Preview

Proceedings of the Voronezh State University of Engineering Technologies

Advanced search

The selection of catalysts that provide stability and high oxidation rate of hydrogen and methane in the reactors R 2 compartments of helium Orenburg helium plant

https://doi.org/10.20914/2310-1202-2018-4-316-321

Abstract

This article presents an overview of promising catalysts, the selection of the most effective, calculated the economic effect of the introduction of a new catalyst. The selection of catalysts providing stability of operation and high rate of oxidation of hydrogen and methane flowing in the reactor P 2 of the helium fine purification unit of helium production from helium concentrate was made. To ensure the technological process in the production of chemical, gas processing and oil refining enterprises, catalysts of different modifications and types of both domestic and imported production are used. For stable operation and high oxidation rate of hydrogen and methane flowing in the reactor P-2 of the helium fine purification unit-22 of the Orenburg helium plant, the AP-56 aluminum-platinum catalyst is used. The catalyst AP-56 participating in oxidation processes in connection with the improvement of the technological process does not meet the standards established in the technological regulations, including an increase in hydrogen concentrations, and this in turn worsens the quality of gasoline fractions, in addition, the catalyst AP-56 is promoted by chlorine, which contributes to the development of corrosion on heat exchange equipment located after the reactor. The above circumstances forced manufacturers to reduce the production of aluminum-platinum catalyst AP-56. The most productive among the units of fine cleaning plant, which includes 3 similar compartments with a capacity of up to 400 Nm3/h for raw materials, is considered. To confirm of the selected catalysts on existing equipment and for implementation, the technological calculations of the catalytic purification unit were made, and the main indicators of the process were determined.

About the Authors

T. A. Kuryakova
Gubkin Russian state University of oil and gas named after I. M. Gubkin
Russian Federation
Cand. Sci. (Engin.), associate professor, st. Young Leninists, 20, Orenbburg, Russia


E. A. Fedorov
Gazprom dobycha Orenburg
deputy head of technical department, helium plant OOO "Gazprom dobycha Orenburg", Chkalova str., 1/2


L. V. Meghueva
Orenburg state university
Dr. Sci. (Engin.), professor, department of food biotechnology, prospekt Pobedy, 13, Orenburg, 460018, Russia


A. V. Bykov
Orenburg state university
Cand. Sci. (Engin.), associate professor, Orenbrug state university, prospekt Pobedy, 13, Orenburg, 460018, Russia


References

1. Grishina M.A., Mardashev Y.S., Goryacheva V.N. Catalytic systems based on metal catalysts in the oxidation of methane. Inzhenernyj zhurnal: nauka i innovacii [Engineering journal: science and innovation]. 2013. vol. 6. doi: 10.18698/2308-6033-2013-6-794 (in Russian).

2. 2 Dynarski Y.I. Processy i apparaty himicheskoj tekhnologii [Processes and apparatuses of chemical technology]. Moscow, Chemistry, 2002. (in Russian).

3. 3 Zashchita atmosfery ot promyshlennyh zagryaznenij [The protection of the atmosphere from industrial air pollution; edited by S. Calvert, G. Englund]. Moscow, Metallurgy, 1988. 58 p. (in Russian).

4. Kalashnikov M.Yu., Becker V.J., Makarov A.M. Phase composition and deposition rate of aluminum hydroxides depending on the conditions for obtaining secondary carrier in the manufacture of block catalysts. ZhPH [JPH]. 1996. vol. 69. no. 12. pp. 1997-2000. (in Russian).

5. 5 Kopsha D.P., Gogoleva I.V., Izyumchenko V.D Possible ways of optimizing the process of fine purification of helium concentrate. Nauchno-tekhnicheskij sbornik vesti gazovoj nauki [Scientific and technical collection is to conduct gas science]. 2015. no. 1 (21). pp. 39-44. (in Russian).

