Carbon monoxide adsorptive capability of low rank coal’s maceral
Abstract The centrifugal separation with gravity experiment was made for getting every pure macerals like inertinite and vitrinite, and the isothermal adsorption tests of pure maceral are carried out at 30, 40, 50, 55, 60, 65 °C, respectively, after analyzing the proximate, element and maceral of co...
Ausführliche Beschreibung
Autor*in: |
Wang, Yue-hong [verfasserIn] Guo, Li-wen [verfasserIn] Zhang, Jiu-ling [verfasserIn] |
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E-Artikel |
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Sprache: |
Englisch |
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2008 |
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Übergeordnetes Werk: |
Enthalten in: Journal of coal science and engineering, China - Beijing : Springer, 1995, 14(2008), 4 vom: 18. Nov., Seite 678-682 |
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Übergeordnetes Werk: |
volume:14 ; year:2008 ; number:4 ; day:18 ; month:11 ; pages:678-682 |
Links: |
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DOI / URN: |
10.1007/s12404-008-0441-2 |
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Katalog-ID: |
SPR02592690X |
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520 | |a Abstract The centrifugal separation with gravity experiment was made for getting every pure macerals like inertinite and vitrinite, and the isothermal adsorption tests of pure maceral are carried out at 30, 40, 50, 55, 60, 65 °C, respectively, after analyzing the proximate, element and maceral of coal samples, which was aimed to study the CO adsorptive capability of every maceral of low rank coal at difference temperature and pressure. The results show that the adsorption isotherm of CO can be described by Langmuir equation because it belongs to the Type I adsorption isotherm at low temperature(T⩽50 °C), and the temperature effect on coal adsorption is greater than of pressure in lower temperature and pressure area; what’s more, the relationship is linear between the coal adsorption quantity of CO and the pressure at high temperature(T>50 °C), it can be described by Henry equation(Q=KP), which increases with pressure. Both temperature and pressure has great influence on CO adsorptive capability of low rank coals, especially the temperature’s effect is so very complex that the mechanism need to study further. At the same time, the volatile matter, inertinite, oxygen-function groups and negative functional groups are high popularly in low rank coal samples, especially, the content of hydroxide(-OH) has great influence on CO adsorption in that the inertinite has stronger effect than vitrinite on adsorptive capability of low rank coal samples, the result is same to the research on $ CH_{4} $ adsorption. | ||
650 | 4 | |a low rank coal |7 (dpeaa)DE-He213 | |
650 | 4 | |a CO |7 (dpeaa)DE-He213 | |
650 | 4 | |a maceral |7 (dpeaa)DE-He213 | |
650 | 4 | |a adsorption isotherm |7 (dpeaa)DE-He213 | |
650 | 4 | |a spontaneous combustion |7 (dpeaa)DE-He213 | |
700 | 1 | |a Guo, Li-wen |e verfasserin |4 aut | |
700 | 1 | |a Zhang, Jiu-ling |e verfasserin |4 aut | |
773 | 0 | 8 | |i Enthalten in |t Journal of coal science and engineering, China |d Beijing : Springer, 1995 |g 14(2008), 4 vom: 18. Nov., Seite 678-682 |w (DE-627)573095507 |w (DE-600)2440422-6 |x 1866-6566 |7 nnns |
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10.1007/s12404-008-0441-2 doi (DE-627)SPR02592690X (SPR)s12404-008-0441-2-e DE-627 ger DE-627 rakwb eng 550 620 660 ASE 38.51 bkl 57.37 bkl Wang, Yue-hong verfasserin aut Carbon monoxide adsorptive capability of low rank coal’s maceral 2008 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract The centrifugal separation with gravity experiment was made for getting every pure macerals like inertinite and vitrinite, and the isothermal adsorption tests of pure maceral are carried out at 30, 40, 50, 55, 60, 65 °C, respectively, after analyzing the proximate, element and maceral of coal samples, which was aimed to study the CO adsorptive capability of every maceral of low rank coal at difference temperature and pressure. The results show that the adsorption isotherm of CO can be described