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Molecular transformation of dissolved organic matter in refinery wastewaters: Characterized by FT-ICR MS coupled with electrospray ionization and atmospheric pressure photoionization 被引量:2
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作者 Chen He Wei-Ming Chen +1 位作者 Chun-Mao Chen Quan Shi 《Petroleum Science》 SCIE EI CAS CSCD 2023年第1期590-599,共10页
Dissolved organic matter(DOM)in refinery wastewater is an extremely complex mixture of various organic compounds.Using mass spectrometry,it is impossible to characterize all of the DOM molecules with only one ionizati... Dissolved organic matter(DOM)in refinery wastewater is an extremely complex mixture of various organic compounds.Using mass spectrometry,it is impossible to characterize all of the DOM molecules with only one ionization source.In this study,negative-ion,electrospray ionization(ESI),positive-ion ESI,and positive-ion atmospheric pressure photoionization(APPI)were coupled with Fourier transform ion cyclotron resonance mass spectrometry(FT-ICR MS)to analyze the molecular composition of DOM in a refinery wastewater stream during the treatment process.There were obvious differences in the heteroatom composition,number of DOM constituents,and chemical properties in refinery wastewater under the three ionization modes.Acidic CHO and CHOS compounds detected by(+)ESI,basic CHN and CHON compounds detected by(þ)ESI,and hydrocarbons detected by(+)APPI were analyzed to determine the molecular transformations that occurred during treatment.In an anaerobic biological treatment process,acidic CHO and CHOS compounds with a high oxygen content were preferentially removed,and acidic CHO and CHOS compounds with a low oxygen content were produced.In an aerobic biological process,acidic CHO and CHOS compounds with a low oxygen content were preferentially removed,and acidic CHO and CHOS compounds with a high oxygen content were produced.The whole biological treatment process has a poor removal efficiency for CHN and CHON compounds,and hydrocarbons.An activated carbon(AC)adsorption process removed different heteroatom compounds mainly with a low oxygen content for acidic and basic compounds.The transformation mechanism of CHO and CHOS compounds in the biological treatment process was analyzed by the Kendrick mass defect(KMD)theory and a mass difference network analysis.In the anaerobic process,large amounts of oxygenated CHO and CHOS compounds were degraded by decarboxylation,deoxydation,demethoxylation,and dehydration reactions,and converted to lower oxygen content compounds.In the aerobic processes,these low oxygen CHO and CHOS compounds mainly underwent carboxylation and oxidation reactions.This study determined the transformation characteristics and mechanisms of different types of organic compounds in refinery wastewater during the treatment process.The results provide guidance for the design and optimization of technologies for refinery wastewater treatment. 展开更多
关键词 refinery wastewater DOM Molecular transformation ESI APPI FT-ICR MS
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Treatment of Slightly Polluted Wastewater in an Oil Refinery Using a Biological Aerated Filter Process 被引量:6
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作者 XIE Wenyu ZHONG Li CHEN Jianjun 《Wuhan University Journal of Natural Sciences》 CAS 2007年第6期1094-1098,共5页
The slightly polluted wastewater from oil refinery contains some COD, oil pollutants and suspended solids (SS). A small-scale fixed film biological aerated filter (BAF) process was used to treat the wastewater. Th... The slightly polluted wastewater from oil refinery contains some COD, oil pollutants and suspended solids (SS). A small-scale fixed film biological aerated filter (BAF) process was used to treat the wastewater. The influences of hydraulic retention time (HRT), air/water volume flow ratio and backwashing cycle on treatment efficiencies were investigated. The wastewater was treated by the BAF process under optimal conditions: the HRT of 1.0 h, the air/water volume flow ratio of about 5 : 1 and the backwashing cycle of every 4-7 days. The results showed that the average removal efficiency of COD, oil pollutants and SS was 84.5%, 94.0% and 83.4%, respectively. And the average effluent concentration of COD, oil pollutants and SS was 12.5, 0.27, 14.5 mg·L^-1, respectively. The experimental results demonstrated that the BAF process is a suitable and highly efficient method to treat the wastewater. 展开更多
关键词 biological aerated filter (BAF) slightly polluted wastewater oil refinery treatment efficiency
