Since the constant increase in petroleum price, use of glycerol waste, which is a byproduct from biodiesel production, as a partial replacement for fossil fuels via thermochemical conversion waste to energy processes ...Since the constant increase in petroleum price, use of glycerol waste, which is a byproduct from biodiesel production, as a partial replacement for fossil fuels via thermochemical conversion waste to energy processes is more practical. Gasification reaction has attracted a lot of interest by producing syngas rich in CO and H2. This syngas can be converted to clean liquid fuels, such as methanol and Fischer-Tropsch oil. Nickel and Cobalt catalyst was widely used in steam reforming reaction. ethanol etc. The aim of this work is to prepare and characterize 5.0 and 10.0%wt of Ni and Co catalysts using the impregnation method on various supporters, such as alumina and titanium oxide (TiO2) and to evaluate their catalytic performance. The specific surface area of developed catalysts was measured. X-ray diffraction (XRD) was applied to determine phase and crystallized size of the catalysts. Examination of the morphology. elemental composition and distribution of metal on the catalysts support were carried out using scanning electron microscopy (SEMi and energy dispersion spectroscopy (EDS) and x-ray mapping. The catalytic performance of prepared catalysts was test at 700 and 900℃ temperature of reaction. 1.87% O2. The result showed that the synthesized nickel and cobalt catalysts via impregnation method using Al2O3 and TiO2 as the catalyst support were suitable for glycerol conversion.展开更多
Energy recovery from waste biomass can have significant impacts on the most pressing development challenges of rural poverty and environmental damages. In this paper, a techno-economic analysis is carried out for elec...Energy recovery from waste biomass can have significant impacts on the most pressing development challenges of rural poverty and environmental damages. In this paper, a techno-economic analysis is carried out for electricity generation by using timber and wood waste (T & WW) gasification in Iceland. Different expenses were considered, like capital, installation, engineering, operation and maintenance costs and the interest rate of the investment. Regarding to revenues, they come from of the electricity sale and the fee paid by the Icelandic municipalities for waste collection and disposal. The economic feasibility was conducted based on the economic indicators of net present value (NPV) and discounted payback period (DPP), bringing together three different subgroups based on gasifier capacities, subgroup a: 50 kW, subgroup b: 100 kW and subgroup c: 200 kW. The results show that total cost increases as the implemented power is increased. This indicator varies from 1228.6 k€ for subgroups a to 1334.7 k€ for subgroups b and 1479.5 k€ for subgroups c. It is worth mentioning that NPV is positive for three subgroups and it grows as gasifier scale is extended. NPV is about 122 k€ (111,020 $), 1824 k€ (1,659,840 $) and 4392 k€ (3,996,720 $) for subgroups a, b and c, respectively. Moreover, DPP has an inversely proportional to the installed capacity. It is around 5.5 years (subgroups a), 9.5 months (subgroups b) and 6 months (subgroups c). The obtained results confirm that using small scale waste biomass gasification integrated with power generation could be techno-economically feasible for remote area in Iceland.展开更多
In this paper,a novel polygeneration system involving plasma gasifier,pyrolysis reactor,gas turbine(GT),supercritical CO_(2)(S-CO_(2))cycle,and organic Rankine cycle(ORC)has been developed.In the proposed scheme,the s...In this paper,a novel polygeneration system involving plasma gasifier,pyrolysis reactor,gas turbine(GT),supercritical CO_(2)(S-CO_(2))cycle,and organic Rankine cycle(ORC)has been developed.In the proposed scheme,the syngas is obtained by the gasification and the pyrolysis is first burned and drives the gas turbine for power generation,and then the resulting hot exhaust gas is applied to heat the working fluid for the supercritical CO_(2)cycle and the working fluid for the bottom organic Rankine cycle.In addition to the electrical output,the pyrolysis subsystem also produces pyrolysis oil and char.Accordingly,energy recovery is achieved while treating waste in a non-hazardous manner.The performance of the new scheme was examined by numerous methods,containing energy analysis,exergy analysis,and economic analysis.It is found that the net total energy output of the polygeneration system could attain 19.89 MW with a net total energy efficiency of 52.77%,and the total exergy efficiency of 50.14%.Besides,the dynamic payback period for the restoration of the proposed project is only 3.31 years,and the relative net present value of 77552640 USD can be achieved during its 20-year lifetime.展开更多
