Disposal testing characteristics of highly emulsified oily wastewater based on dialysis membranes
-
摘要:
目的 超滤技术处理含油废水在工程中得到广泛应用,为了研究基于亲水透析膜的高乳化油污水分离特性, 方法 利用1000号矿油型汽缸油(GB/T 447-1994) 及乳化剂等制备高乳化油污水,搭建小型高乳化油污水分离试验装置,利用流量计、油份检测仪等仪器设备测量不同孔径透析膜组件处理不同温度、不同浓度高乳化油污水原液的效能,并按MEPC.107(49) 决议研究膜组件的抗污性能,以及膜组件频繁自清洗后处理效能的衰减特性。 结果 试验发现0.1~0.45 μm孔径透析膜随着孔径的增加,其处理能力随之增加;且3种膜具有相似的温度-流量特性,即随着温度的增加处理能力先增后减,其中0.45 μm的透析膜在处理55~60℃原液时效能最佳。 结论 研究中形成的各类特性数据对于高乳化油污分离装置的设计、使用操作具有工程指导意义。 Abstract: Ultrafiltration technology is widely applied in the treatment of ship's oily wastewater. In order to study the disposal testing characteristics of highly emulsified oily wastewater based on hydrophilic dialysis membranes, No.1000 cylinder oil and emulsifier is used to make highly emulsified oily wastewater, and a small oil/waster separating tester is created. The relationships between the temperature, consistency of original highly emulsified oily wastewater and dialysis membrane aperture are tested. Not only is the pollution resistance of the dialysis membrane tested on the basis of resolution MEPC.107(49), but the attenuation characteristic of the dialysis membrane is also tested after self-cleaning each time. All the tests show that for dialysis membranes with in the range 0.1 μm to 0.45 μm, the treatment capability will increase with the aperture; they all show a similar flow vs temperature curve, with the treatment capability first increasing and then decreasing with the increasing temperature; when the aperture of the dialysis membrane reaches 0.45 μm, the separation of highly emulsified oily wastewater is best achieved at 55-60℃. All the data and characteristics of this research will be helpful in the design and operation of highly emulsified oily wastewater disposal equipment.-
Key words:
- cylinder oil /
- dialysis membrane /
- highly emulsified oil /
- emulsion concentration
-
表 1 试验仪器仪表
Table 1. Test instruments
名称 主要参数 数量/台 流量计 0~1.0 m3/h,精度0.5级 2 压力表 0~1.0 MPa,精度2.5级 4 温度计 0~100 ℃,精度2.5级 1 油份检测仪 体积分数0~200×10-6 1 乳化油检测仪 体积分数0~50 000×10-6 1 -
[1] 中国船级社. 经1978年议定书修订的 < 1973年国际防止船舶造成污染公约 > [S]. 北京: 人民交通出版社, 2003. [2] 杨顺成, 张康, 倪海, 等. 1000号汽缸油蒸汽乳化油水分离方法研究[J].化学工程师, 2012(7):58-62. http://www.cnki.com.cn/Article/CJFDTOTAL-HXGC201207020.htmYANG S C, ZHANG K, NI H, et al. Researches on disposal method of wastewater from No.1000 cylinder oil emulsified by high-temperatured steam[J]. Chemi-cal Engineer, 2012(7):58-62(in Chinese). http://www.cnki.com.cn/Article/CJFDTOTAL-HXGC201207020.htm [3] 王兰娟, 张才菁.含乳化油污水的超滤膜分离模型[J].石油大学学报(自然科学版), 1998, 22(3):79-81. http://www.cnki.com.cn/Article/CJFDTOTAL-SYDX803.018.htmWANG L J, ZHANG C J. Ultrafiltration model for treat-ing wastewater containing oil[J]. Journal of the Univer-sity of Petroleum(Natural Science), 1998, 22(3):79-81(in Chinese). http://www.cnki.com.cn/Article/CJFDTOTAL-SYDX803.018.htm [4] 刘万鹤, 张英华.