by Langmuir equation because it belongs to the Type I adsorption isotherm at low temperature(T⩽50 °C), and the temperature effect on coal adsorption is greater than of pressure in lower temperature and pressure area; what’s more, the relationship is linear between the coal adsorption quantity of CO and the pressure at high temperature(T>50 °C), it can be described by Henry equation(Q=KP), which increases with pressure. Both temperature and pressure has great influence on CO adsorptive capability of low rank coals, especially the temperature’s effect is so very complex that the mechanism need to study further. At the same time, the volatile matter, inertinite, oxygen-function groups and negative functional groups are high popularly in low rank coal samples, especially, the content of hydroxide(-OH) has great influence on CO adsorption in that the inertinite has stronger effect than vitrinite on adsorptive capability of low rank coal samples, the result is same to the research on $ CH_{4} $ adsorption. low rank coal (dpeaa)DE-He213 CO (dpeaa)DE-He213 maceral (dpeaa)DE-He213 adsorption isotherm (dpeaa)DE-He213 spontaneous combustion (dpeaa)DE-He213 Guo, Li-wen verfasserin aut Zhang, Jiu-ling verfasserin aut Enthalten in Journal of coal science and engineering, China Beijing : Springer, 1995 14(2008), 4 vom: 18. Nov., Seite 678-682 (DE-627)573095507 (DE-600)2440422-6 1866-6566 nnns volume:14 year:2008 number:4 day:18 month:11 pages:678-682 https://dx.doi.org/10.1007/s12404-008-0441-2 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_20 GBV_ILN_40 GBV_ILN_63 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_110 GBV_ILN_120 GBV_ILN_150 GBV_ILN_161 GBV_ILN_213 GBV_ILN_230 GBV_ILN_293 GBV_ILN_702 GBV_ILN_2005 GBV_ILN_2018 GBV_ILN_2190 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 38.51 ASE 57.37 ASE AR 14 2008 4 18 11 678-682 |
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10.1007/s12404-008-0441-2 doi (DE-627)SPR02592690X (SPR)s12404-008-0441-2-e DE-627 ger DE-627 rakwb eng 550 620 660 ASE 38.51 bkl 57.37 bkl Wang, Yue-hong verfasserin aut Carbon monoxide adsorptive capability of low rank coal’s maceral 2008 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract The centrifugal separation with gravity experiment was made for getting every pure macerals like inertinite and vitrinite, and the isothermal adsorption tests of pure maceral are carried out at 30, 40, 50, 55, 60, 65 °C, respectively, after analyzing the proximate, element and maceral of coal samples, which was aimed to study the CO adsorptive capability of every maceral of low rank coal at difference temperature and pressure. The results show that the adsorption isotherm of CO can be described by Langmuir equation because it belongs to the Type I adsorption isotherm at low temperature(T⩽50 °C), and the temperature effect on coal adsorption is greater than of pressure in lower temperature and pressure area; what’s more, the relationship is linear between the coal adsorption quantity of CO and the pressure at high temperature(T>50 °C), it can be described by Henry equation(Q=KP), which increases with pressure. Both temperature and pressure has great influence on CO adsorptive capability of low rank coals, especially the temperature’s effect is so very complex that the mechanism need to study further. At the same time, the volatile matter, inertinite, oxygen-function groups and negative functional groups are high popularly in low rank coal samples, especially, the content of hydroxide(-OH) has great influence on CO adsorption in that the inertinite has stronger effect than vitrinite on adsorptive capability of low rank coal samples, the result is same to the research on $ CH_{4} $ adsorption. low rank coal (dpeaa)DE-He213 CO (dpeaa)DE-He213 maceral (dpeaa)DE-He213 adsorption isotherm (dpeaa)DE-He213 spontaneous combustion (dpeaa)DE-He213 Guo, Li-wen verfasserin aut Zhang, Jiu-ling verfasserin aut Enthalten in Journal of coal science and engineering, China Beijing : Springer, 1995 14(2008), 4 vom: 18. Nov., Seite 678-682 (DE-627)573095507 (DE-600)2440422-6 1866-6566 nnns volume:14 year:2008 number:4 day:18 month:11 pages:678-682 https://dx.doi.org/10.1007/s12404-008-0441-2 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_20 GBV_ILN_40 GBV_ILN_63 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_110 GBV_ILN_120 GBV_ILN_150 GBV_ILN_161 GBV_ILN_213 GBV_ILN_230 GBV_ILN_293 GBV_ILN_702 GBV_ILN_2005 GBV_ILN_2018 GBV_ILN_2190 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 38.51 ASE 57.37 ASE AR 14 2008 4 18 11 678-682 |
