wastewater composition on the calcium carbonate precipitation in upflow anaerobic sludge blanket reactors 被引量:6
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作者 Shucheng YANG Yanling HE +3 位作者 Yonghong LIU Charles CHOU Pengxiang ZHANG Dongqi WANG 《Frontiers of Environmental Science & Engineering》 SCIE EI CSCD 2010年第2期142-149,共8页
Calcium carbonate often precipitates in anaerobic reactors treating wastewater with high calcium content.The aim of this paper is to study the effect of wastewater composition on calcium carbonate precipitation in upf... Calcium carbonate often precipitates in anaerobic reactors treating wastewater with high calcium content.The aim of this paper is to study the effect of wastewater composition on calcium carbonate precipitation in upflow anaerobic sludge blanket(UASB)reactors.Two laboratory-scale UASB reactors were operated with calcium-containing influents using acetate and carbohydrate as substrate,respectively.There was an obvious accumulation of inorganic precipitate observed in the biogranules.Observations via scanning electron microscope(SEM)and energy dispersive spectroscopy(EDS)showed that the acclimated biogranules in the two reactors differed in microstructure.Calcium carbonate was found to have precipitated on the surface of acetate-degrading biogranules,but precipitated at the core of the carbohydrate-degrading biogranules.The results indicated that substrates had significant influence on the location of calcium carbonate precipitation in anaerobic granular sludge,which was expected due to the different methanogens distribution and pH gradient within the granular sludge degrading various substrates.Moreover,the location of calcium carbonate precipitation substantially affected the specific methanogenic activity(SMA)of the granular sludge.The SMA of the acetate-degrading biogranules dropped from 1.96 gCODCH4·gVSS^(–1)·d^(–1)to 0.61 gCODCH4·gVSS^(–1)·d^(–1)after 180-d of operation in the reactor.However,the SMA of the carbohydrate-degrading biogranules was not adversely affected by calcium carbonate precipitation. 展开更多
关键词 calcium carbonate PRECIPITATION anaerobic granular sludge wastewater composition MICROSTRUCTURE upflow anaerobic sludge blanket(UASB)
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Anaerobic treatment of fresh leachate from a municipal solid waste incinerator by upflow blanket filter reactor
