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Roles of Bioenergy and Green Hydrogen in Large Scale Energy Storage for Carbon Neutrality 被引量:1
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作者 chunbao xu 《Engineering》 SCIE EI CAS CSCD 2023年第10期32-34,共3页
1.Roles of biomass and bioenergy in solar energy storage Biomass comprises plant-based material,for example,wood,microalgae,energy crops,and agro-forestry residues,as well as organic waste from industries,farms,and ho... 1.Roles of biomass and bioenergy in solar energy storage Biomass comprises plant-based material,for example,wood,microalgae,energy crops,and agro-forestry residues,as well as organic waste from industries,farms,and households,and plays a key role in solar energy capture and storage. 展开更多
关键词 CROPS ENERGY STORAGE
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Microwave-assisted pyrolysis of plastics for aviation oil production:energy and economic analyses
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作者 Sichen Fan Yifan Liu +2 位作者 Yaning Zhang Wenke Zhao chunbao xu 《Frontiers of Chemical Science and Engineering》 SCIE EI CSCD 2024年第7期141-153,共13页
Microwave-assisted pyrolysis is an effective method for recycling plastic wastes into oils that can be used for aviation fuels. In this study, energy and economic analyses of aviation oil production from microwave-ass... Microwave-assisted pyrolysis is an effective method for recycling plastic wastes into oils that can be used for aviation fuels. In this study, energy and economic analyses of aviation oil production from microwave-assisted pyrolysis of polystyrene were performed. The total energy efficiency, recovered energy efficiency, unitary cost, unitary energy economic cost, relative cost difference, and energy economic factor were detailed. And the effects of microwave power, pyrolysis temperature, microwave absorbent loading, and microwave absorbent type on these parameters were covered. It was found that pyrolysis temperature has the most significant effect on the unitary cost and unitary energy economic cost of aviation oil, and-microwave absorbent type has a significant influence on energy economic factor during the whole microwave-assisted pyrolysis process. The optimum reaction conditions at the tonnage system for pyrolysis of 1 t polystyrene were microwave power of 650 W, pyrolysis temperature of 460 ℃, and silicon carbide (microwave absorbent) at a loading of 2 t (twice than feedstock loading). At these optimal conditions, the total energy efficiency, recovered energy efficiency, unitary cost, unitary energy economic cost, relative cost difference, and energy economic factor were 62.78%, 96.51%, 3.21 × 10^(4) yuan·t^(-1), 779 yuan·GJ^(-1), 1.49, and 71.02%, respectively. 展开更多
关键词 energy analysis economic analysis microwave-assisted pyrolysis POLYSTYRENE aviation oil
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EFFECTS OF GAS TYPE AND TEMPERATURE ON FINE PARTICLE FLUIDIZATION 被引量:6
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作者 chunbao xu J.-X. Zhu 《China Particuology》 SCIE EI CAS CSCD 2006年第3期114-121,共8页
The influence of gas type (helium and argon) and bed temperature (77-473 K) on the fluidization behaviour of Geldart groups C and A particles was investigated. For both types of particles tested, i.e., Al2O3 (4.8... The influence of gas type (helium and argon) and bed temperature (77-473 K) on the fluidization behaviour of Geldart groups C and A particles was investigated. For both types of particles tested, i.e., Al2O3 (4.8μm) and glass beads (39 μm), the fluidization quality in different gases shows the following priority sequence: Ar 〉 He. In the same gaseous atmosphere, the particles when fluidized at an elevated temperature usually show larger bed voidages, higher bed pressure drops, and a lower Umf for the group A powder, all indicating an enhancement in fluidization quality. Possible mechanisms governing the operations of gas type and temperature in influencing the fluidization behaviours of fine particles have been discussed with respect to the changes in both gas properties and interparticle forces (on the basis of the London-van der Waals theory). Gas viscosity (varying significantly with gas-type and temperature) proves to be the key parameter that influences the bed pressure drops and Umf in fluidization of fine particles, while the interparticle forces (also varying with gas-type and temperature) may play an important role in fine-particle fluidization by affecting the expansion behaviour of the particle-bed. 展开更多
关键词 FLUIDIZATION fine particles gas type TEMPERATURE interparticle forces
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Effects of gangue compositions on reduction process of carbonbearing iron ore pellets
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作者 Qing-min Meng Jia-xin Li +6 位作者 Ru-fei Wei Hong-ming Long Tie-jun Chun Ping Wang Zhan-xia Di Luana Dessbeseli chunbao xu 《Journal of Iron and Steel Research International》 SCIE EI CAS CSCD 2018年第11期1105-1112,共8页
The influence of gangue compositions (mainly composed of SiO2,CaO,MgO and Al2O3)on the reduction kinetics of carbon-bearing iron ore pellets was estimated at 1373-1473 K in N2 atmosphere.The results showed that gangue... The influence of gangue compositions (mainly composed of SiO2,CaO,MgO and Al2O3)on the reduction kinetics of carbon-bearing iron ore pellets was estimated at 1373-1473 K in N2 atmosphere.The results showed that gangue content and each component distribution affected the pellets reduction process.The reduction rate was found to follow a linear correlation with quaternary basicity R4 [mass ratio of (CaO +MgO)to (SIO2 +Al2O3)]of the carbon-beating iron ore pellets;also,the content of SiO2 solid solution in iron oxide had a significant impact on the reduction rate.At the same reduction temperature,a higher R4 resulted in a lower SiO2 free content,weakening its inhibitory effect on the Boudouard reaction.The reduction temperature of Fe2SiO4 could be reduced by increasing the contents of CaO and MgO,improving the iron oxide reduction as well as the precipitation and growth of the iron grains.The g'angue content and .component distribution showed no effect on the rate-controlling step of the reduction;however,the apparent activation energy of reaction decreased with increasing quaternary basicity.When R4 increased from 0.15 to 0.67,the apparent activation energy decreased from 228.51 to 193.66 kJ/mol. 展开更多
关键词 Carbon-bearing iron ore PELLET GANGUE composition QUATERNARY BASICITY Reduction kinetics APPARENT activation energy
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