For Finland, carbon dioxide mineralisation was identified as the only option for CCS （carbon capture and storage） application. Unfortunately it has not been embraced by the power sector. One interesting source-sink ...For Finland, carbon dioxide mineralisation was identified as the only option for CCS （carbon capture and storage） application. Unfortunately it has not been embraced by the power sector. One interesting source-sink combination, however, is formed by magnesium silicate resources at Vammala, located -85 km east of the 565 MWe coal-fired Meri-Pori Power Plant on the country＇s southwest coast. This paper assesses mineral sequestration of Meri-Pori power plant CO2, using Vammala mineral resources and the mineralisation process under development at Abo Akademi University. That process implies Mg（OH）E production from magnesium silicate-based rock, followed by gas/solid carbonation of the Mg（OH）2 in a pressurised fluidised bed. Reported are results on experimental work, i.e., Mg（OH）2 production, with rock from locations close to Meri-Pori. Results suggest a total CO2 fixation capacity -50 Mt CO2 for the Vammala site, although production of Mg（OH）2 from rock from the site is challenging. Finally, as mineralisation could be directly applied to flue gases without CO2 pre-capture, we report from experimental work on carbonation of Mg（OH）2 with CO2 and CO2-SO2-O2 gas mixtures. Results show that SO2 readily reacts with Mg（OH）2, providing an opportunity to simultaneously capture SO2 and CO2, which could make separate flue gas desulphurisation redundant.展开更多
In order to reuse the high sulfur petroleum coke, the waste in chemical industry, as fuel of power plant for energy recovery, the combustion property of petroleum coke was researched experimentally in circulating flui...In order to reuse the high sulfur petroleum coke, the waste in chemical industry, as fuel of power plant for energy recovery, the combustion property of petroleum coke was researched experimentally in circulating fluidized bed (CFB) boiler. The performance of the boiler in burning mixed fuel with different ratios of coal to petroleum coke is obtained. Based on the experimental data, Factors influencing the stability of combustion,thermal efficiency of boiler, and emissions and desulphurisation are discussed. This study demonstrates that the combustion of petroleum coke in CFB boiler is applicable, and has great significance on the design and operation of CFB boiler to burn petroleum coke.展开更多
The crystal structure of a (3-phenylureido)-a (2, 4-dichlorophenyl)methyl phenylphosphinic acid, C20H17Cl2N2O3P, Mr= 435. 25,which was obtained bydesulphurisation of cis-3, 4-dipheny1-5- (2, 4-dichlorophenyl ) -1, 3, ...The crystal structure of a (3-phenylureido)-a (2, 4-dichlorophenyl)methyl phenylphosphinic acid, C20H17Cl2N2O3P, Mr= 435. 25,which was obtained bydesulphurisation of cis-3, 4-dipheny1-5- (2, 4-dichlorophenyl ) -1, 3, 4-diazaphospholidin2-thione-4-oxide utilizing Ag+ -H2O system in a yield of 89%, is reported. It crystallizes in orthorhombic space group Pca21 with a= 11. 286(2), b= 20. 601 (4) f c=8. 695(2)A, V= 2021 (1) A3, Z= 4, D.= 1. 430 g/cm3, p=4. 21 cm-1, F(000) =896.The final R factor is 0. 040 and Rw is 0. 045 for 946 unique observed reflections[I>3a(I)]. The result of X-ray analysis indicates that the molecules in the crystal are linkedtogether by the O(3 ) ...H (2d) - N (2d ) intermolecular hydrogen-bondings.展开更多
At combustion of hospital waste numerous harmful pollutants were formed inclusive persistent PCDD/F （polychlorinated dibenzodioxines and dibenzofuranes） compounds. To eliminate these substances an existing incinerat...At combustion of hospital waste numerous harmful pollutants were formed inclusive persistent PCDD/F （polychlorinated dibenzodioxines and dibenzofuranes） compounds. To eliminate these substances an existing incinerator consisting of the furnace heat exchanger with flue gas cleaning was used. This incinerator had a capacity of 250 kg of waste per hour. Elimination od acid gases was executed by dosing of solid sorbents （calcium hydrate and bicarbonate） at two points of the waste gases duct. Local temperatures of waste gases at these two points were different. Sorbents were dosed at different distances from the textile filter by which ash and sorbent were separated from the stream of waste gases. By this arrangement it was possible to alter the residence time of sorbents in waste gases. The effect of addition of bicarbonate on dechlorination and desulphurisation was also studied. The executed experiments indicated that at dosing of calcium hydroxide into waste gases at higher temperatures sulphur oxides reacted preferably to hydrogen chloride. The strong effect of HCI in waste gases on formation of PCDD/F was proved. For sufficient elimination of persistent compounds from waste gases it was necessary to add beside calcium hydrate also active carbon. Two types of sorbents based on carbon were tested, namely Norit and Chezacarb B. Both were macroporous. Chezacarb B was carbon black from the process of hydrogen production by partial oxidation. Efficiency of both sorbents for removal of PCDD/F was similar.展开更多
