Chemical Industry and Engineering Progress ›› 2021, Vol. 40 ›› Issue (10): 5348-5359.DOI: 10.16085/j.issn.1000-6613.2020-2183
• Special column:Resource recycling and value-added utilization • Previous Articles Next Articles
GAO Chuanrui1,2(), TIAN Chunyan1(), LI Zhihe2(), YI Weiming2, YUAN Qiaoxia3, FU Peng1, ZHANG Yuchun1, LI Zhiyu1
Received:
2020-11-02
Revised:
2021-02-04
Online:
2021-10-25
Published:
2021-10-10
Contact:
TIAN Chunyan,LI Zhihe
高传瑞1,2(), 田纯焱1(), 李志合2(), 易维明2, 袁巧霞3, 付鹏1, 张玉春1, 李治宇1
通讯作者:
田纯焱,李志合
作者简介:
高传瑞(1994—),男,硕士研究生,研究方向为生物质能源与材料。E-mail:基金资助:
CLC Number:
GAO Chuanrui, TIAN Chunyan, LI Zhihe, YI Weiming, YUAN Qiaoxia, FU Peng, ZHANG Yuchun, LI Zhiyu. Biorefining of biocrude oil: recirculation of by-products and hydrothermal autocatalysis[J]. Chemical Industry and Engineering Progress, 2021, 40(10): 5348-5359.
高传瑞, 田纯焱, 李志合, 易维明, 袁巧霞, 付鹏, 张玉春, 李治宇. 生物原油炼制: 副产物内循环及水热自催化[J]. 化工进展, 2021, 40(10): 5348-5359.
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催化剂 | 原料 | 过程条件 | 产率提升 | 对生物原油催化效果 | 参考文献 | |||||
---|---|---|---|---|---|---|---|---|---|---|
C | H | O | N | S | HHV | |||||
均相催化剂 | ||||||||||
氢氧化钾 | 玉米芯 | 340℃,60min | +49%TO | -22% | -9% | +67% | +33% | N/A | N/A | [ |
碳酸钾 | 木屑 | 280℃,15min | +136%HO | N/A | N/A | N/A | N/A | N/A | N/A | [ |
碳酸钠 | 水葫芦 | -50%HO | N/A | N/A | N/A | N/A | N/A | N/A | [ | |
微绿球藻 | 300℃,60min | -21%TO | +4% | -4% | -92% | +2% | +70% | -0.9% | [ | |
泡桐 | 300℃,10min | +18%HO | +5% | +2% | -13% | N/A | N/A | +7% | [ | |
螺旋藻 | 350℃,60min | -11%TO | +3% | +17% | -16% | -34% | +0.5% | -5% | [ | |
+29%HO | -2% | +11% | +16% | -14% | -3% | +3% | [ | |||
甲酸 | 380℃,120min | +28%TO | -1% | -12% | +18% | -27% | N/A | -7% | [ | |
盐酸 | 纤维素 | 300℃,0min | +21%LO | N/A | N/A | N/A | N/A | N/A | N/A | [ |
乙酸 | 小球藻蛋白 | 300℃,20min,8.5MPa | 降低LO | -7% | +81% | +3% | -10% | N/A | +18% | [ |
非均相催化剂 | ||||||||||
铁粉 | 泡桐 | 340℃,10min | +51%HO | +10% | +20% | -29% | N/A | N/A | +20% | [ |
硼酸钙石粉 | 山毛榉 | 300℃,0min | +89%HO | +4% | -4% | -6% | N/A | N/A | +3% | [ |
沸石 | +29%TO | -8% | -7% | +3% | +4% | -12% | -8% | [ | ||
Pt/Al2O3 | -12%TO | +9% | +16% | -37% | -12% | N/A | +11% | [ | ||
