Chemical Industry and Engineering Progress ›› 2019, Vol. 38 ›› Issue (02): 1027-1037.DOI: 10.16085/j.issn.1000-6613.2018-0806
• Biochemical and pharmaceutical engineering • Previous Articles Next Articles
Pei GUO1(),Rongjiang MA2,Nanyang YU1(),Yanping YUAN1
Received:
2018-04-18
Revised:
2018-05-22
Online:
2019-02-05
Published:
2019-02-05
Contact:
Nanyang YU
通讯作者:
余南阳
作者简介:
<named-content content-type="corresp-name">郭沛</named-content>(1994—),男,博士研究生,研究方向为生物质能源的开发及应用。E-mail:<email>jeep1994@163.com</email>。|余南阳,教授,博士生导师,研究方向为空调系统故障诊断与节能控制、可再生能源及低温余热综合利用等。E-mail:<email>rhinos@126.com</email>。
基金资助:
CLC Number:
Pei GUO, Rongjiang MA, Nanyang YU, Yanping YUAN. Recent progress in coupling technologies of biogas slurry treatment based on microalgae cultivation[J]. Chemical Industry and Engineering Progress, 2019, 38(02): 1027-1037.
郭沛, 马荣江, 余南阳, 袁艳平. 基于微藻培养的沼液处理相关耦合技术进展[J]. 化工进展, 2019, 38(02): 1027-1037.
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URL: https://hgjz.cip.com.cn/EN/10.16085/j.issn.1000-6613.2018-0806
COD/mg·L–1 | NH3-N/mg·L–1 | TP/mg·L–1 | pH |
---|---|---|---|
300~10000 | 400~3200 | 50~300 | 7.2~8.5 |
COD/mg·L–1 | NH3-N/mg·L–1 | TP/mg·L–1 | pH |
---|---|---|---|
300~10000 | 400~3200 | 50~300 | 7.2~8.5 |
原料 | 油脂质量分数/% | 油脂产量/L·hm-2·a-1 |
---|---|---|
大豆 | 15~20 | 446 |
向日葵 | 25~35 | 952 |
油菜籽 | 38~46 | 1190 |
花生 | 45~55 | 1059 |
玉米 | 48 | 72 |
棕榈树 | 30~60 | 5950 |
微藻(低油成分) | 30 | 58700 |
微藻(中油成分) | 50 | 97800 |
微藻(高油成分) | 70 | 136900 |
原料 | 油脂质量分数/% | 油脂产量/L·hm-2·a-1 |
---|---|---|
大豆 | 15~20 | 446 |
向日葵 | 25~35 | 952 |
油菜籽 | 38~46 | 1190 |
花生 | 45~55 | 1059 |
玉米 | 48 | 72 |
棕榈树 | 30~60 | 5950 |
微藻(低油成分) | 30 | 58700 |
微藻(中油成分) | 50 | 97800 |
微藻(高油成分) | 70 | 136900 |
废水类型 | 藻种 | 生物量 /g·L-1 | 油脂含量 /mg·L-1 | 参考文献 |
---|---|---|---|---|
市政污水 | Chlorella sp.227 | 0.666 | 206.1① | [ |
市政污水 | Nannochloropsis sp. | 0.212 | 63.6 | [ |
市政二级出水 | Chlorella sp., Micractinium sp., Actinastrum sp. | 0.812 | 73.08 | [ |
市政二级出水 | Neochloris oleoabundans OU2 | 0.68 | — | [ |
