- Research Article
1
- 10.1016/s1359-6128(97)90064-1
EIA study identifies nuclear's growing electricity share
- Oct 01, 1997
- Pump Industry Analyst
EIA study identifies nuclear's growing electricity share
Solid waste (SW) outputs of industrial nations, mostly biomass, could fuel much more of their increasing energy needs than they currently do while creating good local jobs and industries. Using U.S. data as an example, 24 types of wasted or underutilized organic solids are identified. Now usually disposal problems, most of these SWs can be converted into useful gas, liquid, and solid (charcoal) fuels via pyrolysis. The non-condensable and condensable pyro-volatiles can be used by direct combustion as a clean source of heat energy or with advanced cleaning, in high-efficiency gas turbines or fuel cells. Pyrolysis processing has some important energy, environmental, economic, and security (EEES) advantages with respect to direct combustion or air or oxygen-blown partial combustion–gasification. An analytical semi-empirical model (ASEM) that points to some order in pyrolysis yields that could be helpful in optimizing the outputs of Solid Waste to Energy by Advanced Thermal Technologies (SWEATT) systems is described. We describe an analytical cost estimation (ACE) model that can be used to relate the cost of electricity for diverse electrical generating technologies including SWEATT systems to capital, operation, environmental control, cost of fuel (COF), and estimated costs of environmental and security externalities (ESE) such as climate change and terror threats. ACE can be useful particularly in estimating the impact of changes in COF and ESE, usually the most uncertain independent variables. The EEES issues related to soil applications of biomass pyrolysis products, i.e., biochar, are outlined. A growing International Biochar Initiative is underway to use biochar to sequester carbon in the soil, thereby mitigating climate change while enhancing soil fertility. High transportation costs due to the low energy densities of biomass/SW, compared to coal or petroleum, imply that siting SWEATT systems close to the SW source would have a number of cost and environmental advantages. The application of SWEATT systems in support of agricultural programs that grow high-yield vegetable oil crops intended for biodiesel production on non-food-producing lands is considered as a means of providing additional revenue streams. Additional SWEATT applications in conjunction with the other forms of the 24 types of SW are to be expected. energy type is very sensitive to its physical form as indicated in Table 2 which gives prices of various forms of energy in the United States at the beginning of 2010. The large carbon dioxide neutral (neither net producing nor consuming CO2) plant matter components in Table 1 can help in greenhouse heating mitigation. The great diversity of physical and chemical characteristics of fuel wastes (feedstock) in Table 1 implies that the world now needs “omnivorous feedstock converters” (OFCs) to change these solid fuels into much more usable liquid or gaseous fuels or better solid fuels. Fig. 1 is a conceptual illustration of an OFC adapted from a number of prior papers in which a SW pyrolyzer–gasifier–liquifier–carbonizer is coutilized with a natural gas-fired combined cycle (NGCC) system, as will be discussed below. Table 3 shows major ranks of coals as well as of peat, wood, and cellulose and their ultimate and proximate analyses as measured by industry for over a century. The SOLID WASTE, SOLID FUELS, AND THEIR PROPERTIES In 2011 the United States was heavily (~50%) reliant on foreign sources for its liquid fuels and somewhat (~10%) dependent upon imports for its gaseous fuels. Our country is now expending “blood and treasure” in its efforts to stabilize regions of the globe that supply these premium fuels. Yet the United States is well endowed with solid fuels in the form of coal, oil shale, and substantial quantities of renewable but wasted solids. As part of a continuing long search for alternatives to oil, this entry is focused on converting our solid waste to energy by advanced thermal technologies (SWEATTs) while mitigating environmental and economic problems. Table 1 is a list of United States’ abundant supply of solid waste (SW) whose organic matter can be converted into gaseous and liquid fuels as well as charcoal. The value society places on a specific fuel or D ow nl oa de d by [ T & F In te rn al U se rs ], [ M eg an H ila nd s] a t 0 6: 09 3 0 Ju ly 2 01 3 Energy: Solid Waste Advanced Thermal Technology 831 En er gy E ffi ci en cy –
