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生物接触氧化塔在炼油污水回用中的应用 总被引:5,自引:0,他引:5
生物接触氧化塔在炼油污水回用中的试验表明,该处理设施具有抗冲击能力强、水力停留时间短、无回流污泥、占地面积小、结构简单、效果稳定等特点,对污水中COD、BOD、氨氮、总磷等污染物具有很高的去除率,最终出水可满足循环冷却水要求。 相似文献
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大庆石化公司炼油厂工业用水主要用于循环水补水、制取化学水、机泵压缩机冷却用水、消防用水、生活洗涤用水、施工用水和部分转供水。其用水大户为循环水补水和制取化学水,其中消耗量占炼油厂工业总水量70%-85%。到2008年底,炼油厂凝结水回收率为66.71%,循环水浓缩倍数为3.52,实现吨油耗水0.92t的历史最好水平,距股份公司要求0.75t相差0.17t。虽然还有进一步提高的空间,但受炼油厂地理位置及工艺流程和产品结构限制,需要高额的投资费用。 相似文献
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炼油污水臭氧氧化-生物炭深度处理水质回用资源化 总被引:4,自引:1,他引:4
设计了臭氧氧化-生物活性炭深度处理装置,对经二级生化处理达标后的炼油污水,再经臭氧-生物炭工艺进行深度处理使水质主要指标达到地表水Ⅲ~Ⅳ类水标准:COD≤13mg·L-1;BOD5≤3.6mg·L-1;石油类≤0.46 mg·L-1;挥发酚≤0.00017 mg·L-1;NH3-N≤0.9 mg·L-1,循回用于工业生产,实现炼油污水资源化,并对臭氧提高有机废水可生化性和生物活性炭的工艺条件进行探讨. 相似文献
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设计了臭氧氧化-生物活性炭深度处理装置,对经二级生化处理达标后的炼油污水,再经臭氧.生物炭工艺进行深度处理使水质主要指标达到地表水Ⅲ~Ⅳ类水标准:COD≤13mg·L^-1;BOD5≤3.6mg·L^-1;石油类≤0.46mg·L^-1;挥发酚≤0.00017mg·L^-1;NH3-N≤0.9mg·L^-1,循回用于工业生产,实现炼油污水资源化,并对臭氧提高有机废水可生化性和生物活性炭的工艺条件进行探讨。 相似文献
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炼油污水的回用技术研究 总被引:3,自引:0,他引:3
提出一个经济合理的炼油污水回用处理工艺“浮选一生物过滤一臭氧催化氧化一高效过滤”,对抚顺石化公司石油一厂水净化车间生化二沉池出水进行了中试处理试验。研究结果表明,出水的主要几项污染指标COD、油、浊度有明显的降低,可达到工业用水的要求。其中COD由原水的70~180mg/L降到15mg/L以下,油质量分数由原水的2.5~5.6mg/L降到0.5mg/L以下,浊度由原水的24~33mg/L降到0.5mg/L左右,总铁离子由原水的1.5mg/L降到0.3mg/L以下,总磷由原水的1~1.5mg/L降到0.5mg/L以下,试验效果比较理想。 相似文献
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介绍了食用油瓶用聚酯切片的品质指标,特殊要求及存在的问题。阐述了生产食用油瓶用聚酯切片的方法,即:调整工艺、加入共聚第三组分IPA、控制添加剂的用量等。提供了一种改性聚酯的新生产工艺。 相似文献
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Abdelhamid Boukerroui Mohand‐Said Ouali 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2000,75(9):773-776
A spent bleaching earth from an edible oil refinery has been regenerated by thermal processing followed by washing with a solution of hydrochloric acid. Optimal regeneration conditions have been controlled by decolorization tests of a degummed and neutralized crude edible oil. Optimal values (temperature: 500 °C, carbonization time: 1 h, HCl concentration: 1 M ) gave a material as efficient as a virgin bleaching earth. The percentage uptake of chlorophyll derivatives and β‐carotenoids calculated at 410 and 460 nm, are respectively 92.8 and 95% for an oil processed by the regenerated spent bleaching earth, against 77.4 and 92.7% for the same oil processed by a commercial virgin bleaching earth. The results obtained after decolorization of an edible oil with a regenerated spent bleaching earth indicate that during the process, the resultant oil did not undergo any changes in the iodine value, the free fatty acid content and the saponification value. © 2000 Society of Chemical Industry 相似文献
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介绍了预处理-复合厌氧-生物接触氧化工艺处理油脂工业废水的设计和运行调试工程实例.运行结果表明,以复合厌氧-生物接触氧化为主体的工艺处理高浓度的油脂加工废水是适宜的,该工艺处理负荷高、运行稳定,在进水COD、BOD5、SS和油类分别为32471.0~41674.5 mg/L、12 751.0~16 138.3 mg/L、3496.9~9 502.3 mg/L和271.6~592.3 mg/L情况下,出水COD为76.9~86.0 mg/L、BOD5 18.0~21.3 mg/L、SS 26.0~52.0 mg/L、油类1.05~4.96 mg/L,达到了设计要求. 相似文献
