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

التفاصيل البيبلوغرافية
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.]
المؤلف الرئيسي: Bedareva E. V. Elena Vyacheslavovna
مؤلف مشترك: Национальный исследовательский Томский политехнический университет (ТПУ) Институт кибернетики (ИК) Кафедра компьютерных измерительных систем и метрологии (КИСМ)
مؤلفون آخرون: Marinushkin P. S., Khudonogova L. I. Ludmila Igorevna
الملخص: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
اللغة:الإنجليزية
منشور في: 2014
الموضوعات:
الوصول للمادة أونلاين:http://dx.doi.org/10.1088/1757-899X/66/1/012005
التنسيق: الكتروني فصل الكتاب
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=637836
الوصف
الملخص: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
DOI:10.1088/1757-899X/66/1/012005