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Number of results: 7
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Abstract

Low manganese and sulfur gray irons were produced by adding inoculant base Fe-Si with small amounts of Al and Ca in the ladle. The effect of the cast thickness, inoculant amount and shakeout time of the green sand molds were studied on the graphite flake formation by microscopically techniques. A thermodynamic analysis was carried out for the cast iron produced with the FactSage 7.2 software. Stability phase diagrams were obtained for both gray cast irons to different manganese (0.1 to 0.9 wt.%) and sulfur (0.01 to 0.12 wt.%) amounts to 1150°C. It was shown that lower amounts of manganese and sulfur allow forming the 3Al2O3·2SiO2, Al2O3, and ZrO2 solid compounds. The thermodynamic results match with those obtained by SEM-EDS. It is possible to form MnS particles in the liquid phase when the solubility product (%Mn) × (%S) equals 0.042 and 0.039 for heats A and B, respectively.

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Authors and Affiliations

G. Reyes-Castellanos
A. Cruz-Ramírez
E. Colin-García
V.H. Gutiérrez-Pérez
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Abstract

The aim of the paper is to revalorizate of the Szewalski binary vapour cycle by analysing thermodynamical and operational parameters of this cycle. This was carried out by accessible numerical computational flow mechanics codes using the step-by-step modeling of separate elements. The binary vapour cycle is providing steam as the working fluid in the high temperature part of the cycle, while another fluid - a low boiling point fluid of low specific volume - as the working substance substituting conventional steam over the temperature range represented by the low pressure steam expansion. The steam cycle for reference conditions has been assumed. Four working fluids in the low temperature part of the binary cycle such as propane, isobutane, ethanol and ammonia have been investigated.
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Authors and Affiliations

P. Ziółkowski
J. Hernet
J. Badur
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Abstract

This paper presents the results of thermodynamic analysis of the crude distillation units of two refineries in Nigeria. The analysis was intended to assess the thermodynamic efficiencies of the refineries and proffer methods of improving the efficiencies. Presented results show the atmospheric distillation units of the refineries have 33.3% and 31.6% exergetic efficiencies and 86.5% and 74.6% energetic efficiencies, respectively. Modifications of the operating and feed conditions of the refineries resulted in increased exergetic efficiencies for as much as 62.3% and 38.7% for the refineries. Thermodynamic analysis of the refineries can bring about efficiency improvement and effectiveness of the refineries.

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Authors and Affiliations

Funmilayo Nihinlola Osuolale
Ambrose Nwora Anozie
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Abstract

Most satellites stationed in space use catalytic propulsion systems for attitude control and orbit adjustment. Hydrazine is consumed extensively as liquid monopropellant, in the thrusters. Catalytic reactor is the most important section in the catalytic thruster. Ammonia and nitrogen gases are produced as a result of complete catalytic decomposition of hydrazine in the reactor, causing an increase in temperature and a rise in specific impulse. Ammonia is subsequently decomposed, leading to nitrogen and hydrogen gases. Decomposition of ammonia leads to a decrease in temperature, molecular weight and specific impulse. The latter phenomenon is unavoidable. The effect of ammonia decomposition on the reactor temperature, molecular weight of gaseous products and conclusively on specific impulse was studied in this article. At adiabatic state, thermodynamic analysis revealed that the maximum and minimum temperatures were 1655 K and 773 K, respectively. The highest molecular weight was obtained at ammonia conversion of zero and the lowest when ammonia conversion was 100%. The maximum specific impulse (305.4 S) was obtained at ammonia conversion of zero and completely conversion of ammonia, the minimum specific impulse (about 213.7 s) was obtained. For specific impulse, the result of thermodynamic calculation in this work was validated by the empirical results.

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Authors and Affiliations

Shahram Pakdehi
Fatemeh Shirvani
Reihaneh Zolfaghari
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Abstract

Recent climate changes stimulate the search and introduction of solutions for the reduction of the anthropogenic effect upon the environment. Transition to the oxy-fuel combustion power cycles is an advanced method of CO2 emission reduction. In these energy units, the main fuel is natural gas but the cycles may also work on syngas produced by the solid fuel gasification process. This paper discloses a new highly efficient oxy-fuel combustion power cycle with coal gasification, which utilizes the syngas heat in two additional nitrogen gas turbine units. The cycle mathematics simulation and optimization result with the energy unit net efficiency of 40.43%. Parametric studies of the cycle show influence of the parameters upon the energy unit net efficiency. Change of the cycle fuel from natural gas to coal is followed by a nearly twice increase of the carbon dioxide emission from 4.63 to 9.92 gmCO2/kWh.
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Bibliography

