光合细菌污水资源化研究进展

doi:10.11894/iwt.2019-0808

摘要/Abstract

摘要：

光合细菌污水资源化是一种新兴的有机废水处理及生物资源转化技术。光合细菌能够高效处理污水，同时把碳氮磷转化为有用的菌体细胞，可用于水产、畜禽养殖和农作物培育。从光合细菌污水资源化技术对营养型废水的资源化、对高氨氮废水的高效氮去除、对其他类型废水的处理、光合细菌污水处理重要影响因素、主要促进方法5个方面进行了综述。最后对未来的研究进行了展望。

关键词: 光合细菌, 污水处理, 污水资源化, 研究进展

Abstract:

Resource recovery of wastewater by photosynthetic bacteria(PSB) is a novel technology for organic wastewater and bioresource recovery. PSB can simultaneously remove pollutants efficiently and convert carbon, nitrogen, and phosphorus into useful bacterial cells. Its economic value lies on that PSB cells can be used in aquaculture, livestock breeding, and crop cultivation. The technology was reviewed from five aspects:resource conversions from non-toxic nutrient-rich wastewaters, high-efficiency nitrogen removal from high ammonia nitrogen wastewater, applications in other types of wastewater, and influence factors and improvement methods. Future developments were also discussed.

Key words: photosynthetic bacteria, wastewater treatment, resource recovery of wastewater, research progress

中图分类号:

X703

张光明,孟帆,曹可凡,郅然. 光合细菌污水资源化研究进展[J]. 工业水处理, 2020, 40(3): 1-6.

Guangming Zhang,Fan Meng,Kefan Cao,Ran Zhi. Research progress in resource recovery of wastewater by photosynthetic bacteria(PSB)[J]. Industrial Water Treatment, 2020, 40(3): 1-6.

https://www.iwt.cn/CN/Y2020/V40/I3/1

图/表 6

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废水	COD去除率/%	初始COD/ （mg·L^-1）	处理后COD/ （mg·L^-1）
大豆废水^〔12〕	96	4 000~8 000	200~1 000
大豆废水^〔13〕	96	490~8500	112~298
大豆废水^〔14〕	93	9 941	690
制糖废水^〔15〕	95	6 000	300
制糖废水^〔16〕	93	6 650	460
制糖废水^〔17〕	80	346~787	70~158
淀粉废水^〔18〕	88	560~2 620	182
淀粉废水^〔19〕	91	10 000	900
淀粉废水^〔20〕	77
淀粉废水^〔21〕	95	2 264	193.3
淀粉废水^〔22〕	70~90	6 500	700
酿酒废水^〔23〕	97	2 200~2 600	80
酿酒废水^〔24〕	97	2 500~4 800	76
酿酒废水^〔25〕	76	9 000~26 000	2 000~6 000
柠檬酸废水^〔9〕	89	4 800	530
果胶废水^〔26〕	95	1 500	75
蛋白粉废水^〔26〕	89	1 700	187
味精废水^〔27〕	80	3 000	600
乳品废水^〔28〕	89	2 000	220

废水	COD去除率/%	初始COD/ （mg·L^-1）	处理后COD/ （mg·L^-1）
大豆废水^〔12〕	96	4 000~8 000	200~1 000
大豆废水^〔13〕	96	490~8500	112~298
大豆废水^〔14〕	93	9 941	690
制糖废水^〔15〕	95	6 000	300
制糖废水^〔16〕	93	6 650	460
制糖废水^〔17〕	80	346~787	70~158
淀粉废水^〔18〕	88	560~2 620	182
淀粉废水^〔19〕	91	10 000	900
淀粉废水^〔20〕	77
淀粉废水^〔21〕	95	2 264	193.3
淀粉废水^〔22〕	70~90	6 500	700
酿酒废水^〔23〕	97	2 200~2 600	80
酿酒废水^〔24〕	97	2 500~4 800	76
酿酒废水^〔25〕	76	9 000~26 000	2 000~6 000
柠檬酸废水^〔9〕	89	4 800	530
果胶废水^〔26〕	95	1 500	75
蛋白粉废水^〔26〕	89	1 700	187
味精废水^〔27〕	80	3 000	600
乳品废水^〔28〕	89	2 000	220

废水	生物量/ （mg·L^-1）	产率
大豆废水^〔12〕	1 585	0.4
大豆废水^〔13〕	1 275	0.5
大豆废水^〔14〕	4 801	0.5
制糖废水^〔15〕	2 645	0.4
制糖废水^〔16〕	1 645	0.2
制糖废水^〔29〕	5 000	1.4
制糖废水^〔17〕	24 800
淀粉废水^〔18〕	940	0.51
淀粉废水^〔19〕	4 060	0.4
淀粉废水^〔20〕	2 500	0.59
淀粉废水^〔21〕	1 937	1.02
淀粉废水^〔22〕		0.4
酿酒废水^〔23〕	1 000	0.2
酿酒废水^〔24〕	4 500	1.0
酿酒废水^〔25〕	900	0.5
柠檬酸废水^〔7〕	2 375	0.8
味精废水^〔27〕	2 000
乳品废水^〔28〕	2 200

废水	生物量/ （mg·L^-1）	产率
大豆废水^〔12〕	1 585	0.4
大豆废水^〔13〕	1 275	0.5
大豆废水^〔14〕	4 801	0.5
制糖废水^〔15〕	2 645	0.4
制糖废水^〔16〕	1 645	0.2
制糖废水^〔29〕	5 000	1.4
制糖废水^〔17〕	24 800
淀粉废水^〔18〕	940	0.51
淀粉废水^〔19〕	4 060	0.4
淀粉废水^〔20〕	2 500	0.59
淀粉废水^〔21〕	1 937	1.02
淀粉废水^〔22〕		0.4
酿酒废水^〔23〕	1 000	0.2
酿酒废水^〔24〕	4 500	1.0
酿酒废水^〔25〕	900	0.5
柠檬酸废水^〔7〕	2 375	0.8
味精废水^〔27〕	2 000
乳品废水^〔28〕	2 200

废水	蛋白质含量	辅酶Q10	5-ALA	色素	PHA
大豆废水^〔13〕	52%
大豆废水^〔26〕	50%		4.5~12.5 mg/g
制糖废水^〔15〕				类胡萝卜素1.5 mg/L，菌绿素1.5 mg/L
制糖废水^〔16〕	42%	38.6 mg/g		类胡萝卜素1.7 mg/L，菌绿素9 mg/L
制糖废水^〔17〕	＞50%			类胡萝卜素100 mg/L
制糖废水^〔30〕	50%	88.8 mg/g
淀粉废水^〔18〕	58%
淀粉废水^〔20〕				类胡萝卜素2.3 mg/L	0.2~0.3 g/g
淀粉废水^〔22〕	30%~50%
酒糟废水^〔23〕	40%			类胡萝卜素3 mg/L，菌绿素11 mg/L
挥发酸废水^〔31〕			3.6~5.8 mg/g	类胡萝卜素5 mg/g
膜浓缩废水^〔32〕	80%

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