Ni/Al2O3 | -47%TO | +13% | +7% | -46% | -12% | N/A | +11% | |||
Co/Mo/Al2O3 | -26%TO | +13% | +1% | -51% | +12% | N/A | +9% | |||
CoMo/γ-Al2O3 | 微绿球藻 | 350℃,60min | +54%TO | +1% | +1% | -7% | +3% | -31% | +1% | [ |
Ni/SiO2-Al2O3 | +44%TO | 0 | 0 | -6% | -11% | -100% | -1% | |||
Pt/C | +34%TO | +1% | +6% | -8% | -3% | -14% | +3% | |||
Ru/C | +43%TO | -4% | +1% | +2% | -17% | -63% | -3% | |||
Pd/C | +63%TO | -3% | +6% | -2% | -7% | -38% | +0.3% | |||
+4%HO | N/A | N/A | N/A | N/A | N/A | N/A | [ | |||
Pt/C | 280℃,30min | +6%HO | N/A | N/A | N/A | N/A | N/A | N/A | ||
Pd/Al2O3 | 小球藻 | +8%HO | N/A | N/A | N/A | N/A | N/A | N/A | ||
Ce/HZSM-5 | 300℃,20min | +47%LO | +15% | +52% | -10% | -97% | N/A | +40% | [ | |
HZSM-5 | +3%LO | +4% | +25% | -2% | -38% | N/A | +15% | |||
螺旋藻 | 380℃,120min | +7%TO | -0.07% | -5% | -0.8% | +9% | N/A | -2% | [ | |
Ni-Mo/Al2O3 | 微绿球藻 | 340℃,30min | +41%TO | +1% | +5% | -9% | -6% | N/A | +3% | [ |
Ni-Cu/γ-Al2O3 | 纸铝塑 | 330℃,30min | +54%HO | +5% | -1% | -21% | N/A | N/A | +7% | [ |
FeHZSM-5 | 玉米秸秆 | 340℃,30min | +25%HO | N/A | N/A | N/A | N/A | N/A | N/A | [ |
催化剂 | 原料 | 过程条件 | 产率提升 | 对生物原油催化效果 | 参考文献 | |||||
---|---|---|---|---|---|---|---|---|---|---|
C | H | O | N | S | HHV | |||||
均相催化剂 | ||||||||||
氢氧化钾 | 玉米芯 | 340℃,60min | +49%TO | -22% | -9% | +67% | +33% | N/A | N/A | [ |
碳酸钾 | 木屑 | 280℃,15min | +136%HO | N/A | N/A | N/A | N/A | N/A | N/A | [ |
碳酸钠 | 水葫芦 | -50%HO | N/A | N/A | N/A | N/A | N/A | N/A | [ | |
微绿球藻 | 300℃,60min | -21%TO | +4% | -4% | -92% | +2% | +70% | -0.9% | [ | |
泡桐 | 300℃,10min | +18%HO | +5% | +2% | -13% | N/A | N/A | +7% | [ | |
螺旋藻 | 350℃,60min | -11%TO | +3% | +17% | -16% | -34% | +0.5% | -5% | [ | |
+29%HO | -2% | +11% | +16% | -14% | -3% | +3% | [ | |||
甲酸 | 380℃,120min | +28%TO | -1% | -12% | +18% | -27% | N/A | -7% | [ | |
盐酸 | 纤维素 | 300℃,0min | +21%LO | N/A | N/A | N/A | N/A | N/A | N/A | [ |
乙酸 | 小球藻蛋白 | 300℃,20min,8.5MPa | 降低LO | -7% | +81% | +3% | -10% | N/A | +18% | [ |
非均相催化剂 | ||||||||||
铁粉 | 泡桐 | 340℃,10min | +51%HO | +10% | +20% | -29% | N/A | N/A | +20% | [ |