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10.1007/s12404-008-0441-2 doi (DE-627)SPR02592690X (SPR)s12404-008-0441-2-e DE-627 ger DE-627 rakwb eng 550 620 660 ASE 38.51 bkl 57.37 bkl Wang, Yue-hong verfasserin aut Carbon monoxide adsorptive capability of low rank coal’s maceral 2008 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract The centrifugal separation with gravity experiment was made for getting every pure macerals like inertinite and vitrinite, and the isothermal adsorption tests of pure maceral are carried out at 30, 40, 50, 55, 60, 65 °C, respectively, after analyzing the proximate, element and maceral of coal samples, which was aimed to study the CO adsorptive capability of every maceral of low rank coal at difference temperature and pressure. The results show that the adsorption isotherm of CO can be described by Langmuir equation because it belongs to the Type I adsorption isotherm at low temperature(T⩽50 °C), and the temperature effect on coal adsorption is greater than of pressure in lower temperature and pressure area; what’s more, the relationship is linear between the coal adsorption quantity of CO and the pressure at high temperature(T>50 °C), it can be described by Henry equation(Q=KP), which increases with pressure. Both temperature and pressure has great influence on CO adsorptive capability of low rank coals, especially the temperature’s effect is so very complex that the mechanism need to study further. At the same time, the volatile matter, inertinite, oxygen-function groups and negative functional groups are high popularly in low rank coal samples, especially, the content of hydroxide(-OH) has great influence on CO adsorption in that the inertinite has stronger effect than vitrinite on adsorptive capability of low rank coal samples, the result is same to the research on $ CH_{4} $ adsorption. low rank coal (dpeaa)DE-He213 CO (dpeaa)DE-He213 maceral (dpeaa)DE-He213 adsorption isotherm (dpeaa)DE-He213 spontaneous combustion (dpeaa)DE-He213 Guo, Li-wen verfasserin aut Zhang, Jiu-ling verfasserin aut Enthalten in Journal of coal science and engineering, China Beijing : Springer, 1995 14(2008), 4 vom: 18. Nov., Seite 678-682 (DE-627)573095507 (DE-600)2440422-6 1866-6566 nnns volume:14 year:2008 number:4 day:18 month:11 pages:678-682 https://dx.doi.org/10.1007/s12404-008-0441-2 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_20 GBV_ILN_40 GBV_ILN_63 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_110 GBV_ILN_120 GBV_ILN_150 GBV_ILN_161 GBV_ILN_213 GBV_ILN_230 GBV_ILN_293 GBV_ILN_702 GBV_ILN_2005 GBV_ILN_2018 GBV_ILN_2190 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 38.51 ASE 57.37 ASE AR 14 2008 4 18 11 678-682 |
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10.1007/s12404-008-0441-2 doi (DE-627)SPR02592690X (SPR)s12404-008-0441-2-e DE-627 ger DE-627 rakwb eng 550 620 660 ASE 38.51 bkl 57.37 bkl Wang, Yue-hong verfasserin aut Carbon monoxide adsorptive capability of low rank coal’s maceral 2008 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract The centrifugal separation with gravity experiment was made for getting every pure macerals like inertinite and vitrinite, and the isothermal adsorption tests of pure maceral are carried out at 30, 40, 50, 55, 60, 65 °C, respectively, after analyzing the proximate, element and maceral of coal samples, which was aimed to study the CO adsorptive capability of every maceral of low rank coal at difference temperature and pressure. The results show that the adsorption isotherm of CO can be described by Langmuir equation because it belongs to the Type I adsorption isotherm at low temperature(T⩽50 °C), and the temperature effect on coal adsorption is greater than of pressure in lower temperature and pressure area; what’s more, the relationship is linear between the coal adsorption quantity of CO and the pressure at high temperature(T>50 °C), it can be described by Henry equation(Q=KP), which increases with pressure. Both temperature and pressure has great influence on CO adsorptive capability of low rank coals, especially the temperature’s effect is so very complex that the mechanism need to study further. At the same time, the volatile matter, inertinite, oxygen-function groups and negative functional groups are high popularly in low rank coal samples, especially, the content of hydroxide(-OH) has great influence on CO adsorption in that the inertinite has stronger effect than vitrinite on adsorptive capability of low rank coal samples, the result is same to the research on $ CH_{4} $ adsorption. low rank coal (dpeaa)DE-He213 CO (dpeaa)DE-He213 maceral (dpeaa)DE-He213 adsorption isotherm (dpeaa)DE-He213 spontaneous combustion (dpeaa)DE-He213 Guo, Li-wen verfasserin aut Zhang, Jiu-ling verfasserin aut Enthalten in Journal of coal science and engineering, China Beijing : Springer, 1995 14(2008), 4 vom: 18. Nov., Seite 678-682 (DE-627)573095507 (DE-600)2440422-6 1866-6566 nnns volume:14 year:2008 number:4 day:18 month:11 pages:678-682 https://dx.doi.org/10.1007/s12404-008-0441-2 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_20 GBV_ILN_40 GBV_ILN_63 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_110 GBV_ILN_120 GBV_ILN_150 GBV_ILN_161 GBV_ILN_213 GBV_ILN_230 GBV_ILN_293 GBV_ILN_702 GBV_ILN_2005 GBV_ILN_2018 GBV_ILN_2190 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 38.51 ASE 57.37 ASE AR 14 2008 4 18 11 678-682 |
allfieldsSound |
10.1007/s12404-008-0441-2 doi (DE-627)SPR02592690X (SPR)s12404-008-0441-2-e DE-627 ger DE-627 rakwb eng 550 620 660 ASE 38.51 bkl 57.37 bkl Wang, Yue-hong verfasserin aut Carbon monoxide adsorptive capability of low rank coal’s maceral 2008 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract The centrifugal separation with gravity experiment was made for getting every pure macerals like inertinite and vitrinite, and the isothermal adsorption tests of pure maceral are carried out at 30, 40, 50, 55, 60, 65 °C, respectively, after analyzing the proximate, element and maceral of coal samples, which was aimed to study the CO adsorptive capability of every maceral of low rank coal at difference temperature and pressure. The results show that the adsorption isotherm of CO can be described by Langmuir equation because it belongs to the Type I adsorption isotherm at low temperature(T⩽50 °C), and the temperature effect on coal adsorption is greater than of pressure in lower temperature and pressure area; what’s more, the relationship is linear between the coal adsorption quantity of CO and the pressure at high temperature(T>50 °C), it can be described by Henry equation(Q=KP), which increases with pressure. Both temperature and pressure has great influence on CO adsorptive capability of low rank coals, especially the temperature’s effect is so very complex that the mechanism need to study further. At the same time, the volatile matter, inertinite, oxygen-function groups and negative functional groups are high popularly in low rank coal samples, especially, the content of hydroxide(-OH) has great influence on CO adsorption in that the inertinite has stronger effect than vitrinite on adsorptive capability of low rank coal samples, the result is same to the research on $ CH_{4} $ adsorption. low rank coal (dpeaa)DE-He213 CO (dpeaa)DE-He213 maceral (dpeaa)DE-He213 adsorption isotherm (dpeaa)DE-He213 spontaneous combustion (dpeaa)DE-He213 Guo, Li-wen verfasserin aut Zhang, Jiu-ling verfasserin aut Enthalten in Journal of coal science and engineering, China Beijing : Springer, 1995 14(2008), 4 vom: 18. Nov., Seite 678-682 (DE-627)573095507 (DE-600)2440422-6 1866-6566 nnns volume:14 year:2008 number:4 day:18 month:11 pages:678-682 https://dx.doi.org/10.1007/s12404-008-0441-2 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_20 GBV_ILN_40 GBV_ILN_63 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_110 GBV_ILN_120 GBV_ILN_150 GBV_ILN_161 GBV_ILN_213 GBV_ILN_230 GBV_ILN_293 GBV_ILN_702 GBV_ILN_2005 GBV_ILN_2018 GBV_ILN_2190 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 38.51 ASE 57.37 ASE AR 14 2008 4 18 11 678-682 |
