Supercritical water gasification of beet residues: From batch to continuous reactor
A residue obtained after the distillation of agricultural alcohol called beet residues is gasified in supercritical water to form a mixture of fuel gas. A parametric study and thermodynamic calculations are first proposed in batch reactor. The results show a significant effect of temperature on the...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Ondze, Félicité [verfasserIn] |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2015transfer abstract |
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| Umfang: |
9 |
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| Übergeordnetes Werk: |
Enthalten in: Plasticity in responses to dimensional variations of soil space in 19 grassland plant species - Dong, Ran ELSEVIER, 2022, Amsterdam [u.a.] |
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| Übergeordnetes Werk: |
volume:123 ; year:2015 ; day:17 ; month:02 ; pages:350-358 ; extent:9 |
| Links: |
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| DOI / URN: |
10.1016/j.ces.2014.11.026 |
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| 520 | |a A residue obtained after the distillation of agricultural alcohol called beet residues is gasified in supercritical water to form a mixture of fuel gas. A parametric study and thermodynamic calculations are first proposed in batch reactor. The results show a significant effect of temperature on the overall mass yields. Gasification efficiencies range from 0.60 to 0.90gg−1 when temperature increases from 450 to 600°C. The gas low heating value increases under these conditions from 7.4 to 13.2MJkg−1 of initial dry feedstock. After that, a continuous system designed for hydrothermal oxidation processes has been used. For supercritical water gasification, the reduction of total organic carbon in the liquid effluent output presents a little variation, between 59 and 69%, when the operating conditions are changed. To increase the reaction temperature, supercritical water partial oxidation has been conducted. The highest carbon gasification yield is obtained for the highest equivalent molar ratio, indicating a great interest of partial oxidation. Moreover, the results indicate that this process configuration accepts biomass flow variations without influencing the global efficiency. | ||
| 520 | |a A residue obtained after the distillation of agricultural alcohol called beet residues is gasified in supercritical water to form a mixture of fuel gas. A parametric study and thermodynamic calculations are first proposed in batch reactor. The results show a significant effect of temperature on the overall mass yields. Gasification efficiencies range from 0.60 to 0.90gg−1 when temperature increases from 450 to 600°C. The gas low heating value increases under these conditions from 7.4 to 13.2MJkg−1 of initial dry feedstock. After that, a continuous system designed for hydrothermal oxidation processes has been used. For supercritical water gasification, the reduction of total organic carbon in the liquid effluent output presents a little variation, between 59 and 69%, when the operating conditions are changed. To increase the reaction temperature, supercritical water partial oxidation has been conducted. The highest carbon gasification yield is obtained for the highest equivalent molar ratio, indicating a great interest of partial oxidation. Moreover, the results indicate that this process configuration accepts biomass flow variations without influencing the global efficiency. | ||
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10.1016/j.ces.2014.11.026 doi GBV00000000000212A.pica (DE-627)ELV018836720 (ELSEVIER)S0009-2509(14)00678-2 DE-627 ger DE-627 rakwb eng 660 660 DE-600 570 630 VZ BIODIV DE-30 fid Ondze, Félicité verfasserin aut Supercritical water gasification of beet residues: From batch to continuous reactor 2015transfer abstract 9 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier A residue obtained after the distillation of agricultural alcohol called beet residues is gasified in supercritical water to form a mixture of fuel gas. A parametric study and thermodynamic calculations are first proposed in batch reactor. The results show a significant effect of temperature on the overall mass yields. Gasification efficiencies range from 0.60 to 0.90gg−1 when temperature increases from 450 to 600°C. The gas low heating value increases under these conditions from 7.4 to 13.2MJkg−1 of initial dry feedstock. After that, a continuous system designed for hydrothermal oxidation processes has been used. For supercritical water gasification, the reduction of total organic carbon in the liquid effluent output presents a little variation, between 59 and 69%, when the operating conditions are changed. To increase the reaction temperature, supercritical water partial oxidation has been conducted. The highest carbon gasification yield is obtained for the highest equivalent molar ratio, indicating a great interest of partial oxidation. Moreover, the results indicate that this