文摘For Finland, carbon dioxide mineralisation was identified as the only option for CCS （carbon capture and storage） application. Unfortunately it has not been embraced by the power sector. One interesting source-sink combination, however, is formed by magnesium silicate resources at Vammala, located -85 km east of the 565 MWe coal-fired Meri-Pori Power Plant on the country＇s southwest coast. This paper assesses mineral sequestration of Meri-Pori power plant CO2, using Vammala mineral resources and the mineralisation process under development at Abo Akademi University. That process implies Mg（OH）E production from magnesium silicate-based rock, followed by gas/solid carbonation of the Mg（OH）2 in a pressurised fluidised bed. Reported are results on experimental work, i.e., Mg（OH）2 production, with rock from locations close to Meri-Pori. Results suggest a total CO2 fixation capacity -50 Mt CO2 for the Vammala site, although production of Mg（OH）2 from rock from the site is challenging. Finally, as mineralisation could be directly applied to flue gases without CO2 pre-capture, we report from experimental work on carbonation of Mg（OH）2 with CO2 and CO2-SO2-O2 gas mixtures. Results show that SO2 readily reacts with Mg（OH）2, providing an opportunity to simultaneously capture SO2 and CO2, which could make separate flue gas desulphurisation redundant.
文摘In order to reuse the high sulfur petroleum coke, the waste in chemical industry, as fuel of power plant for energy recovery, the combustion property of petroleum coke was researched experimentally in circulating fluidized bed (CFB) boiler. The performance of the boiler in burning mixed fuel with different ratios of coal to petroleum coke is obtained. Based on the experimental data, Factors influencing the stability of combustion,thermal efficiency of boiler, and emissions and desulphurisation are discussed. This study demonstrates that the combustion of petroleum coke in CFB boiler is applicable, and has great significance on the design and operation of CFB boiler to burn petroleum coke.
文摘The crystal structure of a (3-phenylureido)-a (2, 4-dichlorophenyl)methyl phenylphosphinic acid, C20H17Cl2N2O3P, Mr= 435. 25,which was obtained bydesulphurisation of cis-3, 4-dipheny1-5- (2, 4-dichlorophenyl ) -1, 3, 4-diazaphospholidin2-thione-4-oxide utilizing Ag+ -H2O system in a yield of 89%, is reported. It crystallizes in orthorhombic space group Pca21 with a= 11. 286(2), b= 20. 601 (4) f c=8. 695(2)A, V= 2021 (1) A3, Z= 4, D.= 1. 430 g/cm3, p=4. 21 cm-1, F(000) =896.The final R factor is 0. 040 and Rw is 0. 045 for 946 unique observed reflections[I>3a(I)]. The result of X-ray analysis indicates that the molecules in the crystal are linkedtogether by the O(3 ) ...H (2d) - N (2d ) intermolecular hydrogen-bondings.
文摘At combustion of hospital waste numerous harmful pollutants were formed inclusive persistent PCDD/F （polychlorinated dibenzodioxines and dibenzofuranes） compounds. To eliminate these substances an existing incinerator consisting of the furnace heat exchanger with flue gas cleaning was used. This incinerator had a capacity of 250 kg of waste per hour. Elimination od acid gases was executed by dosing of solid sorbents （calcium hydrate and bicarbonate） at two points of the waste gases duct. Local temperatures of waste gases at these two points were different. Sorbents were dosed at different distances from the textile filter by which ash and sorbent were separated from the stream of waste gases. By this arrangement it was possible to alter the residence time of sorbents in waste gases. The effect of addition of bicarbonate on dechlorination and desulphurisation was also studied. The executed experiments indicated that at dosing of calcium hydroxide into waste gases at higher temperatures sulphur oxides reacted preferably to hydrogen chloride. The strong effect of HCI in waste gases on formation of PCDD/F was proved. For sufficient elimination of persistent compounds from waste gases it was necessary to add beside calcium hydrate also active carbon. Two types of sorbents based on carbon were tested, namely Norit and Chezacarb B. Both were macroporous. Chezacarb B was carbon black from the process of hydrogen production by partial oxidation. Efficiency of both sorbents for removal of PCDD/F was similar.