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作者 Pinjing HE Min LI +1 位作者 Suyun XU Liming SHAO 《Frontiers of Environmental Science & Engineering》 SCIE EI CSCD 2009年第4期404-411,共8页
This paper describes the feasibility of fresh leachate treatment by an upflow blanket filter(UBF).Through dilution and partial effluent recycling,the organic loading rates increased from 0.51 to 14.56 kg COD/(m^(3)... This paper describes the feasibility of fresh leachate treatment by an upflow blanket filter(UBF).Through dilution and partial effluent recycling,the organic loading rates increased from 0.51 to 14.56 kg COD/(m^(3)·d),meanwhile the corresponding hydraulic retention time decreased from 9.0 to 3.6 d.The reactor was able to achieve steady-state within 80 d.Based on the distribution of COD fluxes in the process,it was concluded that anabolism was the main pathway of COD removal in the initial phase(1–33 d),accounting for 57%–85%of total COD removed.As the anaerobic consortium of bacteria reached steady-state(after 70–86 d),the majority of COD removed was transformed into methane,because the specific methane yield was close to the theoretical value(0.36 L CH4/(g CODdeg)). 展开更多
关键词 distribution of COD fluxes effluent recycling LEACHATE methane yield organic loading rate upflow blanket filter
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上流式反应器渣油加氢催化剂失活特征及对策
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作者 张鹏 王欣刚 于长旺 《石化技术与应用》 2025年第3期217-221,共5页
在中化泉州石化有限公司3.3 Mt/a渣油加氢处理装置考察了上流式反应器和固定床反应器(UFR/VRDS)组合工艺渣油加氢催化剂(RM系列和SRH系列)的运行状况,分析了催化剂失活特征和规律,并提出应对措施。结果表明:UFR催化剂最先失活,其次固定... 在中化泉州石化有限公司3.3 Mt/a渣油加氢处理装置考察了上流式反应器和固定床反应器(UFR/VRDS)组合工艺渣油加氢催化剂(RM系列和SRH系列)的运行状况,分析了催化剂失活特征和规律,并提出应对措施。结果表明:UFR催化剂最先失活,其次固定床第2、第3反应器在承担更多脱金属作用后在运行中后期先后出现催化剂失活,第4、第5反应器催化剂活性相对较好;UFR催化剂容金属能力、积炭量均低于固定床脱金属催化剂,存在级配催化剂失活不同步的问题;通过优化催化剂级配、采用两段式“组合换剂”的优化方案,将脱硫催化剂使用时间由330 d延长至超过600 d,催化剂利用率提高了33.2%,节约25%的新鲜催化剂,有效降低了装置催化剂使用成本。 展开更多
关键词 渣油加氢 催化剂 上流式反应器 固定床反应器 催化剂失活
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油气上窜速度计算方法的改进与应用
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作者 赵洪达 《石油化工建设》 2025年第10期172-174,共3页
文章针对传统油气上窜速度计算方法在复杂工况下的局限性,提出了一种改进方法。该方法综合考虑非牛顿流体特性、井眼轨迹影响、动态参数实时校正及多因素耦合效应,通过引入非牛顿流体流变模型、修正井眼轨迹影响、实时更新关键参数,并... 文章针对传统油气上窜速度计算方法在复杂工况下的局限性,提出了一种改进方法。该方法综合考虑非牛顿流体特性、井眼轨迹影响、动态参数实时校正及多因素耦合效应,通过引入非牛顿流体流变模型、修正井眼轨迹影响、实时更新关键参数,并构建多因素耦合综合模型,显著提升了上窜速度的计算精度。以一口大斜度水平井为例,改进模型的计算误差仅为4.2%,较传统方法大幅降低。研究成果为钻井过程中的井控决策提供了科学依据,也为非常规油气资源的高效开发提供了有力的技术支持。 展开更多
关键词 油气 上窜速度 计算方法
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UASB工艺用于冷轧含油废水预处理的试验