process configuration accepts biomass flow variations without influencing the global efficiency. A residue obtained after the distillation of agricultural alcohol called beet residues is gasified in supercritical water to form a mixture of fuel gas. A parametric study and thermodynamic calculations are first proposed in batch reactor. The results show a significant effect of temperature on the overall mass yields. Gasification efficiencies range from 0.60 to 0.90gg−1 when temperature increases from 450 to 600°C. The gas low heating value increases under these conditions from 7.4 to 13.2MJkg−1 of initial dry feedstock. After that, a continuous system designed for hydrothermal oxidation processes has been used. For supercritical water gasification, the reduction of total organic carbon in the liquid effluent output presents a little variation, between 59 and 69%, when the operating conditions are changed. To increase the reaction temperature, supercritical water partial oxidation has been conducted. The highest carbon gasification yield is obtained for the highest equivalent molar ratio, indicating a great interest of partial oxidation. Moreover, the results indicate that this process configuration accepts biomass flow variations without influencing the global efficiency. TCD Elsevier SCWG Elsevier SCWPO Elsevier TOC Elsevier LHV Elsevier ER Elsevier SCWO Elsevier Boutin, Olivier oth Ruiz, Jean-Christophe oth Ferrasse, Jean-Henry oth Charton, Frédéric oth Enthalten in Elsevier Science Dong, Ran ELSEVIER Plasticity in responses to dimensional variations of soil space in 19 grassland plant species 2022 Amsterdam [u.a.] (DE-627)ELV008347182 volume:123 year:2015 day:17 month:02 pages:350-358 extent:9 https://doi.org/10.1016/j.ces.2014.11.026 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U FID-BIODIV SSG-OLC-PHA AR 123 2015 17 0217 350-358 9 045F 660 |
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10.1016/j.ces.2014.11.026 doi GBV00000000000212A.pica (DE-627)ELV018836720 (ELSEVIER)S0009-2509(14)00678-2 DE-627 ger DE-627 rakwb eng 660 660 DE-600 570 630 VZ BIODIV DE-30 fid Ondze, Félicité verfasserin aut Supercritical water gasification of beet residues: From batch to continuous reactor 2015transfer abstract 9 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier A residue obtained after the distillation of agricultural alcohol called beet residues is gasified in supercritical water to form a mixture of fuel gas. A parametric study and thermodynamic calculations are first proposed in batch reactor. The results show a significant effect of temperature on the overall mass yields. Gasification efficiencies range from 0.60 to 0.90gg−1 when temperature increases from 450 to 600°C. The gas low heating value increases under these conditions from 7.4 to 13.2MJkg−1 of initial dry feedstock. After that, a continuous system designed for hydrothermal oxidation processes has been used. For supercritical water gasification, the reduction of total organic carbon in the liquid effluent output presents a little variation, between 59 and 69%, when the operating conditions are changed. To increase the reaction temperature, supercritical water partial oxidation has been conducted. The highest carbon gasification yield is obtained for the highest equivalent molar ratio, indicating a great interest of partial oxidation. Moreover, the results indicate that this process configuration accepts biomass flow variations without influencing the global efficiency. A residue obtained after the distillation of agricultural alcohol called beet residues is gasified in supercritical water to form a mixture of fuel gas. A parametric study and thermodynamic calculations are first proposed in batch reactor. The results show a significant effect of temperature on the overall mass yields. Gasification efficiencies range from 0.60 to 0.90gg−1 when temperature increases from 450 to 600°C. The gas low heating value increases under these conditions from 7.4 to 13.2MJkg−1 of initial dry feedstock. After that, a continuous system designed for hydrothermal oxidation processes has been used. For supercritical water gasification, the reduction of total organic carbon in the liquid effluent output presents a little variation, between 59 and 69%, when the operating conditions are changed. To increase the reaction temperature, supercritical water partial oxidation has been conducted. The highest carbon gasification yield is obtained for the highest equivalent molar ratio, indicating a great interest of partial oxidation. Moreover, the results indicate that this process configuration accepts biomass flow variations without influencing the global efficiency. TCD Elsevier SCWG Elsevier SCWPO Elsevier TOC Elsevier LHV Elsevier ER Elsevier SCWO Elsevier Boutin, Olivier oth Ruiz, Jean-Christophe oth Ferrasse, Jean-Henry oth Charton, Frédéric oth Enthalten in Elsevier Science Dong, Ran ELSEVIER Plasticity in responses to dimensional variations of soil space in 19 grassland plant species 2022 Amsterdam [u.a.] (DE-627)ELV008347182 volume:123 year:2015 day:17 month:02 pages:350-358 extent:9 https://doi.org/10.1016/j.ces.2014.11.026 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U FID-BIODIV SSG-OLC-PHA AR 123 2015 17 0217 350-358 9 045F 660 |