硼酸钙石粉 | 山毛榉 | 300℃,0min | +89%HO | +4% | -4% | -6% | N/A | N/A | +3% | [ |
沸石 | +29%TO | -8% | -7% | +3% | +4% | -12% | -8% | [ | ||
Pt/Al2O3 | -12%TO | +9% | +16% | -37% | -12% | N/A | +11% | [ | ||
Ni/Al2O3 | -47%TO | +13% | +7% | -46% | -12% | N/A | +11% | |||
Co/Mo/Al2O3 | -26%TO | +13% | +1% | -51% | +12% | N/A | +9% | |||
CoMo/γ-Al2O3 | 微绿球藻 | 350℃,60min | +54%TO | +1% | +1% | -7% | +3% | -31% | +1% | [ |
Ni/SiO2-Al2O3 | +44%TO | 0 | 0 | -6% | -11% | -100% | -1% | |||
Pt/C | +34%TO | +1% | +6% | -8% | -3% | -14% | +3% | |||
Ru/C | +43%TO | -4% | +1% | +2% | -17% | -63% | -3% | |||
Pd/C | +63%TO | -3% | +6% | -2% | -7% | -38% | +0.3% | |||
+4%HO | N/A | N/A | N/A | N/A | N/A | N/A | [ | |||
Pt/C | 280℃,30min | +6%HO | N/A | N/A | N/A | N/A | N/A | N/A | ||
Pd/Al2O3 | 小球藻 | +8%HO | N/A | N/A | N/A | N/A | N/A | N/A | ||
Ce/HZSM-5 | 300℃,20min | +47%LO | +15% | +52% | -10% | -97% | N/A | +40% | [ | |
HZSM-5 | +3%LO | +4% | +25% | -2% | -38% | N/A | +15% | |||
螺旋藻 | 380℃,120min | +7%TO | -0.07% | -5% | -0.8% | +9% | N/A | -2% | [ | |
Ni-Mo/Al2O3 | 微绿球藻 | 340℃,30min | +41%TO | +1% | +5% | -9% | -6% | N/A | +3% | [ |
Ni-Cu/γ-Al2O3 | 纸铝塑 | 330℃,30min | +54%HO | +5% | -1% | -21% | N/A | N/A | +7% | [ |
FeHZSM-5 | 玉米秸秆 | 340℃,30min | +25%HO | N/A | N/A | N/A | N/A | N/A | N/A | [ |
原料 | 操作条件 | pH | TOC/mg·L-1 | TN/mg·L-1 | 参考文献 |
---|---|---|---|---|---|
小球藻 | 260~300℃,30~90min | 7.77~8.29 | N/A | 11000~37000 | [ |
天然蓝藻 | 340℃,60min | N/A | 37.22 | 2215 | [ |
核桃壳 | 280℃,30min | N/A | 22900 | N/A | [ |
团集江蓠 | 350℃,15min | N/A | 2800 | 6400 | [ |
细江蓠 | 350℃,15min | N/A | 1750 | 2100 | [ |
微绿球藻 | 350℃,20min | 8.28 | 25.78 | 10.18 | [ |
等鞭金藻 | 350℃,20min | 6.8 | 17.24 | 8.08 | [ |
锯末 | 250℃,60min | 8.12 | N/A | N/A | [ |
原料 | 操作条件 | pH | TOC/mg·L-1 | TN/mg·L-1 | 参考文献 |
---|---|---|---|---|---|
小球藻 | 260~300℃,30~90min | 7.77~8.29 | N/A | 11000~37000 | [ |
天然蓝藻 | 340℃,60min | N/A | 37.22 | 2215 | [ |
核桃壳 | 280℃,30min | N/A | 22900 | N/A | [ |
团集江蓠 | 350℃,15min | N/A | 2800 | 6400 | [ |
细江蓠 | 350℃,15min | N/A | 1750 | 2100 | [ |
微绿球藻 | 350℃,20min | 8.28 | 25.78 | 10.18 | [ |
等鞭金藻 | 350℃,20min | 6.8 | 17.24 | 8.08 | [ |