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作者 贾利涛 姚治国 +4 位作者 朱伟明 刘旭明 张玉瑶 董舒宇 赵锦 《净水技术》 2025年第10期136-143,共8页
【目的】冷轧含油废水中油、化学需氧量(COD)含量高,可生化性差,传统物理化学法处理冷轧含油废水存在产生大量含油污泥的问题,运行成本高并产生二次污染,而基于污水处理过程中的污泥生物减量化已成为国内外的研究热点和发展趋势。上流... 【目的】冷轧含油废水中油、化学需氧量(COD)含量高,可生化性差,传统物理化学法处理冷轧含油废水存在产生大量含油污泥的问题,运行成本高并产生二次污染,而基于污水处理过程中的污泥生物减量化已成为国内外的研究热点和发展趋势。上流式厌氧污泥床(UASB)对较高的有机负荷具有良好的耐受性,且能提高废水的可生化性,有利于解决上述问题。【方法】采用UASB对冷轧含油废水进行了预处理的可行性试验,通过逐渐提高进水有机负荷和油含量来考察UASB对油和COD的去除效果及试验过程中冷轧含油废水可生化性的变化,并探究有机负荷对产气率和颗粒污泥的影响。【结果】当有机负荷为4~12 kg COD/(m^(3)·d),油质量浓度小于500 mg/L时,COD和油平均去除率分别为77.27%和64.13%,产气率可达0.35 m^(3)/(kg COD),可生化性显著提高,且颗粒污泥粒径、污泥沉降性、胞外聚合物(EPS)随有机负荷的增加而提高;当有机负荷增加至13 kg COD/(m^(3)·d)以上,油质量浓度高于500 mg/L时,UASB处理效果急剧下降,颗粒污泥沉降性变差甚至上浮流失。【结论】UASB对有机负荷的波动和油有较好的耐受性,研究结果为UASB代替破乳、气浮等产生大量含油污泥的物理方法进行冷轧含油废水预处理提供了数据支撑。 展开更多
关键词 上流式厌氧污泥床(UASB) 冷轧含油废水 颗粒污泥 可生化性 胞外聚合物(EPS)
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UASB反应器对冲布水布局模式流动力学特性分析
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作者 阳泽灏 田凤国 +1 位作者 韦志扬 李国华 《节能》 2025年第7期76-79,共4页
对上流式厌氧发酵罐(UASB)内对冲布水模式下的流体动力学特性进行数值模拟研究,探讨不同进水管数量下的速度分布、湍流强度以及剪切速率分布特点。结果表明,对冲进水布置方式下,罐内存在一个中心上升、外围下降的大尺度循环流动。随着... 对上流式厌氧发酵罐(UASB)内对冲布水模式下的流体动力学特性进行数值模拟研究,探讨不同进水管数量下的速度分布、湍流强度以及剪切速率分布特点。结果表明,对冲进水布置方式下,罐内存在一个中心上升、外围下降的大尺度循环流动。随着进水管数量的增加,底部与中心区域的流动强度降低,但未能有效降低整个反应器内的流动滞止区的占比,但湍动能、剪切速率的分布均匀性得到有效改善。 展开更多
关键词 上流式厌氧发酵罐 流体力学 对冲布水模式
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聚酯废水处理及再生水回用工程实例
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作者 林宝春 陈学勤 《净水技术》 2025年第7期177-183,209,共8页
【目的】以年产120万t差别化聚酯项目为例,分析了锦州市某化纤企业3000 m^(3)/d污水站的设计、安装、调试及运行成效。针对废水可生化性差(BOD5/COD<0.3)、有机物质量浓度高(COD均值为8000 mg/L)、含难降解芳香族化合物及微量乙醛的... 【目的】以年产120万t差别化聚酯项目为例,分析了锦州市某化纤企业3000 m^(3)/d污水站的设计、安装、调试及运行成效。针对废水可生化性差(BOD5/COD<0.3)、有机物质量浓度高(COD均值为8000 mg/L)、含难降解芳香族化合物及微量乙醛的特性,构建一套高效稳定的深度处理工艺体系,突破传统生物法对低B/C比废水的处理瓶颈,同时实现污水资源化回用与能源回收的双重目标。【方法】设计采用分质预处理+溶气气浮+均质酸化(提升可生化性)+上流式厌氧污泥床反应器[UASB,有机负荷为8 kg COD/(m^(3)·d)]+2段缺氧-好氧(AO,强化脱氮除磷)+高效沉淀(化学强化除磷)+纤维转盘微滤+臭氧催化氧化(降解难溶有机物)+超滤反渗透(保障回用水质)工艺,并对主要构筑物核心设计参数进行系统介绍。【结果】经系统处理后出水COD质量浓度小于30 mg/L,氨氮、总磷等各项出水指标均优于《城镇污水处理厂污染物排放标准》(GB 18918—2002)一级A标准;同时,出水满足《地表水环境质量标准》(GB 3838—2002)中的Ⅳ类标准,COD去除率可达99%,出水80%以上回用,处理成本为2.63元/m^(3)。【结论】该污水处理工艺在实际应用中表现良好,能有效处理化纤企业产生的高浓度、难降解废水,具有处理效率高、运行稳定、抗冲击负荷强、运行费用省等优点,可为同类污水站提标改造或扩建设计提供指导和借鉴。 展开更多
关键词 聚酯废水 上流式厌氧污泥床反应器(UASB) 两段 AO 工艺 纤维转盘微滤 臭氧催化氧化
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预处理+UASB+两级AO+MBR工艺处理垃圾转运中心废水
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作者 任丽 《中国资源综合利用》 2025年第8期261-264,280,共5页