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10.1016/j.ces.2014.11.026 doi GBV00000000000212A.pica (DE-627)ELV018836720 (ELSEVIER)S0009-2509(14)00678-2 DE-627 ger DE-627 rakwb eng 660 660 DE-600 570 630 VZ BIODIV DE-30 fid Ondze, Félicité verfasserin aut Supercritical water gasification of beet residues: From batch to continuous reactor 2015transfer abstract 9 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier A residue obtained after the distillation of agricultural alcohol called beet residues is gasified in supercritical water to form a mixture of fuel gas. A parametric study and thermodynamic calculations are first proposed in batch reactor. The results show a significant effect of temperature on the overall mass yields. Gasification efficiencies range from 0.60 to 0.90gg−1 when temperature increases from 450 to 600°C. The gas low heating value increases under these conditions from 7.4 to 13.2MJkg−1 of initial dry feedstock. After that, a continuous system designed for hydrothermal oxidation processes has been used. For supercritical water gasification, the reduction of total organic carbon in the liquid effluent output presents a little variation, between 59 and 69%, when the operating conditions are changed. To increase the reaction temperature, supercritical water partial oxidation has been conducted. The highest carbon gasification yield is obtained for the highest equivalent molar ratio, indicating a great interest of partial oxidation. Moreover, the results indicate that this process configuration accepts biomass flow variations without influencing the global efficiency. A residue obtained after the distillation of agricultural alcohol called beet residues is gasified in supercritical water to form a mixture of fuel gas. A parametric study and thermodynamic calculations are first proposed in batch reactor. The results show a significant effect of temperature on the overall mass yields. Gasification efficiencies range from 0.60 to 0.90gg−1 when temperature increases from 450 to 600°C. The gas low heating value increases under these conditions from 7.4 to 13.2MJkg−1 of initial dry feedstock. After that, a continuous system designed for hydrothermal oxidation processes has been used. For supercritical water gasification, the reduction of total organic carbon in the liquid effluent output presents a little variation, between 59 and 69%, when the operating conditions are changed. To increase the reaction temperature, supercritical water partial oxidation has been conducted. The highest carbon gasification yield is obtained for the highest equivalent molar ratio, indicating a great interest of partial oxidation. Moreover, the results indicate that this process configuration accepts biomass flow variations without influencing the global efficiency. TCD Elsevier SCWG Elsevier SCWPO Elsevier TOC Elsevier LHV Elsevier ER Elsevier SCWO Elsevier Boutin, Olivier oth Ruiz, Jean-Christophe oth Ferrasse, Jean-Henry oth Charton, Frédéric oth Enthalten in Elsevier Science Dong, Ran ELSEVIER Plasticity in responses to dimensional variations of soil space in 19 grassland plant species 2022 Amsterdam [u.a.] (DE-627)ELV008347182 volume:123 year:2015 day:17 month:02 pages:350-358 extent:9 https://doi.org/10.1016/j.ces.2014.11.026 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U FID-BIODIV SSG-OLC-PHA AR 123 2015 17 0217 350-358 9 045F 660 |
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10.1016/j.ces.2014.11.026 doi GBV00000000000212A.pica (DE-627)ELV018836720 (ELSEVIER)S0009-2509(14)00678-2 DE-627 ger DE-627 rakwb eng 660 660 DE-600 570 630 VZ BIODIV DE-30 fid Ondze, Félicité verfasserin aut Supercritical water gasification of beet residues: From batch to continuous reactor 2015transfer abstract 9 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier A residue obtained after the distillation of agricultural alcohol called beet residues is gasified in supercritical water to form a mixture of fuel gas. A parametric study and thermodynamic calculations are first proposed in batch reactor. The results show a significant effect of temperature on the overall mass yields. Gasification efficiencies range from 0.60 to 0.90gg−1 when temperature increases from 450 to 600°C. The gas low heating value increases under these conditions from 7.4 to 13.2MJkg−1 of initial dry feedstock. After that, a continuous system designed for hydrothermal oxidation processes has been used. For supercritical water gasification, the reduction of total organic carbon in the liquid effluent output presents a little variation, between 59 and 69%, when the operating conditions are changed. To increase the reaction temperature, supercritical water partial oxidation has been conducted. The highest carbon gasification yield is obtained for the highest equivalent molar ratio, indicating a great interest of partial oxidation. Moreover, the results