Features of application of the methane-hydrogen fraction as fuel for thermal power plant boiler
https://doi.org/10.30724/1998-9903-2019-21-3-109-116
Abstract
The methane-hydrogen fraction is a gaseous hydrocarbon by-product during oil processing for obtaining petroleum products. Until recently, the methane-hydrogen fraction was used as furnace oil in internal technological processes at a refinery. Some of the low-calorie methane-hydrogen fraction was burned in flares. Driven by the prospect of the methane-hydrogen fraction use as a fuel alternative to natural gas for burning in thermal power plants boilers, it became necessary to study the methane-hydrogen fraction combustion processes in large volumes. The conversion of ON-1000/1 and ON-1000/2 furnaces from the combustion of the methane- hydrogen fraction with combustion heat of 25.45 MJ/m3 to the combustion of the composition with combustion heat of 18.8 MJ/m3 leads to a decrease in temperature in the flame core for 100 °C as an average. The intensity of flame radiation on the radiant tubes decreases. Therefore, the operation of furnaces during combustion of methane-hydrogen fraction with a low heat of combustion at the gas oil hydro-treating unit is carried out only with a fresh catalyst, which allows lower flame temperatures in the burner.
The experiments to determine the concentration of nitrogen oxides NOx and the burning rate w of the methane-hydrogen fraction in the ON-1000/1 furnace and natural gas in the TGM-84A boiler, depending upon the heat of combustion Qnr were carried out. The obtained results showed that the increase in the hydrogen content Н2 from 10.05 % to 18.36% (by mass) results in an increase in the burning rate w by 45%. The burning rate of natural gas with methane CH4 content of 98.89% in the TGM-84A boiler is 0.84 m/s, i.e. it is 2.5 times lower than the burning rate of the methane- hydrogen fraction with H2 content of 10.05%. The distributions of heat flux from the flame qf over the burner height h in the TGM-84A boiler were obtained in case of natural gas burning and calculation of burning of the methane-hydrogen fraction with a hydrogen content of 10.05% and methane of 28.27%. The comparison of the obtained data shows that burning of methane- hydrogen fraction causes an increase in the incident heat flux qf at the outlet of the burner.
About the Authors
M. A. TaymarovRussian Federation
Mikhail A. Taymarov
Kazan
V. K. Ilyin
Russian Federation
Vladimir K. Ilyin
Kazan
E. G. Chiklyaev
Russian Federation
Evgeniy G. Chiklyaev
Kazan
R. G. Sungatullin
Russian Federation
Rais G. Sungatullin
Kazan
References
1. Tajmarov MA., Kuvshinov NE., Stepanova TO. Optimizaciya raboty pechej P-101 i P-101A na ustanovke L-24-600. Vestnik Kazanskogo tekhnologicheskogo universiteta.2015.18 (22):50–53 (In Russ).
2. Tanatarov MA., Ahmetshina MN., Faskhutdinov RA. Tekhnologicheskie raschety ustanovok pererabotki nefti. M: Himiya, 1987. (In Russ).
3. Sardanashvili AG., L'vova AI. Primery i zadachi po tekhnologii pererabotki nefti i gaza. M: Himiya, 1980. 256. (In Russ).
4. Manovyan AK. Tekhnologiya pervichnoj pererabotki nefti i prirodnogo gaza .M: Himiya, 2001. 568. (In Russ).
5. Tajmarov MA., Dodov IR. Ustanovka dlya proizvodstva sinteticheskogo motornogo topliva.. Vestnik kazanskogo tekhnologicheskogo universiteta. 2015; 18(8):162–166.
6. Trembovlya VI., Finger ED., Avdeeva AA. Teplotekhnicheskie ispytaniya kotel'nyh ustanovok.2 nd ed. Moscow: Energiya 1977. (In Russ).
7. Tajmarov MA., Ahmetova RV., Lavirko YuV. Sungatullin RG., Zheltuhina ES. Snizhenie vrednyh vybrosov v atmosferu oksidov azota kotlami TES. Izvestiya KGASU 2017.39(1):180–188. (In Russ).
8. Zel'dovich YaB., Sadovnikov PYa., Frank- Kameneckij DA. Okislenie azota pri gorenii. M.-L: ANSSSR 1947 (In Russ).
9. Knorre GF., Aref'ev KM., Bloh AG., Nahapetyan EA., Paleev II., Shtejnberg VB. Teoriya topochnyh processov. M.-L.: Energiya 1966. (In Russ).
10. Bloh AG. Teploobmen v topkah parovyh kotlov. L.: Energoatomizdat 1984. (In Russ).
11. Aksyutin O., Ishkov A., Romanov K., et al. New Methane-Hydrogen Fuel Technology and its Potential Application in the Gas Industry. Development and Innovation in Focus All Eyes Turn to Perth for LNG 18. Report of the International Gas Union, April–September 2016, P. 74–76.
12. Kim JJ. Adsorption equilibria and kinetics of propane and propylene on zeolite 13x pellets. Microporous and mesoporous materials. 2019; 274: 286-298.
13. Mirel I., Pentia D., Florescu C., et al.. Water treatment from swimming pool, piscine and swimming basins. Scientific Bulletin of Politechnica University of Timisoara. 2015; 60(2):79-83.
14. World Energy Outlook / International Energy Agency 2018:46.
15. Steadier Boom for the Oil Sands // Petroleum Economist. 2016. June. P. 8–10.
16. Short-term Canadian Natural Gas Deliverability 2015–2018. P. 6
Review
For citations:
Taymarov M.A., Ilyin V.K., Chiklyaev E.G., Sungatullin R.G. Features of application of the methane-hydrogen fraction as fuel for thermal power plant boiler. Power engineering: research, equipment, technology. 2019;21(3):109-116. https://doi.org/10.30724/1998-9903-2019-21-3-109-116