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Pretreatment of super viscous oil wastewater and its application in refinery 被引量:2
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作者 Chen Chunmao Yan Guangxu +1 位作者 Guo Shaohui Yang Yong 《Petroleum Science》 SCIE CAS CSCD 2008年第3期269-274,共6页
Wastewater from super viscous oil processing cannot be effectively treated by conventional wastewater treatment plants in refineries because of its high concentration of various organic pollutants. In order to resolve... Wastewater from super viscous oil processing cannot be effectively treated by conventional wastewater treatment plants in refineries because of its high concentration of various organic pollutants. In order to resolve this problem, a number of investigations were conducted in our work to understand the physicochemical properties, sedimentation, demulsification and pretreatment of such super viscous oil refinery wastewater. The results showed that the key issues for pretreatment of this wastewater were: (1) Optimized process parameters were used in the sedimentation and demulsification processes for oil removal to effectively recover oil and remove scum from wastewater; (2) A suitable flocculation process was selected to minimize oil, suspended solids (SS) and chemical oxygen demand (CODcr). A pretreatment process including three continuous steps: oil removal by sedimentation, oil removal by demulsification, and flotation separation, was proposed and applied in Liaohe Petrochemical Company, PetroChina and the oil content in effluents was less than 200 mg/L and CODcr less than 2,500 mg/L, which completely met the requirement for influent of the conventional wastewater treatment plant, and the recovered super viscous oil reached 5,873 tons in the initial year in Liaohe Petrochemical Company, PetroChina. 展开更多
关键词 Super viscous oil refinery wastewater pretreatment process SEDIMENTATION DEMULSIFICATION FLOCCULATION
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Efficient ozonation of reverse osmosis concentrates from petroleum refinery wastewater using composite metal oxideloaded alumina 被引量:2
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作者 Yu Chen Chun-Mao Chen +5 位作者 Brandon A.Yoza Qing X.Li Shao-Hui Guo Ping Wang Shi-Jie Dong Qing-Hong Wang 《Petroleum Science》 SCIE CAS CSCD 2017年第3期605-615,共11页
Novel Mn–Fe–Mg-and Mn–Fe–Ce-loaded alumina(Mn–Fe–Mg/Al2O3 and Mn–Fe–Ce/Al2O3) were developed to catalytically ozonate reverse osmosis concentrates generated from petroleum refinery wastewaters(PRW-ROC). Hi... Novel Mn–Fe–Mg-and Mn–Fe–Ce-loaded alumina(Mn–Fe–Mg/Al2O3 and Mn–Fe–Ce/Al2O3) were developed to catalytically ozonate reverse osmosis concentrates generated from petroleum refinery wastewaters(PRW-ROC). Highly dispersed 100–300-nm deposits of composite multivalent metal oxides of Mn(Mn^2+), Mn^3+,and Mn^4+, Fe(Fe^2+)and Fe^3+ and Mg(Mg^2+), or Ce(Ce^4+) were achieved on Al2O3 supports. The developed Mn–Fe–Mg/Al2O3 and Mn–Fe–Ce/Al2O3 exhibited higher catalytic activity during the ozonation of PRW-ROC than Mn–Fe/Al2O3, Mn/Al2O-3, Fe/Al2O3, and Al2O3. Chemical oxygen demand removal by Mn–Fe–Mg/Al2O3-or Mn–Fe–Ce/Al2O3-catalyzed ozonation increased by 23.9% and23.2%, respectively, in comparison with single ozonation.Mn–Fe–Mg/Al2O3 and Mn–Fe–Ce/Al2O3 notably promoted áOH generation and áOH-mediated oxidation. This study demonstrated the potential use of composite metal oxide-loaded Al2O3 in advanced treatment of bio-recalcitrant wastewaters. 展开更多
关键词 Petroleum refinery wastewater Reverseosmosis concentrate Catalytic ozonation Compositemetal oxide
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Rapid aerobic granulation using biochar for the treatment of petroleum refinery wastewater
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作者 Xin Wang Jie Ming +5 位作者 Chun-Mao Chen Brandon A.Yoza Qian-Wei Li Jia-Hao Liang Geoffrey Michael Gadd Qing-Hong Wang 《Petroleum Science》 SCIE CAS CSCD 2020年第5期1411-1421,共11页
