JDS
HOME HELP FEEDBACK SUBSCRIPTIONS ARCHIVE SEARCH TABLE OF CONTENTS
 QUICK SEARCH:   [advanced]


     


Journal of Dairy Science Vol. 53 No. 10 1353-1357
© 1970 by American Dairy Science Association ®
This Article
Right arrow Full Text (PDF)
Right arrow Alert me when this article is cited
Right arrow Alert me if a correction is posted
Services
Right arrow Similar articles in this journal
Right arrow Alert me to new issues of the journal
Right arrow Download to citation manager
Right arrow reprints & permissions
Citing Articles
Right arrow Citing Articles via Google Scholar
Google Scholar
Right arrow Articles by Edgerton, E. R.
Right arrow Articles by Warren, J. A.
Right arrow Search for Related Content
PubMed
Right arrow Articles by Edgerton, E. R.
Right arrow Articles by Warren, J. A.

Effect of Process Variables on the Holding Time in an Ultrahigh-Temperature Steam Injection System1

E. R. Edgerton2, V. A. Jones and J. A. Warren

Department of Food Science
and Department of Experimental Statistics, North Carolina State University, Raleigh 27607

ABSTRACT

Holding time was measured by monitoring the conductivity of a salt charge at each end of a holding tube on a strip chart recorder. The effect of pressure and temperature of the heated product on the holding time was studied in 88.7- and 113.7-cm tubes. Holding tube pressure was designated as that pressure in excess of the saturated vapor pressure of water at the holding temperature. Excess pressures of about 1 kg/cm2 were required to ensure reproducible measurement of holding time. At excess pressures below 0.7 kg/cm2 two-phase flow existed. Holding time decreased with pressure until all vapor was condensed. Holding time also decreased as temperature increased because of condensate added to the product and because of the reduced density at higher temperatures. A method for predicting holding tube length for a desired holding time or a holding time for a given holding tube length is presented. The prediction, computed from process and system parameters, ensures a safe process from a public health viewpoint. Calculation is based upon heat and mass balances and velocity distribution in a pipeline.


FOOTNOTES

1 Paper no. 3074 of the Journal Series of the North Carolina State University Agricultural Experiment Station, Raleigh.

2 Present address: Procter & Gamble, Cincinnati, Ohio.







HOME HELP FEEDBACK SUBSCRIPTIONS ARCHIVE SEARCH TABLE OF CONTENTS
Copyright © 1970 by the American Dairy Science Association ®.