[1] Letcher T.M.: Why do we have global warming? In: Managing Global Warming. An Interface of Technology and Human Issues . Academic Press, 2019, 3–15.
[2] Rogalev A., Komarov I., Kindra V., Zlyvko O.: Entrepreneurial assessment of sustainable development technologies for power energy sector. Entrep. Sustain. Iss. 6(2018), 1, 429–445.
[3] Bose B.K.: Global warming: Energy, environmental pollution, and the impact of power electronics. IEE Ind. Electron. M. 4(2010), 1, 6–17.
[4] Huang W., Chen W., Anandarajah G.: The role of technology diffusion in a decarbonizing world to limit global warming to well below 2C: An assessment with application of Global TIMES model. Appl. Energ. 208(2017), 291–301.
[5] Ziółkowski P., Zakrzewski W., Badur J., Kaczmarczyk O.: Thermodynamic analysis of the double Brayton cycle with the use of oxy combustion and capture of CO2. Arch. Thermodyn. 34(2013), 2, 23–38.
[6] Barba F.C., Sanchez G.M.D., Segui B.S., Darabkhani H.G., Anthony E.J.: A technical evaluation, performance analysis and risk assessment of multiple novel oxy-turbine power cycles with complete CO2 capture. J. Clean. Prod. 133(2016), 971–985.
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[18] Zhao Y., Wang B., Chi J., Xiao Y.: Parametric study of a direct-fired supercritical carbon dioxide power cycle coupled to coal gasification process. Energ. Convers. Manage. 156(2018), 733–745.
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[20] Ebrahimi A., Meratizaman M., Reyhani H. A., Pourali O., Amidpour M.: Energetic, exergetic and economic assessment of oxygen production from two columns cryogenic air separation unit. Energy 90(2015), 1298–1316. [21] Kindra V., Rogalev A., Zlyvko O., Zonov A., Smirnov M., Kaplanovich I.: Research on oxy-fuel combustion power cycle using nitrogen for turbine cooling. Arch. Thermodyn. 41(2020), 4, 191–202.
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Authors and Affiliations

Vladimir Kindra
1
Andrey Rogalev
1
Olga Vladimirovna Zlyvko
Vladimir Sokolov
1
Igor Milukov
1

  1. National Research University “Moscow Power Engineering Institute”, Krasnokazarmennaya 14, Moscow, 111250 Russia
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Abstract

One of the problems in Russia Power Sector strategy until 2035 is the technologies development for mitigation of harmful emissions by the heat and power production industry. This goal may be reached by the transition to environmentally friendly generation units such as oxy-fuel combustion power cycles that burn organic fuels in pure oxygen. This paper provides the results of research on one of the most efficient oxy-fuel combustion power cycle, which was modified by the usage of nitrogen for turbine cooling. The computer simulation and parametric optimization approaches are described in detail. The net efficiency of the oxy-fuel combustion power cycle in relationship to the carbon dioxide turbine exhaust pressure is shown. Moreover, the influence of the regenerator scheme and modeling parameters on heat performance is obtained. Particularly, it was found that the transition to a scheme with five two-threaded heat exchangers decrease cycle efficiency by 4.2% compare to a scheme with a multi-stream regenerator.

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Authors and Affiliations

Vladimir Kindra
Andrey Rogalev
Olga Vladimirovna Zlyvko
Alexey Zonov
Matvey Smirnov
Ilya Kaplanovich
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Abstract

The paper presents a thermodynamic analysis of the integration of a cryogenic air separation unit into a negative CO 2 emission gas power plant. The power cycle utilizes sewage sludge as fuel so this system fits into the innovative idea of bioenergy with carbon capture and storage. A cryogenic air separation unit integrated with the power plant was simulated in professional plant engineering and thermodynamic process analysis software. Two cases of the thermodynamic cycle have been studied, namely with the exhaust bleed for fuel treatment and without it. The results of calculations indicate that the net efficiencies of the negative CO 2 emission gas power plant reach 27.05% (combustion in 95.0% pure oxygen) and 24.57% (combustion in 99.5% pure oxygen) with the bleed. The efficiencies of the cycle without the bleed are 29.26% and 27.0% for combustion in 95.0% pure oxygen and 99.5% pure oxygen, respectively. For the mentioned cycle, the calculated energy penalty of oxygen production was 0.235 MWh/kgO 2 for the lower purity value. However, for higher purity namely 99.5%, the energy penalty of oxygen production for the thermodynamic cycle including the bleed and excluding the bleed was indicated 0.346 and 0.347 MWh/kgO 2, respectively. Additionally, the analysis of the oxygen purity impact on the carbon dioxide purity at the end of the carbon capture and storage installation shows that for the case with the bleed, CO 2 purities are 93.8% and 97.6%, and excluding the bleed they are 93.8% and 97.8%, for the mentioned oxygen purities respectively. Insertion of the cryogenic oxygen production installation is required as the considered gas power plant uses oxy-combustion to facilitate carbon capture and storage method.
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Authors and Affiliations

Maja Kaszuba
1
Paweł Ziółkowski
1
Dariusz Mikielewicz
1

  1. Gdansk University of Technology, Narutowicza 11/12, 80-233 Gdansk, Poland

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