Aerobic granular sludge technology has great potential for the treatment of petroleum refinery wastewater.However,strategies to shorten the granulation time and improvement the stability still need to be developed.In ... Aerobic granular sludge technology has great potential for the treatment of petroleum refinery wastewater.However,strategies to shorten the granulation time and improvement the stability still need to be developed.In this work,biochar was prepared from waste petroleum activated sludge(biochar-WPS) and used in a sequencing batch reactor for the treatment of petroleum refinery wastewater.Biochar-WPS presented the surface area of 229.77 m2/g,pore volume of 0.28 cm3/g,H/C and O/C atomic ratios of 0.42 and 0.21,respectively.The porous structure and a high degree of hydrophilicity were found to facilitate microbial colonization and adhesion as well as particle aggregation.Application of biochar-WPS resulted in the formation of more substantial and stable aerobic granules(~66% of granules> 0.46 mm diameter) 15 days earlier compared with the control.The addition of biochar-WPS enhanced the average removal efficiency of chemical organic demand(~3%),oil(~4%)and total nitrogen(~10%) over the control.Increased microbial richness and diversity were observed within the formed granules and had an increased(~4%) proportion of denitrifying bacteria.These results indicate that an aerobic granulation mechanism using biochar-WPS is a feasible option for the treatment of petroleum refinery wastewater. 展开更多
关键词 BIOCHAR Petroleum refinery wastewater Petroleum activated sludge Granular sludge Denitrifying bacteria
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Wastewater Quality Assessment of a Petroleum Refinery in Ghana
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作者 Frederick Kobina Nkrumah Mike Agbesi Acheampong +1 位作者 Ebenezer David Okwaning Ansa Jackson Adiyiah 《Journal of Environmental Science and Engineering(B)》 2013年第9期514-520,共7页
TOR (Tema oil refinery) is the only petroleum refinery in Ghana. To assess the quality of the wastewater, wastewater samples taken from three points of discharge into the treatment plant and the treated effluent wer... TOR (Tema oil refinery) is the only petroleum refinery in Ghana. To assess the quality of the wastewater, wastewater samples taken from three points of discharge into the treatment plant and the treated effluent were analyzed for physico-chemical characteristics. The levels of the pH, temperature, conductivity, COD (Chemical Oxygen Demand), TDS (Total Dissolved Solids), TSS (Total Suspended Solids) and phenol were assessed from January to June, 2011. The results obtained indicate varied levels of contaminants in both the untreated and treated wastewater. The average values of the treated effluent parameters analyzed were 38 ℃, 6,258 μs.cm-1, 314 mg-L-1, 115 mg.L-1, 2,689 mg-L-1 and 1 mg.L-1 for the temperature, conductivity, COD, TDS, TSS and phenol, respectively. The results suggest that both the raw wastewater and the treated effluent did not meet the discharge limit set by Ghana Environmental Protection Agency. Therefore, the treated effluent required additional treatment before it can be discharged into the environment. This suggests that the wastewater treatment plant of TOR is ineffective for the type of wastewater produced. 展开更多
关键词 Industrial wastewater PETROLEUM EFFLUENT POLLUTANTS Tema oil refinery Ghana.
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Removal of Heavy Metals (Copper, Manganese and Zinc) from Industrial Wastewater of Baiji Refinery by Granular Activated Carbon
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作者 dr Muzher M. Ibrahem AlDoury Abbas Ali Kanoosh 《Journal of Chemistry and Chemical Engineering》 2012年第9期789-798,共10页
The aim of the present work is to remove heavy metals (copper, manganese, and zinc) from industrial wastewater of Baiji refinery using GAC (granular activated carbon). The most important factors affecting adsorpti... The aim of the present work is to remove heavy metals (copper, manganese, and zinc) from industrial wastewater of Baiji refinery using GAC (granular activated carbon). The most important factors affecting adsorption process have been studied, which are granular activated carbon thickness, H, inlet pollutant concentration, Cv, and liquid hourly space velocity, LHSV. All experiments were performed under constant temperature at 25℃ and pH = 7. The experimental apparatus was designed and constructed to enable controlling of the operating conditions. Employing five levels for each of H and LHSV and three levels for Co required 75 runs for each metal. Box-Wilson method was used to reduce the number of experiments to 15 for each metal. The results indicated that copper, manganese, and zinc can be completely removed from wastewater using activated carbon. However, breakthrough time for zinc is low. It is also shown that breakthrough time (TB) and exhaustion time (TE) are inversely proportional with pollutant concentration and LHSV (liquid hour space velocity) while it is directly proportional with the thickness of activated carbon column. 展开更多
关键词 GAC (granular activated carbon) heavy metals oil refinery wastewater.