EIA study identifies nuclear's growing electricity share
EIA study identifies nuclear's growing electricity share
Coal: Energy for the future
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Main aspects of kerosene and gaseous fuel ignition in aero-engine
ABSTRACTVarious liquid and gaseous alternative fuels have been proposed to replace the kerosene as aircraft fuel. Furthermore, new combustion technologies were developed to reduce the emissions of aero-engine. A staged fuel injection arrangement for a lean burn combustion system was applied to improve the operability of an aero-engine by achieving high flame stability at reduced combustion emissions. Originally, both circuits (pilot and main) are fuelled by kerosene; moreover, the pilot injector is operating at low power (engine idle and approach) and the pilot flame is anchored in an airflow recirculation zone. In the case of the performed research, the pilot injector was modified to allow the use of gaseous fuels. Thus, the burner model allows a flexible balancing of the mass flows for gaseous and liquid fuel. The present paper describes the investigation of ignitability for the proposed staged combustor model fuelled by gaseous and liquid fuels. A short overview on physical properties of used fuels is given. To investigate atomisation and ignition, different measurements systems were used. The effectiveness of two ignitor types (spark plug and laser ignitor) was analysed. The ignition performance of the combustor operating on various fuels was compared and discussed in detail.
Read moreAUTONOMOUS POWER SUPPLY ON SOLID FUEL AND BIOGAS
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Read moreAll-solid-state passive direct methanol fuel cells with great orientation stability and high energy density based on solid methanol fuels
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Addressing the advantages and limitations of using Aethalometer data to determine the optimal absorption Ångström exponents (AAEs) values for eBC source apportionment
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This article is the first in a series of articles aimed at introducing common methods for evaluating gaseous, liquid, and solid conventional and alternative fuels. The paper presents an overview of the monitored elements and their non-hydrocarbon compounds for individual liquid and gaseous fuels. Methods for determining these analytes are also presented. The significance of these determinations is also discussed. The emphasis is given mainly on standardized parameters and tests, but in some cases, we discuss also non-standardized tests or analyses not required by standards. The main goal of the article is to provide a comprehensive overview of elements and their non-hydrocarbon compounds monitored for individual fuels, the reason why these analytes are monitored, and what methods are used for this monitoring. Practically all liquid fuels discussed in this article are monitored for sulfur content. The limit value for sulfur content is 10 mg/kg, with the exception of paraffinic diesel fuel and some synthetic liquid fuels. Phosphorus content is monitored in all fuels containing a higher proportion of biocomponents. Examples such fuels are ethanol, FAME, E85, E95, and rapeseed oil. For fuels containing ethanol, the oxygen content (E5, E10) and alcohol content (E5, E10, E85 and E95), or ether content (E5, E10, E85) are also monitored. Among the minor elements, lead (E5, E10, E95), manganese (E5, E10, B7, and B10), copper (ethanol, E95), alkali metals (FAME) and alkaline earth metals (FAME and rape oil) are monitored. As with liquid fuels, the sulfur content of gaseous fuels is also monitored. Of the sulfur compounds, the sum of sulfur and carbonyl sulfide content is monitored for CNG, LNG, and their bioequivalents. For LPG for internal combustion engines, sulfane is determined qualitatively, whereas for LPG for heating purposes, the sulfur content is quantified. In the case of LPG for heating purposes, the ammonia content is determined qualitatively, and in the case of biogas according to ČSN 65 6514, the content of nitrogenous impurities except to nitrogen, and the sum of the content of carbon dioxide, nitrogen and oxygen are also evaluated.
