膜蒸馏处理页岩气井压裂返排液

刘宇程, 吴东海, 袁建梅, 陈菊, 张波. 膜蒸馏处理页岩气井压裂返排液[J]. 环境工程学报, 2017, 11(1): 48-54. doi: 10.12030/j.cjee.201509096
引用本文: 刘宇程, 吴东海, 袁建梅, 陈菊, 张波. 膜蒸馏处理页岩气井压裂返排液[J]. 环境工程学报, 2017, 11(1): 48-54. doi: 10.12030/j.cjee.201509096
LIU Yucheng, WU Donghai, YUAN Jianmei, CHEN Ju, ZHANG Bo. Treatment of fracturing flowback fluids of shale gas wells by membrane distillation[J]. Chinese Journal of Environmental Engineering, 2017, 11(1): 48-54. doi: 10.12030/j.cjee.201509096
Citation: LIU Yucheng, WU Donghai, YUAN Jianmei, CHEN Ju, ZHANG Bo. Treatment of fracturing flowback fluids of shale gas wells by membrane distillation[J]. Chinese Journal of Environmental Engineering, 2017, 11(1): 48-54. doi: 10.12030/j.cjee.201509096

膜蒸馏处理页岩气井压裂返排液

  • 基金项目:

    国家自然科学基金资助项目(51104126)

  • 中图分类号: X741

Treatment of fracturing flowback fluids of shale gas wells by membrane distillation