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炼化企业停工大检修污水水质特性综合表征
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作者 张璇 陈霖 +4 位作者 张鑫倩 王庆宏 何晨 詹亚力 陈春茂 《工业水处理》 CAS CSCD 北大核心 2024年第9期151-159,共9页
炼化企业停工大检修期间无组织排放大量高浓度污水,对综合污水处理厂的正常运行构成严重冲击。将宏观污染指标与微观污染组成相结合,从污染负荷、体系稳定性、污染组成及生物毒性4方面,对清洗污水和清洗-钝化混合污水两类典型大检修污... 炼化企业停工大检修期间无组织排放大量高浓度污水,对综合污水处理厂的正常运行构成严重冲击。将宏观污染指标与微观污染组成相结合,从污染负荷、体系稳定性、污染组成及生物毒性4方面,对清洗污水和清洗-钝化混合污水两类典型大检修污水进行水质特性综合分析。清洗污水和清洗-钝化混合污水均表现出极高的有机污染负荷、悬浮态和胶体态污染物、体系稳定性以及较强的急性生物毒性。清洗污水和清洗-钝化混合污水的有机污染组成复杂,两者的极性污染物组成均以OxS1类为主,前者以O3S1类污染物相对丰度最高,推测源自磺酸盐类表面活性物质;后者以O4S1类污染物相对丰度最高,推测源自烷基硫酸盐类或硫酸酯盐类表面活性物质。两者的弱极性污染物组成差异较大,清洗污水以醇醚类、醚类和石油烃类为主,而清洗-钝化混合污水则主要是小分子杂环类、芳香烃类和酚类。对两类典型大检修污水水质特性的分析研究可指导大检修污水预处理工艺开发,为炼化企业大检修期间综合污水处理厂的稳定运行提供支持。 展开更多
关键词 炼化企业 停工大检修污水 水质特性表征 预处理
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炼化污水中低温水解酸化性能及微生物特性对比
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作者 姜梁妍 王庆宏 +5 位作者 李晋 梁家豪 尚鹏寅 宋艳珂 李琢宇 陈春茂 《化工进展》 EI CAS CSCD 北大核心 2024年第8期4654-4663,共10页
以炼化污水为研究对象,对比了中温和低温条件下的水解酸化性能、微生物群落结构和功能。中温(35℃)水解酸化更利于COD去除(40.51%)和水质可生化性提高(BOD_(5)/COD提高至0.53),而低温(15℃)COD去除率和BOD_(5)/COD仅为20.96%和0.26。中... 以炼化污水为研究对象,对比了中温和低温条件下的水解酸化性能、微生物群落结构和功能。中温(35℃)水解酸化更利于COD去除(40.51%)和水质可生化性提高(BOD_(5)/COD提高至0.53),而低温(15℃)COD去除率和BOD_(5)/COD仅为20.96%和0.26。中温条件有助于难降解化合物(O_(3)S_(1)和O_(4)S_(1))的水解转化,与低温水解酸化相比,中温条件能够产生更多种类的小分子有机物。水解酸化微生物的宏基因组测序结果表明中温条件更利于微生物生长,有机物降解菌unclassified_p_Chloroflexi和可分泌水解酶的unclassified_o_Bacteroidales丰度较高。中温水解酸化富集了ko00643(苯乙烯降解)、ko00633(硝基甲苯降解)、ko00622(二甲苯降解)、ko00364(氟苯甲酸酯降解)、ko00642(乙苯降解)和ko00365(糠醛降解)等功能基因,促进了芳香类及含氮污染物的降解和出水可生化性能的提高。本研究揭示了炼化污水中低温水解酸化的水质变化及微生物特性。 展开更多
关键词 炼化污水 中低温水解酸化 有机物组成 宏基因组 厌氧 生物技术
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原位优势菌人工浮岛耦合生态基处理炼化黑臭水体中试研究
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作者 苏俊涛 张潇元 +2 位作者 韩松 于杰 刘东 《环境科学与管理》 CAS 2024年第8期163-168,共6页
纳污水体的整治成为炙手课题,但对东北高寒盐的纳污水体净化技术未完善。本研究以生态基为膜载体,利用其与芦苇人工浮岛、原位优势菌形成的耦合修复体系开展东北地区某炼化纳污水体净化效果研究。研究表明,当在温度25℃,溶氧浓度4 mg/L... 纳污水体的整治成为炙手课题,但对东北高寒盐的纳污水体净化技术未完善。本研究以生态基为膜载体,利用其与芦苇人工浮岛、原位优势菌形成的耦合修复体系开展东北地区某炼化纳污水体净化效果研究。研究表明,当在温度25℃,溶氧浓度4 mg/L,pH值8.0,以碳素纤维草为材料作为生态基,投放密度2根/浮岛单元的环境下时,该耦合系统对纳污上覆水体COD、NH_(4)^(+)-N、TN和TP平均去除率为最佳,可达到78.40%、79.18%、84.05%和79.76%。实现了炼化纳污水体的原位净化目标,提升了上覆水污染物的去除率,为该技术在炼化纳污上覆水体原位治理工程化应用中系统构建与运行提供理论基础。 展开更多
关键词 人工浮岛 原位修复 炼化黑臭水体 原位优势菌 生态基