锯末 | 250℃,60min | 8.12 | N/A | N/A | [ |
原料 | 操作条件 | 循环 次数 | 检测出的有机酸 | 回用效果 | 参考文献 |
---|---|---|---|---|---|
白杨木 | 400℃,7.1~11.1h | 3 | N/A | 第1~3批次处理产油率上升,第4批次产率降低。水相中无机物和水溶性有机物随批次累积,灰分沉积率从6.2增长到12.6%。TOC含量从54.1g/L增加到136.2g/L | [ |
玉米秸秆 | 300℃,30min | 3 | 乙酸、丙酸 | 有机酸含量富集,促进酚酮类转化,生物原油产率提高了3.89%,固体产物中碳含量提高了0.8% | [ |
刚毛藻 江蓠 | 350℃,15min | 2 | N/A | 随着循环次数的增加,气体产物和液体产物的总量下降,固体沉积率下降,产油率分别增加了8.1%和8.89% | [ |
干酒糟 | 350℃,20min | 9 | 乙酸、乙酰丙酸、异丁酸、异戊酸 | 当循环第8次的时候,生物原油的产率从39.4%大幅增加到54.5%,同时循环后的水相体积更小,浓度更高。循环9次,生物原油的含氧量降低了52%。TOC和TN的浓度随循环次数逐渐增大 | [ |
海藻-锯末 | 250℃,60min | 1 | 乙酸、2-己酸 | 水相循环后,产油率由11.1%降到了9.2%,固体残渣生成增加,从31.3%~38.9%。通过回用能大幅度消减过程副产物 | [ |
大麦秸秆 | 300℃,15min | 3 | 乳酸,乙酸,2-羟基异丁酸, 2-丁烯二酸,2-羟基-3-甲基戊酸 | 循环3次后,产油率由34.9%增长到38.4%。循环前后生物原油的元素并无太大差异,热值有略微提升。水相有机物主要聚合为固体残渣导致循环后的固体残渣产率是未循环的两倍。固体残渣的碳含量随循环次数增加而增加,氧含量则相反,热值显著增加 | [ |
原料 | 操作条件 | 循环 次数 | 检测出的有机酸 | 回用效果 | 参考文献 |
---|---|---|---|---|---|
白杨木 | 400℃,7.1~11.1h | 3 | N/A | 第1~3批次处理产油率上升,第4批次产率降低。水相中无机物和水溶性有机物随批次累积,灰分沉积率从6.2增长到12.6%。TOC含量从54.1g/L增加到136.2g/L | [ |
玉米秸秆 | 300℃,30min | 3 | 乙酸、丙酸 | 有机酸含量富集,促进酚酮类转化,生物原油产率提高了3.89%,固体产物中碳含量提高了0.8% | [ |
刚毛藻 江蓠 | 350℃,15min | 2 | N/A | 随着循环次数的增加,气体产物和液体产物的总量下降,固体沉积率下降,产油率分别增加了8.1%和8.89% | [ |
干酒糟 | 350℃,20min | 9 | 乙酸、乙酰丙酸、异丁酸、异戊酸 | 当循环第8次的时候,生物原油的产率从39.4%大幅增加到54.5%,同时循环后的水相体积更小,浓度更高。循环9次,生物原油的含氧量降低了52%。TOC和TN的浓度随循环次数逐渐增大 | [ |
海藻-锯末 | 250℃,60min | 1 | 乙酸、2-己酸 | 水相循环后,产油率由11.1%降到了9.2%,固体残渣生成增加,从31.3%~38.9%。通过回用能大幅度消减过程副产物 | [ |
大麦秸秆 | 300℃,15min | 3 | 乳酸,乙酸,2-羟基异丁酸, 2-丁烯二酸,2-羟基-3-甲基戊酸 | 循环3次后,产油率由34.9%增长到38.4%。循环前后生物原油的元素并无太大差异,热值有略微提升。水相有机物主要聚合为固体残渣导致循环后的固体残渣产率是未循环的两倍。固体残渣的碳含量随循环次数增加而增加,氧含量则相反,热值显著增加 | [ |
原料 | 操作条件 | 碳元素 /% | HHV /MJ·kg-1 | 灰分(质量分数) /% | 固体产物特性描述 | 参考文献 |
---|---|---|---|---|---|---|
蓖麻渣 | 300℃,90min | 36.47 | N/A | N/A | 焦炭微观形貌为多孔的小尺寸颗粒,含有无定形炭和涡轮层炭,表层附着了残留矿物质。H/C和O/C比值降低,可作为优质的碳基材料 | [ |
死猪 | 400℃,120min | 17.67 | 21.3 | 0.02 | 猪肉灰分较少,因此固体产物几乎全部是焦炭,碳含量高达65.2%。热值为21.3MJ/kg,与某些煤热值相当。焦炭的比表面积与植物热解碳相当 | [ |
大麦秸秆 | 300℃,15min | 22.3 | 22.43 | N/A | 焦炭含碳率65.50%,具有较高的热值。粗糙多孔表面附着一层纤维素和半纤维素分子间脱水形成的微球,微球和多孔提升了比表面积增加了负载位点。水相循环增强脱水和缩合效应,使微球数量增多 | [ |
