Simultaneous recovery of phosphorus and nitrogen from liquid digestate by vacuum membrane distillation with permeate fractional condensation

doi:10.1016/j.cjche.2020.01.019

中国化学工程学报 ›› 2020, Vol. 28 ›› Issue (6): 1558-1565.DOI: 10.1016/j.cjche.2020.01.019

• Separation Science and Engineering • 上一篇下一篇

Simultaneous recovery of phosphorus and nitrogen from liquid digestate by vacuum membrane distillation with permeate fractional condensation

Boya Qiu¹, Senqing Fan¹, Xiaoyu Tang², Bufan Qi³, Liangwei Deng², Wenguo Wang^2,4, Jingyun Liu¹, Yuyang Wang¹, Zeyi Xiao¹

1 School of Chemical Engineering, Sichuan University, Chengdu 610065, China;
2 Biogas Institute of Ministry of Agriculture and Rural Affairs, Chengdu 610041, China;
3 College of Pharmacy and Biological Engineering, Chengdu University, Chengdu 610106, China;
4 Key Laboratory of Development and Application of Rural Renewable Energy, Ministry of Agriculture and Rural Affairs, Chengdu 610041, China

收稿日期:2019-09-02 修回日期:2019-12-23 出版日期:2020-06-28 发布日期:2020-07-29
通讯作者: Senqing Fan, Wenguo Wang
基金资助:
The present work is supported by the Fundamental Research Funds for the Central Universities (No. 20822041B4013) and Key Laboratory of Development and Application of Rural Renewable Energy, Ministry of Agriculture and Rural Affairs, China (No. 18H0491).

Simultaneous recovery of phosphorus and nitrogen from liquid digestate by vacuum membrane distillation with permeate fractional condensation

Boya Qiu¹, Senqing Fan¹, Xiaoyu Tang², Bufan Qi³, Liangwei Deng², Wenguo Wang^2,4, Jingyun Liu¹, Yuyang Wang¹, Zeyi Xiao¹

1 School of Chemical Engineering, Sichuan University, Chengdu 610065, China;
2 Biogas Institute of Ministry of Agriculture and Rural Affairs, Chengdu 610041, China;
3 College of Pharmacy and Biological Engineering, Chengdu University, Chengdu 610106, China;
4 Key Laboratory of Development and Application of Rural Renewable Energy, Ministry of Agriculture and Rural Affairs, Chengdu 610041, China

Received:2019-09-02 Revised:2019-12-23 Online:2020-06-28 Published:2020-07-29
Contact: Senqing Fan, Wenguo Wang
Supported by:
The present work is supported by the Fundamental Research Funds for the Central Universities (No. 20822041B4013) and Key Laboratory of Development and Application of Rural Renewable Energy, Ministry of Agriculture and Rural Affairs, China (No. 18H0491).

摘要/Abstract

摘要： A vacuum membrane distillation (VMD) process with permeate fractional condensation on membrane downstream has been developed for simultaneous recovery of phosphorus and nitrogen from liquid digestate. The polytetrafluoroethylene (PTFE) membrane flux could reach 6000 g·m^-2·h^-1 with the rejection efficiency of total phosphorus (TP) over 0.99, under the condition of flowrate being 120 L·h^-1 and temperature being 40℃. Membrane fouling occurred with a film of organics and microorganism deposited on the surface of the membrane. Membrane flux could be reversed after the membrane was rinsed by water. Higher feed temperature and flowrate could improve the membrane flux, while hardly affect the rejection efficiency of total phosphorus. The concentration of TP could reach 1600 mg·L^-1 after membrane distillation, which is about 5 times of that in initial liquid digestate. On the downstream of the membrane, some of the permeate vapor was condensed under the vacuum condition and most of water was collected here. The remaining vapor enriched with total nitrogen (TN) was compressed and pumped to the atmospheric condition to condense. The TN concentration in atmospheric condensate was as high as 7000 mg·L^-1 with the process separation factor for ammonia being enhanced to 114.

