Dergiler / Isı Bilimi ve Tekniği Dergisi / 2020 / Cilt: 40 - Sayı: 1

THE EFFECTS OF CO2, H2O, AND N2DILUTIONS ON POLLUTANTS OF SHALE GAS COMBUSTION

Sayfa
15–25
Yayın Tarihi
2022-10-18
DOI
—
🏛️Bu makalenin bibliyografik verileri ve tam metin bağlantısı DergiPark üzerinden sağlanmıştır.
DergiPark Kaydı ↗
✨

Yapay Zeka Hızlı Bakış & Çıkarımlar

AI Insight
⚡ TL;DR(1 Cümlede Hızlı Çıkarım)

The use of H2O dilution steps forward in compared with CO2and N2because of itsopposite effects on NOxand CO pollutants.

📌 3 Maddede Bu Makale

🎯
Amaç & Hipotez:Increase in demands for energy and discovered huge reserves of shale gas in the world cause countries and researchers to focus on it progressively.
📊
Temel Bulgular & Veri:It is concluded that NOxfor New Albany and Haynesville come to the maximum value at 1.025 and 1.02 of equivalence ratio and the maximum reaction temperatures are 2027 and 2014 K in turn.
💡
Sonuç & Katkı:The use of H2O dilution steps forward in compared with CO2and N2because of itsopposite effects on NOxand CO pollutants.
🔬Tür:Modelleme & Sayısal Simülasyon
📍Kapsam:2027 Verileri
⚙️Değişkenler:Alan Parametreleri

Abstract

Increase in demands for energy and discovered huge reserves of shale gas in the world cause countries and researchers to focus on it progressively. The amount of shale gas production has begun to rise by developing the techniques of gas extraction from shale rocks recently. In this paper, the non-premixed combustion characteristic and emissions of shale gas and humid air with dilution effects are numerically investigated under different equivalence ratio, pressure and temperature. A two dimension model of cylindrical combustor is considered. It is concluded that NOxfor New Albany and Haynesville come to the maximum value at 1.025 and 1.02 of equivalence ratio and the maximum reaction temperatures are 2027 and 2014 K in turn. The rising equivalence ratio raises CO mass fractions. The increasing dilution rates decrease NOxand uplift CO mass fractions. The enhancing pressure rears NOxand diminishes CO fractions. The ascending wall temperature boosts NOx, CO and reaction temperatures. NOxand CO from environmental pollutants emerging at the end of shale gas combustion can be lowered by decreasing equivalence ratio, wall temperature, and pressure. The use of H2O dilution steps forward in compared with CO2and N2because of itsopposite effects on NOxand CO pollutants.

🔖

Bu Makaleye Atıf Yap

ÖZTÜRK, S. (2022). THE EFFECTS OF CO2, H2O, AND N2DILUTIONS ON POLLUTANTS OF SHALE GAS COMBUSTION. Isı Bilimi ve Tekniği Dergisi, Cilt: 40 - Sayı: 1, 15–25. https://ajindex.com/articles/542468

📄 Tam Metin PDF Okuyucu

📄

PDF görüntüleyici hazırlanıyor...

Kaynakça (10)

  1. Akça H., ÜrelG., Karacan C. D., Tuygun N., and Polat E., 2017, The Effect of Carbon Monoxide Poisoning on Platelet Volume in Children, J Pediatr Emerg Intensive Care Med, 4, 13-16. Alberts W.M., 1994, Indoor Air Pollution: NO, NO2, CO, and CO2, J Allergy Clin Immunol, 94, 289-95. ANSYS Release 12.0. Tutorial 14.Modeling Species Transport and Gaseous Combustion. 1-46,
  2. ANSYS, Inc, 2009.
  3. Bilgen, S., and Sarıkaya, İ., 2016, New Horizon in Energy: Shale Gas,Journal of Natural Gas Science and Engineering, 35, 637-645.
  4. Bullin K., Krouskop P., and Bryan Research and Engineering Inc. Bryan, Tex., 2008, Composition Variety Complicates Processing Plans for US Shale Gas, E-book, Based on: Annual Forum, Gas Processors Association, Houston Chapter, Houston.Chang Y., Huang R,. Ries R. J., and MasanetE., 2015, Life-Cycle Comparison of Greenhouse Gas Emissions and Water Consumption for Coal and Shale Gas Fired Power Generation in China, Energy, 86, 335-343. Cohen B, and Winkler H., 2014, Greenhouse Gas Emissions from ShaleGas and Coal for Electricity Generation in South Africa, S Afr J Sci., 110 (3/4), 1-5. Garreton D. and Simonin O., 1994, Aerodynamics of Steady State Combustion Chambers and Furnaces, In ASCF Ercoftac Cfd Workshop, Org: EDF Chatou, France.Hayashi S., Yamada H., Shimodaira K., and Machida T., 1998,
  5. NOxEmissions from Non-Premixed, Direct Fuel Injection Methane Burners at High-Temperature and Elevated Pressure Conditions, Twenty-Seventh Symposium (International) on Combustion/The Combustion Institute, 1833-1839.
  6. Hraiech, I., Sautet, J. C., Yon, S., and Mhimid, A.,2015,Combustion of Hythane Diluted with CO2,Thermal Science, 19 (1), 1-10.
  7. Jerzak W., Kuzniaa M., Zajemska M., 2014, The Effect of Adding CO2to The Axis of Natural Gas Combustion Fames on CO and NOxConcentrations in The Combustion Chamber, Journal of Power Technologies, 94 (3), 202-210.
  8. McTaggart-Cowan G. P., Wu N., Jin B., Rogak S. N., Davy M. H. and Bushe W. K., 2009, Effects of Fuel Composition on High-Pressure Non-Premixed Natural Gas Combustion, Combust. Sci. and Tech., 181, 397-416.
  9. Muharam, Y., Mahendra, M., Giffari, F., and Kartohardjono, S., 2015, Effects of Injection Temperature and Pressure on Combustion in An Existing Otto Engine using CNG Fuel,Journal of Environmental Science and Technology, 8 (1), 25-34.
  10. Lan, Y., Yang, Z., Wang, P., Yan, Y., Zhang, L., and Ran, J., 2019, A Review of Microscopic Seepage Mechanism for Shale Gas Extracted by Supercritical CO2Flooding,Fuel, 238,412-424. Oz