Acta Agriculturae Zhejiangensis ›› 2023, Vol. 35 ›› Issue (6): 1407-1415.DOI: 10.3969/j.issn.1004-1524.2023.06.18
• Environmental Science • Previous Articles Next Articles
XIAO Hua1(), XU Xing1, XIE Chuanqi1, ZHOU Xin1, ZHOU Weidong1,*(
), TANG Wensheng2,*(
)
Received:
2022-06-21
Online:
2023-06-25
Published:
2023-07-04
CLC Number:
XIAO Hua, XU Xing, XIE Chuanqi, ZHOU Xin, ZHOU Weidong, TANG Wensheng. Effect of struvite precipitation pretreatment on membrane concentration process of piggery biogas slurry[J]. Acta Agriculturae Zhejiangensis, 2023, 35(6): 1407-1415.
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URL: http://www.zjnyxb.cn/EN/10.3969/j.issn.1004-1524.2023.06.18
Fig.1 Devices used in experiment and flow-process A, Photo of chemical precipitation device; b, Flow of chemical precipitation; c, Photo of membrane concentration device; d, Flow of membrane concentration.
样品 Sample | pH | 浊度 Turbidity | 电导率 Electrical conductivity/(μS·cm-1) | CODCr/ (mg·L-1) | 氨氮 Ammonia nitrogen/(mg·L-1) |
---|---|---|---|---|---|
预处理前Before pretreatment | 8.42 | 1 560 | 6 530 | 2 994 | 561 |
预处理后After pretreatment | 9.47 | 1 146 | 3 170 | 2 534 | 66.7 |
Table 1 Physicochemical properties of biogas slurry before and after chemical precipitation pretreatment
样品 Sample | pH | 浊度 Turbidity | 电导率 Electrical conductivity/(μS·cm-1) | CODCr/ (mg·L-1) | 氨氮 Ammonia nitrogen/(mg·L-1) |
---|---|---|---|---|---|
预处理前Before pretreatment | 8.42 | 1 560 | 6 530 | 2 994 | 561 |
预处理后After pretreatment | 9.47 | 1 146 | 3 170 | 2 534 | 66.7 |
Fig.2 Effect of chemical precipitation pretreatment on ultrafiltration membrane flux Reaction conditions are as follows: operation pressure of 0.15 MPa, temperature of (32±1) ℃.
Fig.3 Effect of chemical precipitation pretreatment on reverse osmosis membrane flux Reaction conditions are as follows: operation pressure of 1.0 MPa, temperature of (28±1) ℃.
组别 Category | 不同浓缩倍数出水的浊度 Turbidity of outlet at different volume reduction factor | 不同浓缩倍数出水的CODCr CODCr of outlet at different volume reduction factor/(mg·L-1) | ||||||
---|---|---|---|---|---|---|---|---|
2 | 3 | 4 | 5 | 2 | 3 | 4 | 5 | |
对照组 Control group | 1.2 (99.92%) | 1.52 (99.90%) | 1.84 (99.88%) | 1.94 (99.87%) | 1 284 (57.11%) | 1 354 (54.78%) | 1 474 (50.77%) | 1 754 (41.42%) |
预处理组 Pretreatment group | 0.73 (99.94%) | 0.72 (99.94%) | 0.87 (99.92%) | 1.18 (99.90%) | 694 (72.61%) | 704 (72.22%) | 764 (69.85%) | 864 (65.90%) |
Table 2 Effect of pretreatment on removal of turbidity and CODcr of biogas slurry by ultrafiltration
组别 Category | 不同浓缩倍数出水的浊度 Turbidity of outlet at different volume reduction factor | 不同浓缩倍数出水的CODCr CODCr of outlet at different volume reduction factor/(mg·L-1) | ||||||
---|---|---|---|---|---|---|---|---|
2 | 3 | 4 | 5 | 2 | 3 | 4 | 5 | |
对照组 Control group | 1.2 (99.92%) | 1.52 (99.90%) | 1.84 (99.88%) | 1.94 (99.87%) | 1 284 (57.11%) | 1 354 (54.78%) | 1 474 (50.77%) | 1 754 (41.42%) |
预处理组 Pretreatment group | 0.73 (99.94%) | 0.72 (99.94%) | 0.87 (99.92%) | 1.18 (99.90%) | 694 (72.61%) | 704 (72.22%) | 764 (69.85%) | 864 (65.90%) |
Fig.4 Effect of chemical precipitation pretreatment on CODCr and salinity removal by reverse osmosis Reaction conditions are as follows: operation pressure of 1.0 MPa, temperature of (28±1) ℃.
Fig.5 Effect of pretreatment on ammonia nitrogen mass concentration of reverse osmosis permeate Reaction conditions: operation pressure of 1.0 MPa, temperature of (28±1) ℃.
样品 Sample | CODCr/ (mg·L-1) | 氨氮 Ammonia nitrogen/ (mg·L-1) | 电导率 Electrical conductivit/ (μS·cm-1) |
---|---|---|---|
原水Raw | 2 994 | 561 | 6 530 |
对照组超滤出水Ultrafiltration effluent without pretreatment | 1 310 | 470 | 5 790 |
对照组反渗透出水Reverse osmosis effluent without pretreatment | 366 | 160 | 620 |
预处理出水Effluent after pretreatment | 2 534 | 67 | 3 170 |
预处理组超滤出水Ultrafiltration effluent after pretreatment | 637 | 63 | 2 910 |
预处理组反渗透出水Reverse osmosis effluent after pretreatment | 135 | 21 | 160 |
Table 3 Effluent quality of different units
样品 Sample | CODCr/ (mg·L-1) | 氨氮 Ammonia nitrogen/ (mg·L-1) | 电导率 Electrical conductivit/ (μS·cm-1) |
---|---|---|---|
原水Raw | 2 994 | 561 | 6 530 |
对照组超滤出水Ultrafiltration effluent without pretreatment | 1 310 | 470 | 5 790 |
对照组反渗透出水Reverse osmosis effluent without pretreatment | 366 | 160 | 620 |
预处理出水Effluent after pretreatment | 2 534 | 67 | 3 170 |
预处理组超滤出水Ultrafiltration effluent after pretreatment | 637 | 63 | 2 910 |
预处理组反渗透出水Reverse osmosis effluent after pretreatment | 135 | 21 | 160 |
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