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炼厂污水臭氧处理系统中奥氏体不锈钢的腐蚀行为
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作者 杨琰嘉 王雪峰 +4 位作者 宋延达 刘超 杜延年 张宏飞 段永锋 《工业水处理》 CAS CSCD 北大核心 2024年第11期122-131,共10页
臭氧催化氧化技术在炼厂污水处理领域的应用较为广泛,但装置在长周期运行过程中经常出现不同程度的腐蚀问题,尤其是奥氏体不锈钢的设备及管道。为了明确炼厂不锈钢设备及管道在含臭氧污水环境下的腐蚀特性,采用电化学试验和浸泡试验,以3... 臭氧催化氧化技术在炼厂污水处理领域的应用较为广泛,但装置在长周期运行过程中经常出现不同程度的腐蚀问题,尤其是奥氏体不锈钢的设备及管道。为了明确炼厂不锈钢设备及管道在含臭氧污水环境下的腐蚀特性,采用电化学试验和浸泡试验,以316L材质为主要研究对象,系统研究了其在含臭氧模拟污水环境中的腐蚀行为,并推测臭氧与Cl^(-)共同作用下不锈钢的腐蚀机制。结果表明:环境温度升高、pH偏离中性、臭氧浓度升高、Cl^(-)质量浓度升高、SO_(4)^(2-)质量浓度降低均会增大316L在污水环境中的点蚀敏感性,使其耐腐蚀性能下降;在焊接接头中,焊缝热影响区的点蚀敏感性相对较高;在含氯污水环境中臭氧与Cl^(-)存在协同腐蚀机制,会增大316L的点蚀敏感性和缝隙腐蚀敏感性,加速316L点蚀的发生。相比于304L和316L,317L在该环境中表现出更好的耐点蚀性能。 展开更多
关键词 炼厂污水 316L 腐蚀行为 臭氧 协同腐蚀
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气升式环流反应器在生化处理中的中试试验
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作者 吴振虎 顾镛 +1 位作者 袁方 杨强 《水处理技术》 CAS CSCD 北大核心 2024年第8期98-102,共5页
生化处理是炼油废水处理过程中的关键环节,目前的生化处理工艺以氧化塘、SBR为主,但好氧反应区域存在气液混合不均匀、发泡尺寸较大等问题,进而导致氧气利用率低、能耗高。为提高生化反应效率,缩短曝气时间,本文设计了气升式环流反应器(... 生化处理是炼油废水处理过程中的关键环节,目前的生化处理工艺以氧化塘、SBR为主,但好氧反应区域存在气液混合不均匀、发泡尺寸较大等问题,进而导致氧气利用率低、能耗高。为提高生化反应效率,缩短曝气时间,本文设计了气升式环流反应器(ALR),通过安装微细气泡曝气盘配合曝气环产生分形气泡以强化气-液-固三相传质和混合,将二级生化处理单元中的好氧反应区和沉淀区集成在同一个反应器内,并开展了中试试验。研究对比了ALR和SBR对气浮出水的处理效果,衡量了两者的技术经济性指标。试验结果表明:在ALR与SBR在油含量、COD和氨氮去除效果相当的情况下,ALR的污泥负荷提升了10倍,COD容积负荷提升了5倍;同时,ALR的吨水处理的鼓气量减少了57%,吨水处理占地面积仅为SBR的50%左右,吨水处理的能耗降低了22.9%,解决了传统生化处理工艺占地面积大、能耗高等问题,为未来生化反应器的升级改造提供了重要参考。 展开更多
关键词 生化处理 炼油废水 气升式环流反应器 SBR
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炼厂污水臭氧处理系统的腐蚀特性与选材研究
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作者 杨琰嘉 王雪峰 +4 位作者 宋延达 刘超 杜延年 张宏飞 段永锋 《压力容器》 北大核心 2024年第1期1-11,共11页
针对炼厂污水臭氧处理系统长周期运行过程中,设备及管道存在跑冒滴漏现象,尤其是在管道的焊缝热影响区腐蚀尤为严重的问题,采用电化学试验、模拟浸泡试验和现场腐蚀评价试验,研究臭氧浓度和氯离子浓度对腐蚀速率的影响,明确不同金属材... 针对炼厂污水臭氧处理系统长周期运行过程中,设备及管道存在跑冒滴漏现象,尤其是在管道的焊缝热影响区腐蚀尤为严重的问题,采用电化学试验、模拟浸泡试验和现场腐蚀评价试验,研究臭氧浓度和氯离子浓度对腐蚀速率的影响,明确不同金属材料在臭氧和污水环境中的耐蚀性能,并给出了推荐选材方案。结果表明,在炼厂高氯污水和臭氧环境中,022Cr17Ni12Mo2的点蚀敏感性与臭氧浓度和氯离子浓度呈正相关,且两因素之间存在协同腐蚀作用;Q245R,022Cr19Ni10,022Cr17Ni12Mo2材料在该环境下的耐蚀性能相对较差;022Cr19Ni13Mo3,015Cr21Ni26Mo5Cu2,022Cr23Ni5Mo3N,015Cr20Ni18Mo6CuN等材料则表现出良好的抗点蚀及缝隙腐蚀能力。建议炼厂污水臭氧处理系统主要设备和管道的选材以022Cr19Ni13Mo3为主。 展开更多
关键词 金属材料 炼厂污水 腐蚀 臭氧 氯离子 选材
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催化臭氧氧化技术在污水提质工程应用中的效果分析