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The results show that the adsorption isotherm of CO can be described by Langmuir equation because it belongs to the Type I adsorption isotherm at low temperature(T⩽50 °C), and the temperature effect on coal adsorption is greater than of pressure in lower temperature and pressure area; what’s more, the relationship is linear between the coal adsorption quantity of CO and the pressure at high temperature(T>50 °C), it can be described by Henry equation(Q=KP), which increases with pressure. Both temperature and pressure has great influence on CO adsorptive capability of low rank coals, especially the temperature’s effect is so very complex that the mechanism need to study further. 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Wang, Yue-hong |
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Wang, Yue-hong ddc 550 bkl 38.51 bkl 57.37 misc low rank coal misc CO misc maceral misc adsorption isotherm misc spontaneous combustion Carbon monoxide adsorptive capability of low rank coal’s maceral |
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550 620 660 ASE 38.51 bkl 57.37 bkl Carbon monoxide adsorptive capability of low rank coal’s maceral low rank coal (dpeaa)DE-He213 CO (dpeaa)DE-He213 maceral (dpeaa)DE-He213 adsorption isotherm (dpeaa)DE-He213 spontaneous combustion (dpeaa)DE-He213 |
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ddc 550 bkl 38.51 bkl 57.37 misc low rank coal misc CO misc maceral misc adsorption isotherm misc spontaneous combustion |
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Carbon monoxide adsorptive capability of low rank coal’s maceral |
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carbon monoxide adsorptive capability of low rank coal’s maceral |
title_auth |
Carbon monoxide adsorptive capability of low rank coal’s maceral |
abstract |
Abstract The centrifugal separation with gravity experiment was made for getting every pure macerals like inertinite and vitrinite, and the isothermal adsorption tests of pure maceral are carried out at 30, 40, 50, 55, 60, 65 °C, respectively, after analyzing the proximate, element and maceral of coal samples, which was aimed to study the CO adsorptive capability of every maceral of low rank coal at difference temperature and pressure. The results show that the adsorption isotherm of CO can be described by Langmuir equation because it belongs to the Type I adsorption isotherm at low temperature(T⩽50 °C), and the temperature effect on coal adsorption is greater than of pressure in lower temperature and pressure area; what’s more, the relationship is linear between the coal adsorption quantity of CO and the pressure at high temperature(T>50 °C), it can be described by Henry equation(Q=KP), which increases with pressure. Both temperature and pressure has great influence on CO adsorptive capability of low rank coals, especially the temperature’s effect is so very complex that the mechanism need to study further. At the same time, the volatile matter, inertinite, oxygen-function groups and negative functional groups are high popularly in low rank coal samples, especially, the content of hydroxide(-OH) has great influence on CO adsorption in that the inertinite has stronger effect than vitrinite on adsorptive capability of low rank coal samples, the result is same to the research on $ CH_{4} $ adsorption. |
abstractGer |
Abstract The centrifugal separation with gravity experiment was made for getting every pure macerals like inertinite and vitrinite, and the isothermal adsorption tests of pure maceral are carried out at 30, 40, 50, 55, 60, 65 °C, respectively, after analyzing the proximate, element and maceral of coal samples, which was aimed to study the CO adsorptive capability of every maceral of low rank coal at difference temperature and pressure. The results show that the adsorption isotherm of CO can be described by Langmuir equation because it belongs to the Type I adsorption isotherm at low temperature(T⩽50 °C), and the temperature effect on coal adsorption is greater than of pressure in lower temperature and pressure area; what’s more, the relationship is linear between the coal adsorption quantity of CO and the pressure at high temperature(T>50 °C), it can be