关键词: Liquid digestate, Resource recovery, Vacuum membrane distillation, Permeate fractional condensation, Enhanced separation factor

Abstract: A vacuum membrane distillation (VMD) process with permeate fractional condensation on membrane downstream has been developed for simultaneous recovery of phosphorus and nitrogen from liquid digestate. The polytetrafluoroethylene (PTFE) membrane flux could reach 6000 g·m^-2·h^-1 with the rejection efficiency of total phosphorus (TP) over 0.99, under the condition of flowrate being 120 L·h^-1 and temperature being 40℃. Membrane fouling occurred with a film of organics and microorganism deposited on the surface of the membrane. Membrane flux could be reversed after the membrane was rinsed by water. Higher feed temperature and flowrate could improve the membrane flux, while hardly affect the rejection efficiency of total phosphorus. The concentration of TP could reach 1600 mg·L^-1 after membrane distillation, which is about 5 times of that in initial liquid digestate. On the downstream of the membrane, some of the permeate vapor was condensed under the vacuum condition and most of water was collected here. The remaining vapor enriched with total nitrogen (TN) was compressed and pumped to the atmospheric condition to condense. The TN concentration in atmospheric condensate was as high as 7000 mg·L^-1 with the process separation factor for ammonia being enhanced to 114.

Key words: Liquid digestate, Resource recovery, Vacuum membrane distillation, Permeate fractional condensation, Enhanced separation factor

Boya Qiu, Senqing Fan, Xiaoyu Tang, Bufan Qi, Liangwei Deng, Wenguo Wang, Jingyun Liu, Yuyang Wang, Zeyi Xiao. Simultaneous recovery of phosphorus and nitrogen from liquid digestate by vacuum membrane distillation with permeate fractional condensation[J]. 中国化学工程学报, 2020, 28(6): 1558-1565.