indicate that this process configuration accepts biomass flow variations without influencing the global efficiency. A residue obtained after the distillation of agricultural alcohol called beet residues is gasified in supercritical water to form a mixture of fuel gas. A parametric study and thermodynamic calculations are first proposed in batch reactor. The results show a significant effect of temperature on the overall mass yields. Gasification efficiencies range from 0.60 to 0.90gg−1 when temperature increases from 450 to 600°C. The gas low heating value increases under these conditions from 7.4 to 13.2MJkg−1 of initial dry feedstock. After that, a continuous system designed for hydrothermal oxidation processes has been used. For supercritical water gasification, the reduction of total organic carbon in the liquid effluent output presents a little variation, between 59 and 69%, when the operating conditions are changed. To increase the reaction temperature, supercritical water partial oxidation has been conducted. The highest carbon gasification yield is obtained for the highest equivalent molar ratio, indicating a great interest of partial oxidation. Moreover, the results indicate that this process configuration accepts biomass flow variations without influencing the global efficiency. TCD Elsevier SCWG Elsevier SCWPO Elsevier TOC Elsevier LHV Elsevier ER Elsevier SCWO Elsevier Boutin, Olivier oth Ruiz, Jean-Christophe oth Ferrasse, Jean-Henry oth Charton, Frédéric oth Enthalten in Elsevier Science Dong, Ran ELSEVIER Plasticity in responses to dimensional variations of soil space in 19 grassland plant species 2022 Amsterdam [u.a.] (DE-627)ELV008347182 volume:123 year:2015 day:17 month:02 pages:350-358 extent:9 https://doi.org/10.1016/j.ces.2014.11.026 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U FID-BIODIV SSG-OLC-PHA AR 123 2015 17 0217 350-358 9 045F 660 |
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10.1016/j.ces.2014.11.026 doi GBV00000000000212A.pica (DE-627)ELV018836720 (ELSEVIER)S0009-2509(14)00678-2 DE-627 ger DE-627 rakwb eng 660 660 DE-600 570 630 VZ BIODIV DE-30 fid Ondze, Félicité verfasserin aut Supercritical water gasification of beet residues: From batch to continuous reactor 2015transfer abstract 9 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier A residue obtained after the distillation of agricultural alcohol called beet residues is gasified in supercritical water to form a mixture of fuel gas. A parametric study and thermodynamic calculations are first proposed in batch reactor. The results show a significant effect of temperature on the overall mass yields. Gasification efficiencies range from 0.60 to 0.90gg−1 when temperature increases from 450 to 600°C. The gas low heating value increases under these conditions from 7.4 to 13.2MJkg−1 of initial dry feedstock. After that, a continuous system designed for hydrothermal oxidation processes has been used. For supercritical water gasification, the reduction of total organic carbon in the liquid effluent output presents a little variation, between 59 and 69%, when the operating conditions are changed. To increase the reaction temperature, supercritical water partial oxidation has been conducted. The highest carbon gasification yield is obtained for the highest equivalent molar ratio, indicating a great interest of partial oxidation. Moreover, the results indicate that this process configuration accepts biomass flow variations without influencing the global efficiency. A residue obtained after the distillation of agricultural alcohol called beet residues is gasified in supercritical water to form a mixture of fuel gas. A parametric study and thermodynamic calculations are first proposed in batch reactor. The results show a significant effect of temperature on the overall mass yields. Gasification efficiencies range from 0.60 to 0.90gg−1 when temperature increases from 450 to 600°C. The gas low heating value increases under these conditions from 7.4 to 13.2MJkg−1 of initial dry feedstock. After that, a continuous system designed for hydrothermal oxidation processes has been used. For supercritical water gasification, the reduction of total organic carbon in the liquid effluent output presents a little variation, between 59 and 69%, when the operating conditions are changed. To increase the reaction temperature, supercritical water partial oxidation has been conducted. The highest carbon gasification yield is obtained for the highest equivalent molar ratio, indicating a great interest of partial oxidation. Moreover, the results indicate that this process configuration accepts biomass flow variations without influencing the global efficiency. TCD Elsevier SCWG Elsevier SCWPO Elsevier TOC Elsevier LHV Elsevier ER Elsevier SCWO Elsevier Boutin, Olivier oth Ruiz, Jean-Christophe oth Ferrasse, Jean-Henry oth Charton, Frédéric oth Enthalten in Elsevier Science Dong, Ran ELSEVIER Plasticity in responses to dimensional variations of soil space in 19 grassland plant species 2022 Amsterdam [u.a.] (DE-627)ELV008347182 volume:123 year:2015 day:17 month:02 pages:350-358 extent:9 https://doi.org/10.1016/j.ces.2014.11.026 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U FID-BIODIV SSG-OLC-PHA AR 123 2015 17 0217 350-358 9 045F 660 |