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作者 李本高 《石油炼制与化工》 CAS CSCD 北大核心 2024年第11期106-110,共5页
分析评价催化臭氧氧化技术在污水三级(深度)处理领域的应用效果,对炼化企业污水提质技术的选择具有重要意义。对工业化运行的含油污水和含盐污水两套典型的非均相催化臭氧氧化装置进行现场调查、运行水质数据收集和取样分析,装置的进出... 分析评价催化臭氧氧化技术在污水三级(深度)处理领域的应用效果,对炼化企业污水提质技术的选择具有重要意义。对工业化运行的含油污水和含盐污水两套典型的非均相催化臭氧氧化装置进行现场调查、运行水质数据收集和取样分析,装置的进出水化学需氧量(COD)统计和分析结果表明:非均相催化臭氧氧化对含油污水和含盐污水COD具有一定的去除作用,但催化剂失活较快;运行一段时间后COD平均降低约10 mg L,与无催化的臭氧氧化效果相当,对改善生化需氧量(BOD)基本无效。 展开更多
关键词 炼化污水 深度处理 臭氧 催化氧化
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粉末活性炭改善MBBR处理效果的工程应用实例
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作者 桑军强 赵锐 +1 位作者 高峰 曹晓磊 《水处理技术》 CAS CSCD 北大核心 2024年第7期139-143,共5页
在某炼化企业高浓度污水处理系统的MBBR反应器中投加75 mg/L的粉末活性炭,从工程应用的角度考察了活性炭投加后MBBR的运行效果。工业装置运行结果表明,在MBBR系统的缺氧单元空床停留时间4 h、好氧MBBR反应器空床停留时间16 h、进水COD≤... 在某炼化企业高浓度污水处理系统的MBBR反应器中投加75 mg/L的粉末活性炭,从工程应用的角度考察了活性炭投加后MBBR的运行效果。工业装置运行结果表明,在MBBR系统的缺氧单元空床停留时间4 h、好氧MBBR反应器空床停留时间16 h、进水COD≤600 mg/L、氨氮≤40 mg/L、TN≤45 mg/L的运行条件下,MBBR系统保持了长期稳定运行,出水水质满足了设计要求。该工程实例表明,在MBBR装置中少量投加粉末活性炭,是提高在用MBBR装置运行稳定性和处理效果的一个简单、可行且有效的方法。 展开更多
关键词 MBBR 活性炭 炼化污水 生物膜 活性污泥
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蓄热式氧化炉在炼油污水处理厂中的应用
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作者 黄代存 《化工环保》 CAS CSCD 北大核心 2024年第4期589-594,共6页
采用蓄热式氧化炉技术高效处理炼油污水处理厂VOCs。介绍了蓄热式氧化炉的应用流程、工艺设计和运行情况。实验结果表明:在蓄热式氧化炉入口气体浓度为甲烷爆炸下限的6.5%~7.0%、炉膛温度为800~820℃的条件下,装置运行效果较好,处理后... 采用蓄热式氧化炉技术高效处理炼油污水处理厂VOCs。介绍了蓄热式氧化炉的应用流程、工艺设计和运行情况。实验结果表明:在蓄热式氧化炉入口气体浓度为甲烷爆炸下限的6.5%~7.0%、炉膛温度为800~820℃的条件下,装置运行效果较好,处理后烟气排放非甲烷总烃、苯、甲苯、二甲苯的平均质量浓度分别为5.28,0.09,0.20,0.02 mg/m^(3),远低于国家排放标准。蓄热式氧化炉具有热效率和净化率高、操作安全可靠、维护工作量少等特点,是炼油污水处理厂VOCs治理的有效途径。 展开更多
关键词 蓄热式氧化炉 VOCs治理 炼油污水处理
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炼油厂电脱盐废水催化氧化喷淋塔用催化剂负载方法的实验研究
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作者 姜宝安 《化工设计通讯》 CAS 2024年第5期59-60,66,共3页
实验研究了一种炼油厂电脱盐废水催化氧化喷淋塔用催化剂的负载方法,将一定形状的塑料填料加热,填料表面热熔后,与催化剂共混搅拌,催化剂黏附于塑料填料表面,填料冷却后,催化剂能牢固地附着于塑料填料表面。将此塑料填料填于催化氧化塔... 实验研究了一种炼油厂电脱盐废水催化氧化喷淋塔用催化剂的负载方法,将一定形状的塑料填料加热,填料表面热熔后,与催化剂共混搅拌,催化剂黏附于塑料填料表面,填料冷却后,催化剂能牢固地附着于塑料填料表面。将此塑料填料填于催化氧化塔内的支撑格栅上形成填料层,参与催化氧化反应。该结构形式降低了传统催化剂层的阻力降,改善了喷淋塔中的气液分布条件。 展开更多
关键词 炼油 电脱盐废水 催化氧化 催化剂 喷淋塔 填料
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Waveband Selection with Equivalent Prediction Performance for FTIR/ATR Spectroscopic Analysis of COD in Sugar Refinery Waste Water 被引量:1