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利用Anton Paar MCR301旋转流变仪开展了不同区块稠油粘温性的实验研究,在20~300℃,利用HA-Ⅱ型比热容测定装置及HA-Ⅱ型导热测定装置,测定了岩石、水和不同区块稠油的比热容及不同区块稠油的导热系数.研究结果表明,稠油的粘度对温度非常敏感,随温度升高而大幅度降低.在20~300℃,稠油的比热容值在1.6840~4.4939 J/(g·K)变化,变化范围较大.稠油的导热系数都有随着温度的升高而降低的规律,并且在数值上较为接近,在20~300℃,导热系数在0.1196~0.1650W/(m·K)变化,变化范围很小. 相似文献
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The use of coal liquefaction catalysts for coal/oil coprocessing and heavy oil upgrading 总被引:2,自引:0,他引:2
A. V. Cugini K. S. Rothenberger D. Krastman M. V. Ciocco R. L. Thompson C. McCreary T. J. Gardner 《Catalysis Today》1998,43(3-4):291-303
The catalytic hydrogenation of heavy oil and mixed coal-heavy oil (coprocessing) systems has been the focus of a recent study at the Federal Energy Technology Center (FETC). The intent of this effort was to extend the use of coal liquefaction technologies to heavy oil upgrading and coprocessing systems. Specifically, new dispersed molybdenum-based catalysts developed at FETC and a novel silica-doped hydrous titanium oxide (HTO : Si)-supported NiMo catalyst developed at Sandia National Laboratories (SNL) were tested in these systems. The results indicate the potential of coal liquefaction catalysts for use in coprocessing and heavy oil upgrading. High conversions of coal–oil mixtures were observed with dispersed catalyst loadings as low as 100 ppm Mo. Similar results were observed in heavy oil systems. Also, the novel NiMo/HTO : Si catalyst was at least as effective as commercially-available supported catalysts (e.g. Amocat 1C) for conversion of high boiling point material to distillable products and aromatics removal. 相似文献
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在PVDF/PVP体系中添加Al2O3和TiO2两种无机纳米颗粒,利用沉浸凝胶相转化法制得纳米颗粒总量不同和比例不同的改性PVDF平板超滤膜。探讨了纳米颗粒比例和总量对膜性能的影响。利用SEM、XRD对改性膜的结构进行了表征。并利用该改性膜处理典型沿海油库含油污水。结果显示:两种无机纳米颗粒的加入,明显增强了纳米改性膜的亲水性,使膜的抗污染性能得到提高;膜的韧性和强度得到改进;膜表面及膜孔的微观结构、改性膜的结晶度没有受到无机纳米颗粒的明显影响。最佳的纳米颗粒总含量为3%,两种纳米颗粒最佳质量比例为1:2。采用改性膜处理油库含油污水,稳定时出水中悬浮物含量低于0.4 mg·L-1;石油烃类含量低于0.5 mg·L-1;COD值在60~70 mg·L-1之间,达到了国家污水排放标准。 相似文献
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Sajid Husain M. Kifayatullah G. S. R. Sastry N. Prasada Raju 《Journal of the American Oil Chemists' Society》1993,70(12):1251-1254
Application of13C nuclear magnetic resonance (NMR) spectroscopy for detection of castor oil (CO) in various edible oils, such as coconut oil,
palm oil, groundnut oil and mustard oil, is described. Characteristic signals observed at δ 132.4, δ 125.6, δ 71.3, δ 36.8
and δ 35.4 ppm, due to C10, C9, C12, C13 and C11 carbons of ricinoleic acid (RA) in CO, were selected for distinguishing it
from edible oils. Quantitative13C NMR spectra of oils were recorded in CDCl3 with a gated decoupling technique. The minimum detection limits for qualitative and quantitative analyses were 2.0 and 3.0%,
respectively. The proposed method is simple, nondestructive and requires no sample pretreatment. Its application to heat-abused
oils has also been demonstrated successfully without any of the interferences observed in most other methods. 相似文献