6. 6 Kravtsov A.V., Ivanchina E.D. Komp'yuternoe prognozirovanie raboty promyshlennyh katalizatorov processov riforminga i izomerizacii uglevodorodov benzinovoj frakcii [Computer prediction of the operation of industrial catalysts for the processes of reforming and isomerization of hydrocarbons in the gasoline fraction]. Tomsk, Tomsk Polytechnic University, 2010. 129 p. (in Russian).

7. 7 Kuzmina R.I. Kataliticheskij riforming uglevodorodov [Catalytic reforming of hydrocarbons]. Saratov, MVD of Russia, 2010. 252 p. (in Russian).

8. 8 Lichnicki K.V., Jaskula M. Promising catalysts for the oxidation of hydrogen for fuel cells. Proceedings of IX International Conference "Hydrogen Material Science and Chemistry of Metal Hydrides". 2005. pp. 988-989. (in Russian).

9. 9 Panteleev D.V., Stolypin E.V., Volchenko A.G. The development of industrial production of helium in OOO "Gazprom dobycha Orenburg". Neftegazovoe delo [Oil and gas business]. 2011. no. 2. pp. 128-135. (in Russian).

10. 10 Ob ischislenii i vzimanii platy za negativnoe vozdejstvie na okruzhayushchuyu sredu [On the calculation and collection of fees for a negative impact on the environment (Decree of the Government of the Russian Federation No. 255 of March 3, 2017)]. in Russian).

11. Slash A., Chaudhry U., Wagner F. et al. Kataliz v promyshlennosti [Catalysis in industry; edited by V.M. Gryaznov]. Moscow, Mir, 1986. 291 p. (in Russian).

12. 12 Sycheva A.M., Genkin V.S., Mel'nikov S.I., Durik N.M. Reactor for carrying out catalytic processes. Otkrytiya. Izobreteniya [Open. Inventions]. 1983. no. 46. pp. 18-19. (in Russian).

13. 13 Romanovskii B.V. Osnovy himicheskoj kinetiki [Fundamentals of chemical kinetics]. Moscow, Exam, 2006. 415 p. (in Russian).

14. 14 Stronberg A.G. Fizicheskaya himiya [Physical chemistry]. Moscow, Higher school, 2003. 527 p. (in Russian).

15. 15 Timonova O.A., Mardashev Yu.S. Catalysts for complete oxidation of natural gas as the basis of environmentally friendly energy. MPGU, VII Mezhdunarodnaya konferenciya [Moscow pedagogical state University, VII International conference]. Moscow – Yerevan, 2008. pp. 274–275. (in Russian).

16. 16 Filimonova I.V. Strukturoobrazovanie i svojstva vysokoporistogo blochnogo katalizatora okisleniya molekulyarnogo vodoroda [Structure formation and properties of highly porous block catalyst of molecular hydrogen oxidation]. Perm, 1998. 165 p. (in Russian).

17. 17 Shirokopoyas S.I. Gidrodearomatizaciya uglevodorodnogo syr'ya s ispol'zovaniem bimetallicheskih platino-palladievyh katalizatorov na osnove mezoporistyh alyumosilikatov [Hydrodearomatization hydrocarbons using bimetallic platinum-palladium catalysts based on mesoporous aluminosilicates]. Moscow, 2014. 121 p. (in Russian).


Review

For citations:


Kuryakova T.A., Fedorov E.A., Meghueva L.V., Bykov A.V. The selection of catalysts that provide stability and high oxidation rate of hydrogen and methane in the reactors R 2 compartments of helium Orenburg helium plant. Proceedings of the Voronezh State University of Engineering Technologies. 2018;80(4):316-321. (In Russ.) https://doi.org/10.20914/2310-1202-2018-4-316-321

Views: 580


Creative Commons License
This work is licensed under a Creative Commons Attribution 4.0 License.


ISSN 2226-910X (Print)
ISSN 2310-1202 (Online)