团集江蓠 | 350℃,15min | 14.3 | 13.1 | N/A | 大型藻类中的糖类含量较高,通常比微型藻类具有更高的焦炭生成量。由于灰分含量多导致了固体产物产率高 | [ |
滇池蓝藻 | 340℃,60min | N/A | N/A | 77.47 | 固体产物中含碳量低,主要成分是灰分,Al、Fe、Si、Ca是含量最多的元素。较多的灰分降低了固体产物的热值 | [ |
锯末-藻 | 250℃,60min | 16.6 | 16.2 | 7.67 | 使用藻类和锯末共液化,随着藻类的添加,固体残渣中C、H及热值均下降,N、O则相反 | [ |
小球藻 | 280℃,30min | N/A | N/A | N/A | 在催化剂作用下,原料中的P在Ca、Mg的作用下形成固体沉淀沉积在固体产物中促进了P的回收。部分碳和无机混合物沉积在催化剂表面和孔道内,使催化剂中毒 | [ |
原料 | 操作条件 | 碳元素 /% | HHV /MJ·kg-1 | 灰分(质量分数) /% | 固体产物特性描述 | 参考文献 |
---|---|---|---|---|---|---|
蓖麻渣 | 300℃,90min | 36.47 | N/A | N/A | 焦炭微观形貌为多孔的小尺寸颗粒,含有无定形炭和涡轮层炭,表层附着了残留矿物质。H/C和O/C比值降低,可作为优质的碳基材料 | [ |
死猪 | 400℃,120min | 17.67 | 21.3 | 0.02 | 猪肉灰分较少,因此固体产物几乎全部是焦炭,碳含量高达65.2%。热值为21.3MJ/kg,与某些煤热值相当。焦炭的比表面积与植物热解碳相当 | [ |
大麦秸秆 | 300℃,15min | 22.3 | 22.43 | N/A | 焦炭含碳率65.50%,具有较高的热值。粗糙多孔表面附着一层纤维素和半纤维素分子间脱水形成的微球,微球和多孔提升了比表面积增加了负载位点。水相循环增强脱水和缩合效应,使微球数量增多 | [ |
团集江蓠 | 350℃,15min | 14.3 | 13.1 | N/A | 大型藻类中的糖类含量较高,通常比微型藻类具有更高的焦炭生成量。由于灰分含量多导致了固体产物产率高 | [ |
滇池蓝藻 | 340℃,60min | N/A | N/A | 77.47 | 固体产物中含碳量低,主要成分是灰分,Al、Fe、Si、Ca是含量最多的元素。较多的灰分降低了固体产物的热值 | [ |
锯末-藻 | 250℃,60min | 16.6 | 16.2 | 7.67 | 使用藻类和锯末共液化,随着藻类的添加,固体残渣中C、H及热值均下降,N、O则相反 | [ |
小球藻 | 280℃,30min | N/A | N/A | N/A | 在催化剂作用下,原料中的P在Ca、Mg的作用下形成固体沉淀沉积在固体产物中促进了P的回收。部分碳和无机混合物沉积在催化剂表面和孔道内,使催化剂中毒 | [ |
原料 | 操作条件 | 气体产物体积分数①/% | 参考文献 | |||
---|---|---|---|---|---|---|
CO2 | CO | CH4 | H2 | |||
白杨木② | 400℃,60min | 60.8~63.6 | 2.7~3.3 | 4.2~4.6 | 28.8~32 | [ |
纤维素 | 380℃,30min,N2 | 5.32 | 11.32 | 0.37 | 15.43 | [ |
380℃,30min,H2 | 6.14 | 9.21 | 3.67 | 80.98 | ||
380℃,30min,CO | 12.63 | 66.94 | 1.74 | 18.69 | ||
甘蔗渣② | 345℃,30min | N/A | N/A | 5.46 | 2.31 | [ |
滇池蓝藻 | 340℃,60min,N2 | 81.43 | N/A | 0.7 | 0.05 | [ |
原料 | 操作条件 | 气体产物体积分数①/% | 参考文献 | |||
---|---|---|---|---|---|---|
CO2 | CO | CH4 | H2 | |||
白杨木② | 400℃,60min | 60.8~63.6 | 2.7~3.3 | 4.2~4.6 | 28.8~32 | [ |
纤维素 | 380℃,30min,N2 | 5.32 | 11.32 | 0.37 | 15.43 | [ |
380℃,30min,H2 | 6.14 | 9.21 | 3.67 | 80.98 | ||
380℃,30min,CO | 12.63 | 66.94 | 1.74 | 18.69 | ||
甘蔗渣② | 345℃,30min | N/A | N/A | 5.46 | 2.31 | [ |
滇池蓝藻 | 340℃,60min,N2 | 81.43 | N/A | 0.7 | 0.05 | [ |
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