675 research outputs found

    Cimarron Citizen, 06-24-1908

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    https://digitalrepository.unm.edu/cimarron_citizen_news/1016/thumbnail.jp

    Cimarron Citizen, 04-08-1908

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    https://digitalrepository.unm.edu/cimarron_citizen_news/1005/thumbnail.jp

    Cimarron Citizen, 04-15-1908

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    https://digitalrepository.unm.edu/cimarron_citizen_news/1006/thumbnail.jp

    Cimarron Citizen, 06-10-1908

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    https://digitalrepository.unm.edu/cimarron_citizen_news/1014/thumbnail.jp

    Cimarron Citizen, 03-11-1908

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    https://digitalrepository.unm.edu/cimarron_citizen_news/1001/thumbnail.jp

    Cimarron Citizen, 06-03-1908

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    https://digitalrepository.unm.edu/cimarron_citizen_news/1013/thumbnail.jp

    Cimarron Citizen, 07-08-1908

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    https://digitalrepository.unm.edu/cimarron_citizen_news/1018/thumbnail.jp

    Cimarron Citizen, 04-22-1908

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    https://digitalrepository.unm.edu/cimarron_citizen_news/1007/thumbnail.jp

    Cimarron Citizen, 03-25-1908

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    https://digitalrepository.unm.edu/cimarron_citizen_news/1003/thumbnail.jp

    Heat Flow in the Finite Cylinder with Variable Surface Temperature

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    If heat be supplied at a constant rate to a liquid which is kept at uniform temperature throughout by stirring, and if this liquid lose heat according to Newton\u27s law of cooling, we get dΘ/dt = β/C – αΘ for the differential equation from which to obtain the temperature, Θ, as a function of time. β/c is the rate of heat supply divided by thermal capacity and a Θ the rate of cooling. The surrounding medium is assumed to be at zero temperature. This equation is equally valid if the liquid be replaced by a solid of very high diffusivity. Equation (1) assumes the thermal capacity of the liquid to be independent of temperature
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