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A parametric study and thermodynamic calculations are first proposed in batch reactor. The results show a significant effect of temperature on the overall mass yields. Gasification efficiencies range from 0.60 to 0.90gg−1 when temperature increases from 450 to 600°C. The gas low heating value increases under these conditions from 7.4 to 13.2MJkg−1 of initial dry feedstock. After that, a continuous system designed for hydrothermal oxidation processes has been used. For supercritical water gasification, the reduction of total organic carbon in the liquid effluent output presents a little variation, between 59 and 69%, when the operating conditions are changed. To increase the reaction temperature, supercritical water partial oxidation has been conducted. The highest carbon gasification yield is obtained for the highest equivalent molar ratio, indicating a great interest of partial oxidation. 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Supercritical water gasification of beet residues: From batch to continuous reactor |
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A residue obtained after the distillation of agricultural alcohol called beet residues is gasified in supercritical water to form a mixture of fuel gas. A parametric study and thermodynamic calculations are first proposed in batch reactor. The results show a significant effect of temperature on the overall mass yields. Gasification efficiencies range from 0.60 to 0.90gg−1 when temperature increases from 450 to 600°C. The gas low heating value increases under these conditions from 7.4 to 13.2MJkg−1 of initial dry feedstock. After that, a continuous system designed for hydrothermal oxidation processes has been used. For supercritical water gasification, the reduction of total organic carbon in the liquid effluent output presents a little variation, between 59 and 69%, when the operating conditions are changed. To increase the reaction temperature, supercritical water partial oxidation has been conducted. The highest carbon gasification yield is obtained for the highest equivalent molar ratio, indicating a great interest of partial oxidation. Moreover, the results indicate that this process configuration accepts biomass flow variations without influencing the global efficiency. |
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A residue obtained after the distillation of agricultural alcohol called beet residues is gasified in supercritical water to form a mixture of fuel gas. A parametric study and thermodynamic calculations are first proposed in batch reactor. The results show a significant effect of temperature on the overall mass yields. Gasification efficiencies range from 0.60 to 0.90gg−1 when temperature increases from 450 to 600°C. The gas low heating value increases under these conditions from 7.4 to 13.2MJkg−1 of initial dry feedstock. After that, a continuous system designed for hydrothermal oxidation processes has been used. For supercritical water gasification, the reduction of total organic carbon in the liquid effluent output presents a little variation, between 59 and 69%, when the operating conditions are changed. To increase the reaction temperature, supercritical water partial oxidation has been conducted. The highest carbon gasification yield is obtained for the highest equivalent molar ratio, indicating a great interest of partial oxidation. Moreover, the results indicate that this process configuration accepts biomass flow variations without influencing the global efficiency. |
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A residue obtained after the distillation of agricultural alcohol called beet residues is gasified in supercritical water to form a mixture of fuel gas. A parametric study and thermodynamic calculations are first proposed in batch reactor. The results show a significant effect of temperature on the overall mass yields. Gasification efficiencies range from 0.60 to 0.90gg−1 when temperature increases from 450 to 600°C. The gas low heating value increases under these conditions from 7.4 to 13.2MJkg−1 of initial dry feedstock. After that, a continuous system designed for hydrothermal oxidation processes has been used. For supercritical water gasification, the reduction of total organic carbon in the liquid effluent output presents a little variation, between 59 and 69%, when the operating conditions are changed. To increase the reaction temperature, supercritical water partial oxidation has been conducted. The highest carbon gasification yield is obtained for the highest equivalent molar ratio, indicating a great interest of partial oxidation. Moreover, the results indicate that this process configuration accepts biomass flow variations without influencing the global efficiency. |
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