Calculation of coaxial shunts superheat temperature; IOP Conference Series: Materials Science and Engineering; Vol. 66: 20th International Conference for Students and Young Scientists: Modern Techniques and Technologies (MTT'2014), Tomsk, Russia, 14-18 April 2014

Detalhes bibliográficos
Parent link:IOP Conference Series: Materials Science and Engineering
Vol. 66: 20th International Conference for Students and Young Scientists: Modern Techniques and Technologies (MTT'2014), Tomsk, Russia, 14-18 April 2014.— 2014.— [012005, 5 p.]
Autor principal: Bedareva E. V. Elena Vyacheslavovna
Autor Corporativo: Национальный исследовательский Томский политехнический университет (ТПУ) Институт кибернетики (ИК) Кафедра компьютерных измерительных систем и метрологии (КИСМ)
Outros Autores: Marinushkin P. S., Khudonogova L. I. Ludmila Igorevna
Resumo:Title screen
Coaxial shunt temperature field distribution has been obtained and analyzed using software package ANSYS. The main stages of 3D modeling of coaxial shunt temperature field in ANSYS are considered in the paper. It is determined that coaxial shunt temperature field distribution is nonuniform because of the material physical properties and free convection. The difference between theoretical temperature cylinder (60 °C) and experimentally observed temperature value (49 °C) of resistive pipe is caused by the fact that free convection and heat emission were not taken into account when calculating.
Режим доступа: по договору с организацией-держателем ресурса
Idioma:inglês
Publicado em: 2014
Assuntos:
Acesso em linha:http://dx.doi.org/10.1088/1757-899X/66/1/012005
Formato: Recurso Electrónico Capítulo de Livro
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=637836

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330 |a Coaxial shunt temperature field distribution has been obtained and analyzed using software package ANSYS. The main stages of 3D modeling of coaxial shunt temperature field in ANSYS are considered in the paper. It is determined that coaxial shunt temperature field distribution is nonuniform because of the material physical properties and free convection. The difference between theoretical temperature cylinder (60 °C) and experimentally observed temperature value (49 °C) of resistive pipe is caused by the fact that free convection and heat emission were not taken into account when calculating. 
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