Chemical Industry and Engineering Progress ›› 2024, Vol. 43 ›› Issue (7): 3672-3691.DOI: 10.16085/j.issn.1000-6613.2024-0196
• Column: Thermochemical Reaction Engineering Technology • Previous Articles
HU Rui1,4,5,6(), LI Xianru2, PIAO Weiling2, FENG Pan2, LUO Lei3, LUO Gang1,4,5,6, WEI Huangzhao2(), LIU Zhengang3(), ZHANG Shicheng1,4,5,6()
Received:
2024-01-25
Revised:
2024-05-07
Online:
2024-08-14
Published:
2024-07-10
Contact:
WEI Huangzhao, LIU Zhengang, ZHANG Shicheng
胡锐1,4,5,6(), 李先如2, 朴玮玲2, 冯盼2, 罗磊3, 罗刚1,4,5,6, 卫皇曌2(), 刘振刚3(), 张士成1,4,5,6()
通讯作者:
卫皇曌,刘振刚,张士成
作者简介:
胡锐(1995—),男,博士研究生,研究方向为有机固废污染控制与资源化利用、废水生物脱氮和资源化利用技术。E-mail:21110740028@m.fudan.edu.cn。
基金资助:
CLC Number:
HU Rui, LI Xianru, PIAO Weiling, FENG Pan, LUO Lei, LUO Gang, WEI Huangzhao, LIU Zhengang, ZHANG Shicheng. Progress on the hydrothermal conversion equipment and technology of organic waste[J]. Chemical Industry and Engineering Progress, 2024, 43(7): 3672-3691.
胡锐, 李先如, 朴玮玲, 冯盼, 罗磊, 罗刚, 卫皇曌, 刘振刚, 张士成. 有机废物水热转化设备与技术研究进展[J]. 化工进展, 2024, 43(7): 3672-3691.
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URL: https://hgjz.cip.com.cn/EN/10.16085/j.issn.1000-6613.2024-0196
条件 | 温度/℃ | 压力/MPa | 密度/kg·m-3 | 静态介电常数/F·m-1 | 离子积(pKw) | 动态黏度/mPa·s |
---|---|---|---|---|---|---|
标准条件 | 25 | 0.1 | 1000 | 78.5 | 14 | 0.89 |
亚临界条件 | 350 | 25 | 600 | 14.07 | 12 | 0.064 |
超临界条件 | 500 | 25 | 78 | 1.46 | 23 | 0.03 |
条件 | 温度/℃ | 压力/MPa | 密度/kg·m-3 | 静态介电常数/F·m-1 | 离子积(pKw) | 动态黏度/mPa·s |
---|---|---|---|---|---|---|
标准条件 | 25 | 0.1 | 1000 | 78.5 | 14 | 0.89 |
亚临界条件 | 350 | 25 | 600 | 14.07 | 12 | 0.064 |
超临界条件 | 500 | 25 | 78 | 1.46 | 23 | 0.03 |
方法 | 温度/℃ | 压力/MPa | 催化剂 | 主要产物产率 | 优点 | 限制 |
---|---|---|---|---|---|---|
HTC | 120~260 | 2~10 | 过氧化氢、有机酸、无机酸、无机碱、金属氯化物、金属氧化物等 | 水热炭:5%~97% | 高湿度底物、高热值、无NO x 和SO x 释放 | 水热炭灰分含量高、重金属含量高 |
HTL | 200~375 | 5~35 | 碳酸钠、氯化钾、氢氧化钾、氢氧化钠、固体酸/碱等 | 生物油率:9.4%~77.2% | 高的油产率、高热值、应用范围广 | 生物原油含有较多的杂原子、呈酸性、高黏度和高氨氮性质,需要进一步提炼 |
HTG | 300~900 | >22.1 | 氢氧化钾、镍、碳酸钾、碳酸钠、钌基催化剂、金属氯化物等 | H2产率:10%~80% | 消除传质限制、无NO x 和SO x 释放 | 盐沉积、危险性高、催化剂失活、反应器堵塞 |
HTO | >100 | >2 | 氧化剂:如过氧化氢、氧气 | — | 有机物矿化率高 | 盐沉积和堵塞、需要催化剂、高能耗和操作费用 |
方法 | 温度/℃ | 压力/MPa | 催化剂 | 主要产物产率 | 优点 | 限制 |
---|---|---|---|---|---|---|
HTC | 120~260 | 2~10 | 过氧化氢、有机酸、无机酸、无机碱、金属氯化物、金属氧化物等 | 水热炭:5%~97% | 高湿度底物、高热值、无NO x 和SO x 释放 | 水热炭灰分含量高、重金属含量高 |
HTL | 200~375 | 5~35 | 碳酸钠、氯化钾、氢氧化钾、氢氧化钠、固体酸/碱等 | 生物油率:9.4%~77.2% | 高的油产率、高热值、应用范围广 | 生物原油含有较多的杂原子、呈酸性、高黏度和高氨氮性质,需要进一步提炼 |
HTG | 300~900 | >22.1 | 氢氧化钾、镍、碳酸钾、碳酸钠、钌基催化剂、金属氯化物等 | H2产率:10%~80% | 消除传质限制、无NO x 和SO x 释放 | 盐沉积、危险性高、催化剂失活、反应器堵塞 |
HTO | >100 | >2 | 氧化剂:如过氧化氢、氧气 | — | 有机物矿化率高 | 盐沉积和堵塞、需要催化剂、高能耗和操作费用 |
废水名称 | 主要有机物 | 接受废水量 /t | 废水COD /mg·L-1 | COD去除率/% |
---|---|---|---|---|
TPU废水 | 四氢呋喃、丙二醇等 | 440 | 15000~40000 | 90~98 |
TMP废水 | 二羟甲基丁醛、 TMP等 | 6 | 90000~110000 | 95~98 |
IP废水 | 异佛尔酮、甲醇等 | 15 | 80000~100000 | 90~96 |
MDBA废水 | 丁酮、仲丁醇等 | 80 | 15000~26000 | 90~95 |
SAP废水 | 丙烯酸等 | 4 | 20000~25000 | 93~95 |
废水名称 | 主要有机物 | 接受废水量 /t | 废水COD /mg·L-1 | COD去除率/% |
---|---|---|---|---|
TPU废水 | 四氢呋喃、丙二醇等 | 440 | 15000~40000 | 90~98 |
TMP废水 | 二羟甲基丁醛、 TMP等 | 6 | 90000~110000 | 95~98 |
IP废水 | 异佛尔酮、甲醇等 | 15 | 80000~100000 | 90~96 |
MDBA废水 | 丁酮、仲丁醇等 | 80 | 15000~26000 | 90~95 |
SAP废水 | 丙烯酸等 | 4 | 20000~25000 | 93~95 |
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