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作者 Jun Xie Dapeng Sun +1 位作者 Jiaxiang Cai Fuhong Cai 《Computers, Materials & Continua》 SCIE EI 2019年第5期687-695,共9页
The level of chemical oxygen demand(COD)is an important index to evaluate whether sewage meets the discharge requirements,so corresponding tests should be carried out before discharge.Fourier transform infrared spectr... The level of chemical oxygen demand(COD)is an important index to evaluate whether sewage meets the discharge requirements,so corresponding tests should be carried out before discharge.Fourier transform infrared spectroscopy(FTIR)and attenuated total reflectance(ATR)can detect COD in sewage effectively,which has advantages over conventional chemical analysis methods.And the selection of characteristic bands was one of the key links in the application of FTIR/ATR spectroscopy.In this work,based on the moving window partial least-squares(MWPLS)regression to select a characteristic wavelength,a method of equivalent wavelength selection was proposed combining with paired t-test equivalent concept.The results showed that the prediction effect of the selected wavelength was very close to that of the MWPLS method,while the number of wavelength points was much smaller.SEPAve,RP,Ave,SEPStd,and RP,Std which characterized the modeling effect were 26.3 mg L^-1,0.969,3.49 mg L^-1,and 0.006,respectively.The validation effect V-SEP and V-RP were 28.64 mg L^-1 and 0.960,respectively.The selected waveband was between 1809 cm^-1 and 1568 cm^-1.The method was of more reference value for the design of FTIR/ATR spectral instrument for COD detection. 展开更多
关键词 Sugar refinery wastewater COD FTIR/ATR spectroscopy waveband selection
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Selecting Suitable Heat Source in Refinery for Multi-effect Distillation Based on Grey System Theory 被引量:1
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作者 Xue Jianliang Zhao Dongfeng +3 位作者 Li Shi Liu Wei Shen Chanchan Chen Lu 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2013年第1期66-72,共7页