以某垃圾中转站废水处理为研究对象,介绍处理工艺、设计参数及运行效果。废水处理量为100 m^(3)/d。其化学需氧量(Chemical Oxygen Demand,COD)高,总氮(Total Nitrogen,TN)浓度高,含重金属和动植物油脂等杂质。采用“预处理+升流式厌氧... 以某垃圾中转站废水处理为研究对象,介绍处理工艺、设计参数及运行效果。废水处理量为100 m^(3)/d。其化学需氧量(Chemical Oxygen Demand,COD)高,总氮(Total Nitrogen,TN)浓度高,含重金属和动植物油脂等杂质。采用“预处理+升流式厌氧污泥床(Upflow Anaerobic Sludge Bed,UASB)+两级厌氧好氧(Anaerobic Oxic,AO)+膜生物反应器(Membrane Bio-Reactor,MBR)”的处理工艺,出水符合《污水排入城镇下水道水质标准》(GB/T 31962—2015)的一级B标准,吨水费用为33.671元。该工艺具有较好的技术经济性。 展开更多
关键词 垃圾转运中心 废水处理 升流式厌氧污泥床(UASB) 二级厌氧好氧(AO) 膜生物反应器(MBR)
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“隔油气浮+UASB+两级AO+加磁高效沉淀”组合工艺处理椰子制品饮料废水的项目设计
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作者 宋冬 《中国资源综合利用》 2025年第10期262-264,共3页
某椰子制品饮料企业废水含有多种污染物,可溶性有机物、化学需氧量(Chemical Oxygen Demand,COD)、生化需氧量(Biochemical Oxygen Demand,BOD)、悬浮物(Suspended Solids,SS)和油脂类含量高,可生化性好。废水处理站采用“隔油气浮+升... 某椰子制品饮料企业废水含有多种污染物,可溶性有机物、化学需氧量(Chemical Oxygen Demand,COD)、生化需氧量(Biochemical Oxygen Demand,BOD)、悬浮物(Suspended Solids,SS)和油脂类含量高,可生化性好。废水处理站采用“隔油气浮+升流式厌氧污泥床(Upflow Anaerobic Sludge Bed,UASB)+两级厌氧好氧(Anaerobic Oxic,AO)+加磁高效沉淀”组合工艺,降低COD、BOD、总氮(Total Nitrogen,TN)、总磷(Total Phosphorus,TP)、SS等污染物的含量,使得出水水质稳定达到《城镇污水处理厂污染物排放标准》(GB 18918—2002)的一级A标准,同时满足《地表水环境质量标准》(GB 3838—2002)的Ⅳ类水标准较严值要求。 展开更多
关键词 椰子制品饮料 废水 隔油气浮 升流式厌氧污泥床(UASB) 两级厌氧好氧(AO) 加磁高效沉淀
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Morphology of polar ionospheric O^+ ion upflow: FAST observations during quiet time 被引量:3
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作者 DANG Ge MA ShuYing ZHOU YunLiang 《Chinese Science Bulletin》 SCIE EI CAS 2007年第24期3403-3415,共13页
With energetic ion measurements on FAST satellite, the morphologic features of quiet-time ionospheric O+ ion upflowing at altitudes of 2000 to 4000 km are drawn out for the first time. The pre-noon cusp/cleft is the p... With energetic ion measurements on FAST satellite, the morphologic features of quiet-time ionospheric O+ ion upflowing at altitudes of 2000 to 4000 km are drawn out for the first time. The pre-noon cusp/cleft is the predominant region of upflowing occurrence for O+ with lower energy. Meanwhile the pre-dawn sector near the equatorward edge of the plasma convection dominates the occurrence for the higher energy O+ ions. No matter whether the energy is lower or higher, the upflows occur often over a wide MLT range of lower latitudes outside the auroral oval. The upflowing within the pre-midnight (21:00― 22:00 MLT) auroral oval carrys larger energy fluxes, with extremely large fluxes for higher energy O+ appearing near the polar cap boundary. For altitudes of 2000―4200 km under observation, the ion conics occur much more frequently than ion beams. Ion beams are rarely found below 3000 km, while the conics occur uniformly over the observed altitudes. 展开更多