  • Fund Project:
  • 摘要: 页岩气压裂返排液的有效处理是页岩气开发急需解决的关键环保问题之一。针对新页HF-1井页岩气压裂返排液经预氧化结合湿式氧化(PO-WAO)工艺处理的出水COD不达标、含盐量高等技术难题,采用膜蒸馏处理技术对工艺的出水进行深度处理。通过膜蒸馏单因素和正交实验表明料液温度和冷凝温度对膜蒸馏处理效果影响较大,在料液温度、冷凝液温度、真空度、运行时间分别为80℃、8℃、0.090 MPa和60 min的最佳工艺条件下,膜通量可达1.750 L·(m2·h)-1,出水COD浓度为95.8 mg·L-1,出水水质可满足《污水综合排放标准》(GB 8978-1996)中一级排放的要求。膜蒸馏出水中电导率为63 μS·cm-1,氯化钠的质量浓度为1.168 0 mg·L-1,可有效降低处理后的压裂废液对周围土壤的盐碱化伤害。
  • 加载中
  • [1] U. S. Energy Information Administration. World Shale Gas Resources:An Initial Assessment of 14 Regions Outside the United States[R]. Washington:EIA, 2011
    [2] Ground Water Protection Council, ALL Consulting. Modern Shale Gas Development in the United States:A Primer[R]. Washington, D. C.:United States Department of Energy, Office of Fossil Energy, 2009:96
    [3] RAHM D. Regulating hydraulic fracturing in shale gas plays:The case of Texas[J]. Energy Policy, 2011, 39(5):2974-2981
    [4] GREGORY K B, VIDIC R D, DZOMBAK D A. Water management challenges associated with the production of shale gas by hydraulic fracturing[J]. Elements, 2011, 7(3):181-186
    [5] VIDIC R D, BRANTLEY S L, VANDENBOSSCHE J M, et al. Impact of shale gas development on regional water quality[J]. Science, 2013, 340(6134):1235009
    [6] LUTZ B D, LEWIS A N, DOYLE M W. Generation, transport, and disposal of wastewater associated with Marcellus Shale gas development[J]. Water Resources Research, 2013, 49(2):647-656
    [7] JIANG Qiying, RENTSCHLER J, PERRONE R, et al. Application of ceramic membrane and ion-exchange for the treatment of the flowback water from Marcellus shale gas production[J]. Journal of Membrane Science, 2013, 431:55-61
    [8] CATH T Y, CHILDRESS A E, ELIMELECH M. Forward osmosis:Principles, applications, and recent developments[J]. Journal of Membrane Science, 2006, 281(1/2):70-87
    [9] GE Qingchun, SU Jincai, AMY G L, et al. Exploration of polyelectrolytes as draw solutes in forward osmosis processes[J]. Water Research, 2012, 46(4):1318-1326
    [10] HOLLOWAY R W, CHILDRESS A E, DENNETT K E, et al. Forward osmosis for concentration of anaerobic digester centrate[J]. Water Research, 2007, 41(17):4005-4014
    [11] DEBELLEFONTAINE H, FOUSSARD J N. Wet air oxidation for the treatment of industrial wastes. Chemical aspects, reactor design and industrial applications in Europe[J]. Waste Management, 2000, 20(1):15-25
    [12] LUCK F. Wet air oxidation:Past, present and future[J]. Catalysis Today, 1999, 53(1):81-91
    [13] AL-OBAIDANI S, CURCIO E, MACEDONIO F, et al. Potential of membrane distillation in seawater desalination:Thermal efficiency, sensitivity study and cost estimation[J]. Journal of Membrane Science, 2008, 323(1):85-98
    [14] ALKHUDHIRI A, DARWISH N, HILAL N. Membrane distillation:A comprehensive review[J]. Desalination, 2012, 287:2-18
    [15] CURCIO E, DRIOLI E. Membrane distillation and related operations:A review[J]. Separation & Purification Reviews, 2005, 34(1):35-86
    [16] LAWSON K W, LLOYD D R. Membrane distillation[J]. Journal of Membrane Science, 1997, 124(1):1-25
    [17] 张亚静, 吴雪妹. 膜蒸馏技术的应用和发展[J]. 过滤与分离, 2001, 22(2):16-19
    [18] 张建芳. 减压膜蒸馏淡化高盐废水的研究[D]. 乌鲁木齐:新疆大学, 2005
    [19] 杨兰, 丁忠伟, 马润宇. 温度极化对膜蒸馏过程的影响研究[J]. 膜科学与技术, 2004, 24(3):4-9
    [20] 游文婷. 真空膜蒸馏-结晶耦合过程处理模拟高含铵盐废水的研究[D]. 上海:华东理工大学, 2014
  • 加载中
计量
  • 文章访问数:  2948
  • HTML全文浏览数:  2526
  • PDF下载数:  485
  • 施引文献:  0
出版历程
  • 收稿日期:  2015-10-15
  • 刊出日期:  2017-01-05
刘宇程, 吴东海, 袁建梅, 陈菊, 张波. 膜蒸馏处理页岩气井压裂返排液[J]. 环境工程学报, 2017, 11(1): 48-54. doi: 10.12030/j.cjee.201509096
引用本文: 刘宇程, 吴东海, 袁建梅, 陈菊, 张波. 膜蒸馏处理页岩气井压裂返排液[J]. 环境工程学报, 2017, 11(1): 48-54. doi: 10.12030/j.cjee.201509096
LIU Yucheng, WU Donghai, YUAN Jianmei, CHEN Ju, ZHANG Bo. Treatment of fracturing flowback fluids of shale gas wells by membrane distillation[J]. Chinese Journal of Environmental Engineering, 2017, 11(1): 48-54. doi: 10.12030/j.cjee.201509096
Citation: LIU Yucheng, WU Donghai, YUAN Jianmei, CHEN Ju, ZHANG Bo. Treatment of fracturing flowback fluids of shale gas wells by membrane distillation[J]. Chinese Journal of Environmental Engineering, 2017, 11(1): 48-54. doi: 10.12030/j.cjee.201509096

膜蒸馏处理页岩气井压裂返排液

  • 1. 西南石油大学化学化工学院, 成都, 610500
基金项目:

国家自然科学基金资助项目(51104126)

摘要: 页岩气压裂返排液的有效处理是页岩气开发急需解决的关键环保问题之一。针对新页HF-1井页岩气压裂返排液经预氧化结合湿式氧化(PO-WAO)工艺处理的出水COD不达标、含盐量高等技术难题,采用膜蒸馏处理技术对工艺的出水进行深度处理。通过膜蒸馏单因素和正交实验表明料液温度和冷凝温度对膜蒸馏处理效果影响较大,在料液温度、冷凝液温度、真空度、运行时间分别为80℃、8℃、0.090 MPa和60 min的最佳工艺条件下,膜通量可达1.750 L·(m2·h)-1,出水COD浓度为95.8 mg·L-1,出水水质可满足《污水综合排放标准》(GB 8978-1996)中一级排放的要求。膜蒸馏出水中电导率为63 μS·cm-1,氯化钠的质量浓度为1.168 0 mg·L-1,可有效降低处理后的压裂废液对周围土壤的盐碱化伤害。

English Abstract

参考文献 (20)

返回顶部

目录

/

返回文章
返回