参考文献

[1] J.P. Sheets, L. Yang, X. Ge, Z. Wang, Y. Li, Beyond land application:Emerging technologies for the treatment and reuse of anaerobically digested agricultural and food waste, Waste Manag. 44(2015) 94-115.
[2] G.Y. Zhen, X.Q. Lu, H. Kato, Y.C. Zhao, Y.Y. Li, Overview of pretreatment strategies for enhancing sewage sludge disintegration and subsequent anaerobic digestion:Current advances, full-scale application and future perspectives, Renew. Sust. Energ. Rev. 69(2017) 559-577.
[3] C. Sawatdeenarunat, K.C. Surendra, D. Takara, H. Oechsner, S.K. Khanal, Anaerobic digestion of lignocellulosic biomass:Challenges and opportunities, Bioresour. Technol. 178(2015) 178-186.
[4] P. Elefsiniotis, D.G. Wareham, W.K. Oldham, Particulate organic carbon solubilization in an acid-phase upflow anaerobic sludge blanket system, Environ. Sci. Technol. 30(1996) 1508-1514.
[5] Y.-Y. Li, T. Kobayashi, Applications and new developments of biogas technology in Japan, Environ. Anaerobic Technol. pp (2010) 35-58.
[6] Z.J. Ren, A.K. Umble, Recover wastewater resources locally, Nature. 529(2016) 25.
[7] W.D. Tao, A.T. Ukwuani, Coupling thermal stripping and acid absorption for ammonia recovery from dairy manure:Ammonia volatilization kinetics and effects of temperature, pH and dissolved solids content, Chem. Eng. J. 280(2015) 188-196.
[8] X. Vecino, M. Reig, B. Bhushan, O. Gibert, C. Valderrama, J.L. Cortina, Liquid fertilizer production by ammonia recovery from treated ammonia-rich regenerated streams using liquid-liquid membrane contactors, Chem. Eng. J. 360(2019) 890-899.
[9] A.T. Ukwuani, W. Tao, Developing a vacuum thermal stripping-acid absorption process for ammonia recovery from anaerobic digester effluent, Water Res. 106(2016) 108-115.
[10] A.P. Jiang, T.X. Zhang, Q.B. Zhao, X.J. Li, S.L. Chen, C.S. Frear, Evaluation of an integrated ammonia stripping, recovery, and biogas scrubbing system for use with anaerobically digested dairy manure, Biosyst. Eng. 119(2014) 117-126.
[11] T. Lyu, K. He, R. Dong, S. Wu, The intensified constructed wetlands are promising for treatment of ammonia stripped effluent:Nitrogen transformations and removal pathways, Environ. Pollut. 236(2018) 273-282.
[12] L. Pastor, D. Mangin, J. Ferrer, A. Seco, Struvite formation from the supernatants of an anaerobic digestion pilot plant, Bioresour. Technol. 101(2010) 118-125.
[13] M. Ronteltap, M. Maurer, R. Hausherr, W. Gujer, Struvite precipitation from urine-Influencing factors on particle size, Water Res. 44(2010) 2038-2046.
[14] I. Wollmann, A. Gauro, T. Muller, K. Moller, Phosphorus bioavailability of sewage sludge-based recycled fertilizers, J. Plant Nutr. Soil Sci. 181(2018) 158-166.
[15] M. Xie, H.K. Shon, S.R. Gray, M. Elimelech, Membrane-based processes for wastewater nutrient recovery:Technology, challenges, and future direction, Water Res. 89(2016) 210-221.
[16] A. Zarebska, D. Romero Nieto, K.V. Christensen, L. Fjerbæk Søtoft, B. Norddahl, Ammonium fertilizers production from manure:A critical review, Crit. Rev. Env. Sci. Tec. 45(2015) 1469-1521.
[17] S. Kertesz, S. Beszedes, Z. Laszlo, G. Szabo, C. Hodur, Nanofiltration and reverse osmosis of pig manure:Comparison of results from vibratory and classical modules, Desalin. Water Treat. 14(2010) 233-238.
[18] L.I.M. Ayala, M. Paquet, K. Janowska, P. Jamard, C.A.Q. Jensen, G.N. Bosio, D.O. Martire, D. Fabbri, V. Boffa, Water defluoridation:Nanofiltration vs membrane distillation, Ind. Eng. Chem. Res. 57(2018) 14740-14748.
[19] J.Z. Ma, H.M. Irfan, Y.F. Wang, X. Feng, D.M. Xu, Recovering wastewater in a cooling water system with thermal membrane distillation, Ind. Eng. Chem. Res. 57(2018) 10491-10499.
[20] J. Li, W. Zhou, S. Fan, Z. Xiao, Y. Liu, J. Liu, B. Qiu, Y. Wang, Bioethanol production in vacuum membrane distillation bioreactor by permeate fractional condensation and mechanical vapor compression with polytetrafluoroethylene (PTFE) membrane, Bioresour. Technol. 268(2018) 708-714.
[21] X. Song, W. Luo, J. McDonald, S.J. Khan, F.I. Hai, W.E. Price, L.D. Nghiem, An anaerobic membrane bioreactor-membrane distillation hybrid system for energy recovery and water reuse:Removal performance of organic carbon, nutrients, and trace organic contaminants, Sci. Total Environ. 628-629(2018) 358-365.