符合MEPC.107(49) 决议要求的两种新型油水分离器[J].航海技术, 2012(5):49-51. http://www.cnki.com.cn/Article/CJFDTOTAL-HHJS201205024.htmLIU W H, ZHANG Y H. Two new oily water separator meeting the decision of MEPC.107(49)[J]. Marine Technology, 2012(5):49-51(in Chinese). http://www.cnki.com.cn/Article/CJFDTOTAL-HHJS201205024.htm [5] COLIC M, ZHANG Y H. Novel pretreatment enables performance of MBR installed to treat oily wastewater[C]//Proceedings of 2010 the Water Environment Fed-eration.[S.l.]:Water Environment Federation, 2010:4049-4055. [6] ABBASI M, MIRFENDERESKI M, NIKBAKHT M, et al. Performance study of mullite and mullite-alumi-na ceramic MF membranes for oily wastewaters treat-ment[J]. Desalination, 2010, 259(1/3):169-178. [7] 刘喜元, 李树, 谢承利, 等. MBR运行参数对处理船舶含油餐饮废水的影响[J].中国舰船研究, 2016, 11(2):133-138. http://www.ship-research.com/CN/abstract/abstract1538.shtmlLIU X Y, LI S, XIE C L, et al. Effects of operating pa-rameters of MBR on the treatment of ship's restaurant oily wastewater[J]. Chinese Journal of Ship Research, 2016, 11(2):133-138(in Chinese). http://www.ship-research.com/CN/abstract/abstract1538.shtml [8] 承雪航. 含乳化油冷轧废水处理的试验研究[D]. 上海: 上海交通大学, 2009: 3-10.CHENG X H. Study on the treatment of cold rolling mill wastewater containing emulsion[D]. Shanghai:Shanghai Jiao Tong University, 2009:3-10(in Chi-nese). [9] 王元波.离心分离技术在重污油处理中的应用[J].石油化工环境保护, 2006, 29(3):46-47, 61. http://www.cnki.com.cn/Article/CJFDTOTAL-SYHB200603015.htmWANG Y B. Application of centrifugal separation tech-nology to heavy sump oil treatment[J]. Environmental Protection in Petrochemical Industry, 2006, 29(3):46-47, 61(in Chinese). http://www.cnki.com.cn/Article/CJFDTOTAL-SYHB200603015.htm [10] 吴凯凯, 梁光川, 马培红, 等.聚醚型稠油破乳剂破乳效果影响因素分析[J].天然气与石油, 2010, 28(2):12-14. http://www.cnki.com.cn/Article/CJFDTOTAL-TRYS201002007.htmWU K K, LIANG G C, MA P H, et al. Analysis on demulsification influence factor of polyether-type heavy oil demulsifying agent[J]. Natural Gas and Oil, 2010, 28(2):12-14(in Chinese). http://www.cnki.com.cn/Article/CJFDTOTAL-TRYS201002007.htm [11] 叶晓, 谢飞, 罗孝曦, 等.聚合物膜材料在油水分离过程中的应用[J].化工进展, 2012, 31(增刊2):163-166. http://www.cnki.com.cn/Article/CJFDTOTAL-HGJZ2012S2038.htmYE X, XIE F, LUO X X, et al. Application of poly-mer membrane materials for oil/water separation[J]. Chemical Industry and Engineering Progress, 2012, 31(Supp 2):163-166(in Chinese). http://www.cnki.com.cn/Article/CJFDTOTAL-HGJZ2012S2038.htm [12] 肖丙雁, 阮红权, 刘捷涛.应用膜生物反应器处理冷轧含油废水[J].环境科学与管理, 2007, 32(12):95-96, 142. doi: 10.3969/j.issn.1673-1212.2007.12.029XIAO B Y, RUAN H Q, LIU J T, et al. Application of membrane bioreactor in cold-rolling oily waster wa-ter[J]. Environmental Science and Management, 2007, 32(12):95-96, 142(in Chinese). doi: 10.3969/j.issn.1673-1212.2007.12.029 -