豆腐厂废水(20%) | Chlorella vulgaris | 0.758 | 166.8 | [ |
豆腐厂废水(30%) | Chlorella vulgaris | 0.827 | 191.9 | [ |
造纸厂废水和市政污水(1∶1) | Scenedesmus dimorphus | 0.92 | 220.8 | [ |
牛场废水 | Chroococcus sp.1 | 3.83 | — | [ |
秸秆厌氧发酵液 | Chorella pyrenoidosa | 1.45 | 270.9 | [ |
猪场厌氧发酵液 | Desmodesmus sp. | 1.039 | 261.8 | [ |
废水类型 | 藻种 | 生物量 /g·L-1 | 油脂含量 /mg·L-1 | 参考文献 |
---|---|---|---|---|
市政污水 | Chlorella sp.227 | 0.666 | 206.1① | [ |
市政污水 | Nannochloropsis sp. | 0.212 | 63.6 | [ |
市政二级出水 | Chlorella sp., Micractinium sp., Actinastrum sp. | 0.812 | 73.08 | [ |
市政二级出水 | Neochloris oleoabundans OU2 | 0.68 | — | [ |
豆腐厂废水(20%) | Chlorella vulgaris | 0.758 | 166.8 | [ |
豆腐厂废水(30%) | Chlorella vulgaris | 0.827 | 191.9 | [ |
造纸厂废水和市政污水(1∶1) | Scenedesmus dimorphus | 0.92 | 220.8 | [ |
牛场废水 | Chroococcus sp.1 | 3.83 | — | [ |
秸秆厌氧发酵液 | Chorella pyrenoidosa | 1.45 | 270.9 | [ |
猪场厌氧发酵液 | Desmodesmus sp. | 1.039 | 261.8 | [ |
技术类型 | 主要技术手段 | 特点 | 参考文献 |
---|---|---|---|
微藻高密度培养技术 | 固定化培养 | 易收获、产量稳定、成本低 | [ |
连续化培养 | 微藻生长状态稳定、产量高、培养成本高 | [ | |
微藻采收技术 | 化学法:絮凝、电凝 | 应用广泛、效果较好 | [ |
物理法:离心、膜过滤、气浮收获 | 操作简单、投入少但能耗较高 | ||
微藻干燥技术 | 冻干、喷雾、鼓风、自然风干 | 自然风干受天气影响较大且易受污染;其他方法成本较高,但成分破坏较少 | [ |
微藻细胞破壁技术 | 物理法:超声波处理、高压均质、珠磨 | 破碎效率高、能耗高、设备要求高 | [ |
酶法:酶处理 | 破碎效率一般,成本高 | [ | |
化学法:酸处理、臭氧处理、反复冻溶 | 破碎效率一般,需化学物质,污染环境 | [ | |
微藻高值生物质提取技术 | 有机溶剂提取法 | 溶剂添加量大、提取效率低、技术简单 | [ |
超/亚临界萃取法 | 处理工艺能耗高、经济性较差、技术设备要求高 | ||
原位萃取法 | 不需干燥、提取效率较高、技术不成熟 |
技术类型 | 主要技术手段 | 特点 | 参考文献 |
---|---|---|---|
微藻高密度培养技术 | 固定化培养 | 易收获、产量稳定、成本低 | [ |
连续化培养 | 微藻生长状态稳定、产量高、培养成本高 | [ | |
微藻采收技术 | 化学法:絮凝、电凝 | 应用广泛、效果较好 | [ |
物理法:离心、膜过滤、气浮收获 | 操作简单、投入少但能耗较高 | ||
微藻干燥技术 | 冻干、喷雾、鼓风、自然风干 | 自然风干受天气影响较大且易受污染;其他方法成本较高,但成分破坏较少 | [ |
微藻细胞破壁技术 | 物理法:超声波处理、高压均质、珠磨 | 破碎效率高、能耗高、设备要求高 | [ |
酶法:酶处理 | 破碎效率一般,成本高 | [ | |
化学法:酸处理、臭氧处理、反复冻溶 | 破碎效率一般,需化学物质,污染环境 | [ | |
微藻高值生物质提取技术 | 有机溶剂提取法 | 溶剂添加量大、提取效率低、技术简单 | [ |
超/亚临界萃取法 | 处理工艺能耗高、经济性较差、技术设备要求高 | ||
原位萃取法 | 不需干燥、提取效率较高、技术不成熟 |
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