[22] M.S. El-Bourawi, M. Khayet, R. Ma, Z. Ding, Z. Li, X. Zhang, Application of vacuum membrane distillation for ammonia removal, J. Membrane Sci. 301(2007) 200-209.
[23] A. Zarebska, D.R. Nieto, K.V. Christensen, B. Norddahl, Ammonia recovery from agricultural wastes by membrane distillation:Fouling characterization and mechanism, Water Res. 56(2014) 1-10.
[24] Q. He, T. Tu, S. Yan, X. Yang, M. Duke, Y. Zhang, S. Zhao, Relating water vapor transfer to ammonia recovery from biogas slurry by vacuum membrane distillation, Sep. Purif. Technol. 191(2018) 182-191.
[25] D. Qu, D. Sun, H. Wang, Y. Yun, Experimental study of ammonia removal from water by modified direct contact membrane distillation, Desalination 326(2013) 135-140.
[26] L. Li, Z. Xiao, S. Tan, L. Pu, Z. Zhang, Composite PDMS membrane with high flux for the separation of organics from water by pervaporation, J. Membrane Sci. 243(2004) 177-187.
[27] F.J. Baumann, Dichromate reflux chemical oxygen demand-Proposed method for chloride correction in highly saline wastes, Anal. Chem. 46(1974) 1336-1338.
[28] A. Bonmatí, X. Flotats, Air stripping of ammonia from pig slurry:characterisation and feasibility as a pre-or post-treatment to mesophilic anaerobic digestion, Waste Manag. 23(2003) 261-272.
[29] C.-K. Chiam, R. Sarbatly, Vacuum membrane distillation processes for aqueous solution treatment-A review, Chem. Eng. Process. 74(2013) 27-54.
[30] H. Li, F. Tan, L. Ke, D. Xia, Y. Wang, N. He, Y. Zheng, Q. Li, Mass balances and distributions of C, N, and P in the anaerobic digestion of different substrates and relationships between products and substrates, Chem. Eng. J. 287(2016) 329-336.
[31] I. Dincer, Renewable energy and sustainable development:A crucial review, Renew. Sust. Energ. Rev. 4(2000) 157-175.
[32] B. Wu, X. Tan, K. Li, W.K. Teo, Removal of 1,1,1-trichloroethane from water using a polyvinylidene fluoride hollow fiber membrane module:Vacuum membrane distillation operation, Sep. Purif. Technol. 52(2006) 301-309.
[33] L. Tang, A. Iddya, X.B. Zhu, A.V. Dudchenko, W.Y. Duan, C. Turchi, J. Vanneste, T.Y. Cath, D. Jassby, Enhanced flux and electrochemical cleaning of silicate scaling on carbon nanotube-coated membrane distillation membranes treating geothermal brines, Acs Appl. Mater. Inter. 9(2017) 38594-38605.
[34] C. Chen,W.Guo,H.H. Ngo, D.-J. Lee, K.-L. Tung, P.Jin, J. Wang,Y.Wu,Challengesin biogas production from anaerobic membrane bioreactors, Renew. Energ. 98(2016) 120-134.
[35] M. Laqbaqbi, M.C. García-Payo, M. Khayet, J. El Kharraz, M. Chaouch, Application of direct contact membrane distillation for textile wastewater treatment and fouling study, Sep. Purif. Technol. 209(2019) 815-825.
[36] F. Li, J. Huang, Q. Xia, M. Lou, B. Yang, Q. Tian, Y. Liu, Direct contact membrane distillation for the treatment of industrial dyeing wastewater and characteristic pollutants, Sep. Purif. Technol. 195(2018) 83-91.
[37] L.E. de-Bashan, Y. Bashan, Recent advances in removing phosphorus from wastewater and its future use as fertilizer (1997-2003), Water Res. 38(2004) 4222-4246.
[38] T. Yan, Y. Ye, H. Ma, Y. Zhang, W. Guo, B. Du, Q. Wei, D. Wei, H.H. Ngo, A critical review on membrane hybrid system for nutrient recovery from wastewater, Chem. Eng. J. 348(2018) 143-156.
[39] Q.Y. He, G. Yu, T. Tu, S.P. Yan, Y.L. Zhang, S.F. Zhao, Closing CO₂ loop in biogas production:Recycling ammonia as fertilizer, Environ. Sci. Technol. 51(2017) 8841-8850.
[40] Z. Ding, L. Liu, Z. Li, R. Ma, Z. Yang, Experimental study of ammonia removal from water by membrane distillation (MD):The comparison of three configurations, J. Membrane Sci. 286(2006) 93-103.

Simultaneous recovery of phosphorus and nitrogen from liquid digestate by vacuum membrane distillation with permeate fractional condensation

Simultaneous recovery of phosphorus and nitrogen from liquid digestate by vacuum membrane distillation with permeate fractional condensation

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