For dealing with high-salinity wastewater in the refinery, the high cost of driving heat source is the disadvantage of multi-effect distillation (MED) so it is of great importance to evaluate the performance of low-te... For dealing with high-salinity wastewater in the refinery, the high cost of driving heat source is the disadvantage of multi-effect distillation (MED) so it is of great importance to evaluate the performance of low-temperature heat source for conducting MED and select the optimal temperature for it. Both the MED and the low-temperature heat sources studied in this paper were from a typical refinery located in northwestern China. Besides, a new methodology to evaluate heat sources as the optimal candidate was proposed for MED based on the grey system theory. Five process units, which included 18 fluids of the refinery, were named as the evaluation projects. Three factors, which included safety effects, total costs and characteristics of low-temperature heat sources were determined as the evaluation indexes, the values of which were established through the analyses. The results obtained through the grey correlation analyses have revealed that the grey correlation degrees of these units were 0.661(AVDU), 0.732 (#1 FCCU), 0.618 (#2 FCCU), 0.535 (#1 DCU), and 0.572 (#2 DCU), respectively. Thus, the optimal heat source was provided from #1 FCCU. Through further analyses of the fluids from #1 FCCU, the grey correlation degrees of the fluids were 0.597 (oil and gas at top of tower), 0.714 (recycle oil and gas), and 0.512 (diesel), respectively. Thus, the optimal heat source was the oil and gas recycle stream. 展开更多
关键词 multi-effect distillation grey system theory heat recovery high-salinity wastewater refinery
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Cu/γ-Al_(2)O_(3)催化剂催化臭氧氧化处理炼油污水 被引量:3
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作者 龚小芝 《化工环保》 CAS CSCD 北大核心 2023年第3期404-408,共5页
以γ-Al_(2)O_(3)为载体,通过浸渍法制备了Cu/γ-Al_(2)O_(3)臭氧氧化催化剂。物化性能测试结果表明,催化剂比表面积为304.8 m^(2)/g,孔径为5~10 nm,抗压碎力大于100 N,该催化剂可耐受短期酸性废水冲击,并具有一定的抗结垢性。将该催化... 以γ-Al_(2)O_(3)为载体,通过浸渍法制备了Cu/γ-Al_(2)O_(3)臭氧氧化催化剂。物化性能测试结果表明,催化剂比表面积为304.8 m^(2)/g,孔径为5~10 nm,抗压碎力大于100 N,该催化剂可耐受短期酸性废水冲击,并具有一定的抗结垢性。将该催化剂用于臭氧氧化工艺与曝气生物滤池结合处理炼油污水生化出水。催化剂对臭氧氧化降解炼油污水生化出水COD催化效果良好,同时废水可生化性显著提高,利于后续曝气生物滤池深度去除COD。在进水COD为40~154 mg/L的条件下,出水COD稳定在20~40 mg/L,实现了耐冲击稳定运行。 展开更多
关键词 臭氧氧化 催化剂 炼油污水 曝气生物滤池 深度处理
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