described by Henry equation(Q=KP), which increases with pressure. Both temperature and pressure has great influence on CO adsorptive capability of low rank coals, especially the temperature’s effect is so very complex that the mechanism need to study further. At the same time, the volatile matter, inertinite, oxygen-function groups and negative functional groups are high popularly in low rank coal samples, especially, the content of hydroxide(-OH) has great influence on CO adsorption in that the inertinite has stronger effect than vitrinite on adsorptive capability of low rank coal samples, the result is same to the research on $ CH_{4} $ adsorption. |
abstract_unstemmed |
Abstract The centrifugal separation with gravity experiment was made for getting every pure macerals like inertinite and vitrinite, and the isothermal adsorption tests of pure maceral are carried out at 30, 40, 50, 55, 60, 65 °C, respectively, after analyzing the proximate, element and maceral of coal samples, which was aimed to study the CO adsorptive capability of every maceral of low rank coal at difference temperature and pressure. The results show that the adsorption isotherm of CO can be described by Langmuir equation because it belongs to the Type I adsorption isotherm at low temperature(T⩽50 °C), and the temperature effect on coal adsorption is greater than of pressure in lower temperature and pressure area; what’s more, the relationship is linear between the coal adsorption quantity of CO and the pressure at high temperature(T>50 °C), it can be described by Henry equation(Q=KP), which increases with pressure. Both temperature and pressure has great influence on CO adsorptive capability of low rank coals, especially the temperature’s effect is so very complex that the mechanism need to study further. At the same time, the volatile matter, inertinite, oxygen-function groups and negative functional groups are high popularly in low rank coal samples, especially, the content of hydroxide(-OH) has great influence on CO adsorption in that the inertinite has stronger effect than vitrinite on adsorptive capability of low rank coal samples, the result is same to the research on $ CH_{4} $ adsorption. |
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Carbon monoxide adsorptive capability of low rank coal’s maceral |
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The results show that the adsorption isotherm of CO can be described by Langmuir equation because it belongs to the Type I adsorption isotherm at low temperature(T⩽50 °C), and the temperature effect on coal adsorption is greater than of pressure in lower temperature and pressure area; what’s more, the relationship is linear between the coal adsorption quantity of CO and the pressure at high temperature(T>50 °C), it can be described by Henry equation(Q=KP), which increases with pressure. Both temperature and pressure has great influence on CO adsorptive capability of low rank coals, especially the temperature’s effect is so very complex that the mechanism need to study further. At the same time, the volatile matter, inertinite, oxygen-function groups and negative functional groups are high popularly in low rank coal samples, especially, the content of hydroxide(-OH) has great influence on CO adsorption in that the inertinite has stronger effect than vitrinite on adsorptive capability of low rank coal samples, the result is same to the research on $ CH_{4} $ adsorption.</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">low rank coal</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">CO</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">maceral</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">adsorption isotherm</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">spontaneous combustion</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Guo, Li-wen</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Zhang, Jiu-ling</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">Enthalten in</subfield><subfield code="t">Journal of coal science and engineering, China</subfield><subfield code="d">Beijing : Springer, 1995</subfield><subfield code="g">14(2008), 4 vom: 18. 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