Read moreInvestigations of the Emission Characteristics of a Dual-Fuel Gas Turbine Combustion Chamber Operating Simultaneously on Liquid and Gaseous Fuels
This study is dedicated to investigations of the working process in a dual-fuel low-emission combustion chamber for a floating vessel’s gas turbine. As the object of the research, a low-emission gas turbine combustion chamber with partial premixing of fuel and air inside the outer and inner radial-axial swirls was chosen. The method of the research is based on the numerical solution of the system of differential equations which represent the physical process of mass and energy conservation and transformations and species transport for a multi-component chemically reactive turbulent system, considering nitrogen oxides formation and a discrete ordinates model of radiation. The chemistry kinetics is presented by the 6-step mechanism of combustion. Seven fuel supply operating modes, varying from 100% gaseous fuel to 100% liquid fuel, have been analysed. This analysis has revealed the possibility of the application of computational fluid dynamics for problems of dual-fuel combustion chambers for the design of a floating vessel’s gas turbine. Moreover, the study has shown the possibility of working in different transitional gaseous and liquid fuel supply modes, as they satisfy modern ecological requirements. The dependencies of the averaged temperature, NO, and CO concentrations along the length of the low-emission gas turbine combustion chamber for different cases of fuel supply are presented. Depending on the different operating modes, the calculated emission of nitrogen oxides NO and carbon monoxide CO at the outlet cross-section of a flame tube are different, but, they lie in the ranges of 31‒50 and 23‒24 mg/nm3 on the peak of 100% liquid fuel supply mode. At operating modes where a gaseous fuel supply prevails, nitrogen oxide NO and carbon monoxide CO emissions lie in the ranges of 1.2‒4.0 and 0.04‒18 mg/nm3 respectively.
Read moreBiorefining of biomass to liquid fuels and organic chemicals
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Comprehensive review on pyrolytic oil production, upgrading and its utilization
Utilization of fuel oil from biomass (i.e., bio-oil) reduces emission of greenhouse gases. This paper discusses the different pyrolyis processes, physiochemical properties of pyrolysis products, upgrading techniques for safe storage and application in transportation and industrial activities. The production of bio-oil is challenging and requires inclusion of modern technologies. Pyrolysis plays a key role in the production of solid, liquid, and gaseous fuels from biomass. About 60–65% yield of bio-oil produced through the pyrolysis process using fluidized bed reactor has been reported. Among the all pyrolysis technologies vacuum pyrolysis was found a well suitable not only for bio-oil production, but also for improving the physicochemical properties of biochar such as surface area, porosity (macro/micro), functional groups, etc. In bio-oil upgrading, catalytic cracking process was observed as a most promising technique for the upgrading of bio-crude in to liquid fuel. Pyrolysis based synthetic fuels are considered as one of the key to saving the potential greenhouse gas emission up to 60—80% as compared to fossil fuels.
Read moreCritical requirements in combustion research
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Bioelectrosynthesis as an alternative to photosynthesis
The CO2 reduction processes have been discussed as a way of designing an ecologically totally closed technology. An electric current and molecular hydrogen are the two related available agents that can be discussed as ecologically pure reductants. The most important products are liquid and gaseous fuels, the products of large-scale organic synthesis, monomers, and amino acids. For CO2 reduction, the necessary energy consumption and H2 costs were calculated. For complex organic molecules, amino acids for instance, the energy consumption does not make up the main portion of the costs. The biocatalytic systems of CO2 reduction based on cryoimmobilized cells are described. Conversion of CO2 into L-lysine with electrochemical decomposition of water was effected on the laboratory scale. A general unit for diverse technological processes can be a bioelectrosynthetic Index Entries: Bioelectrosynthesis; CO2 reduction; liquid fuels; amino acids; immobilized cells; economic estimates. modulus, an electrochemical hydrogen generator coupled with a biocatalytic converter of hydrogen and oxygen. The systems for bioelectrosynthesis of motor fuels and essential amino acids have been economically estimated and characterized. The possibilities of combining the solar energy transformation and H2–CO2 conversion have been discussed.
Read moreBiogas Energy Resources in Pakistan Status, Potential, and Barriers
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