文摘Since the constant increase in petroleum price, use of glycerol waste, which is a byproduct from biodiesel production, as a partial replacement for fossil fuels via thermochemical conversion waste to energy processes is more practical. Gasification reaction has attracted a lot of interest by producing syngas rich in CO and H2. This syngas can be converted to clean liquid fuels, such as methanol and Fischer-Tropsch oil. Nickel and Cobalt catalyst was widely used in steam reforming reaction. ethanol etc. The aim of this work is to prepare and characterize 5.0 and 10.0%wt of Ni and Co catalysts using the impregnation method on various supporters, such as alumina and titanium oxide (TiO2) and to evaluate their catalytic performance. The specific surface area of developed catalysts was measured. X-ray diffraction (XRD) was applied to determine phase and crystallized size of the catalysts. Examination of the morphology. elemental composition and distribution of metal on the catalysts support were carried out using scanning electron microscopy (SEMi and energy dispersion spectroscopy (EDS) and x-ray mapping. The catalytic performance of prepared catalysts was test at 700 and 900℃ temperature of reaction. 1.87% O2. The result showed that the synthesized nickel and cobalt catalysts via impregnation method using Al2O3 and TiO2 as the catalyst support were suitable for glycerol conversion.
文摘Energy recovery from waste biomass can have significant impacts on the most pressing development challenges of rural poverty and environmental damages. In this paper, a techno-economic analysis is carried out for electricity generation by using timber and wood waste (T & WW) gasification in Iceland. Different expenses were considered, like capital, installation, engineering, operation and maintenance costs and the interest rate of the investment. Regarding to revenues, they come from of the electricity sale and the fee paid by the Icelandic municipalities for waste collection and disposal. The economic feasibility was conducted based on the economic indicators of net present value (NPV) and discounted payback period (DPP), bringing together three different subgroups based on gasifier capacities, subgroup a: 50 kW, subgroup b: 100 kW and subgroup c: 200 kW. The results show that total cost increases as the implemented power is increased. This indicator varies from 1228.6 k€ for subgroups a to 1334.7 k€ for subgroups b and 1479.5 k€ for subgroups c. It is worth mentioning that NPV is positive for three subgroups and it grows as gasifier scale is extended. NPV is about 122 k€ (111,020 $), 1824 k€ (1,659,840 $) and 4392 k€ (3,996,720 $) for subgroups a, b and c, respectively. Moreover, DPP has an inversely proportional to the installed capacity. It is around 5.5 years (subgroups a), 9.5 months (subgroups b) and 6 months (subgroups c). The obtained results confirm that using small scale waste biomass gasification integrated with power generation could be techno-economically feasible for remote area in Iceland.
基金supported by the National Natural Science Fund of China(No.52106008)Science Fund for Creative Research Groups of the National Natural Science Foundation of China(No.51821004)Science and Technology Planning Project of Guangdong Province(No.2020B1212060048).
文摘In this paper,a novel polygeneration system involving plasma gasifier,pyrolysis reactor,gas turbine(GT),supercritical CO_(2)(S-CO_(2))cycle,and organic Rankine cycle(ORC)has been developed.In the proposed scheme,the syngas is obtained by the gasification and the pyrolysis is first burned and drives the gas turbine for power generation,and then the resulting hot exhaust gas is applied to heat the working fluid for the supercritical CO_(2)cycle and the working fluid for the bottom organic Rankine cycle.In addition to the electrical output,the pyrolysis subsystem also produces pyrolysis oil and char.Accordingly,energy recovery is achieved while treating waste in a non-hazardous manner.The performance of the new scheme was examined by numerous methods,containing energy analysis,exergy analysis,and economic analysis.It is found that the net total energy output of the polygeneration system could attain 19.89 MW with a net total energy efficiency of 52.77%,and the total exergy efficiency of 50.14%.Besides,the dynamic payback period for the restoration of the proposed project is only 3.31 years,and the relative net present value of 77552640 USD can be achieved during its 20-year lifetime.