关键词 双极电离层 氧离子流 磁气圈耦合 人造卫星观测
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前置上流式反应器的固定床渣油加氢工艺运行分析及研发建议 被引量:5
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作者 邵志才 刘涛 +1 位作者 胡大为 戴立顺 《石油炼制与化工》 CAS CSCD 北大核心 2024年第3期32-37,共6页
原油价格高企,需要高效利用原油资源,渣油加氢技术是较好的选择,微膨胀的上流式反应器与固定床反应器结合的渣油加氢工艺技术已成功开发并多次工业应用。分别选取两套上流式反应器与固定床反应器结合的渣油加氢装置(A、C)和两套固定床... 原油价格高企,需要高效利用原油资源,渣油加氢技术是较好的选择,微膨胀的上流式反应器与固定床反应器结合的渣油加氢工艺技术已成功开发并多次工业应用。分别选取两套上流式反应器与固定床反应器结合的渣油加氢装置(A、C)和两套固定床渣油加氢装置(B、D)进行对比分析,结果表明:前置上流式反应器的渣油加氢工艺技术也能加工不同类型的渣油原料,A装置加工高氮含量的渣油原料,其在装置运转第14周期脱硫率、脱氮率、脱金属率和降残炭率分别为82.46%,31.51%,73.69%,54.85%;C装置加工高硫含量的渣油原料,其在装置运转第5周期脱硫率、脱氮率、脱金属率和降残炭率分别为85.23%,38.71%,72.83%,54.49%;级配催化剂均满足装置的技术需求。与固定床渣油加氢装置相同,上流式反应器第一催化剂层也会出现较大的径向温差,第一反应器压降也会升高,主要与催化剂床层中的物流分布和膨胀程度有关。建议进行上流式反应器内构件、催化剂和关键工艺参数的协同研发。 展开更多
关键词 上流式反应器 渣油加氢 径向温差 加氢脱硫 加氢脱氮
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南京地区水厂上、下向流生物活性炭工艺应用效能对比
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作者 周冰洁 兰童 +4 位作者 王萌 杨遇春 毛步云 刘成 陈卫 《净水技术》 CAS 2024年第S01期15-20,81,共7页
通过对南京地区两水厂中上向流和下向流生物活性炭(biological activated carbon,BAC)池的长期检测,系统对比了两种类型BAC的净化效能和自身性能变化规律。结果表明,在水厂长期运行过程中,上向流BAC池对氨、高锰酸盐指数等水质指标的总... 通过对南京地区两水厂中上向流和下向流生物活性炭(biological activated carbon,BAC)池的长期检测,系统对比了两种类型BAC的净化效能和自身性能变化规律。结果表明,在水厂长期运行过程中,上向流BAC池对氨、高锰酸盐指数等水质指标的总体去除效能优于下向流BAC池;上向流、下向流BAC池中BAC的碘值和亚甲蓝值衰减程度相近,但上向流BAC池中BAC颗粒的吸附性能优于下向流水厂;运行8年后,两类BAC池中生物量和生物活性都趋于稳定,但上向流BAC池中的微生物群落丰富度较高,生物降解性能较好。 展开更多
关键词 生物活性炭池 上向流 下向流 碘值 种群结构
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基于UHOFe处理制浆造纸废水体系的计算模拟与优化 被引量:3
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作者 梁琛 黄闻宇 +4 位作者 董怡武 蒙李杰 韦子深 高宇凡 王双飞 《中国造纸》 CAS 北大核心 2024年第6期154-164,共11页
在保证废水水力停留时间的情况下,为研究上流式多相废水处理氧化塔(UHOFe)的结构及进水参数、搅拌转速对反应器内部流态均匀度的影响,通过计算流体力学(CFD)的数值模拟方法,考察装载搅拌桨叶对UHOFe反应器内部流场的影响情况。首先建立... 在保证废水水力停留时间的情况下,为研究上流式多相废水处理氧化塔(UHOFe)的结构及进水参数、搅拌转速对反应器内部流态均匀度的影响,通过计算流体力学(CFD)的数值模拟方法,考察装载搅拌桨叶对UHOFe反应器内部流场的影响情况。首先建立了反应器的参数化模型,通过引入平面内速度变异系数(MF)作为进水均匀度的评价指标,然后使用计算机流体力学软件ANSYS 2022,结合单因素实验以及正交实验,对反应器的内部流体流态进行三维流场数值模拟仿真。模拟仿真结果表明,装载搅拌桨叶可加强反应器内部液体的混合,且当出水口高度为12850 mm、入水口速率为3 m/s、搅拌桨叶尺寸为1300 mm、搅拌转速为140 r/min时,反应器内的进水均匀度效果最优,最有利于提升Fenton体系的药剂间混合效率,最终提高废水处理效率。 展开更多
关键词 上流式多相废水处理氧化塔 计算流体力学 进水均匀度 数值模拟仿真
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