Severity: Warning
Message: file_get_contents(https://...@pubfacts.com&api_key=b8daa3ad693db53b1410957c26c9a51b4908&a=1): Failed to open stream: HTTP request failed! HTTP/1.1 429 Too Many Requests
Filename: helpers/my_audit_helper.php
Line Number: 176
Backtrace:
File: /var/www/html/application/helpers/my_audit_helper.php
Line: 176
Function: file_get_contents
File: /var/www/html/application/helpers/my_audit_helper.php
Line: 250
Function: simplexml_load_file_from_url
File: /var/www/html/application/helpers/my_audit_helper.php
Line: 1034
Function: getPubMedXML
File: /var/www/html/application/helpers/my_audit_helper.php
Line: 3152
Function: GetPubMedArticleOutput_2016
File: /var/www/html/application/controllers/Detail.php
Line: 575
Function: pubMedSearch_Global
File: /var/www/html/application/controllers/Detail.php
Line: 489
Function: pubMedGetRelatedKeyword
File: /var/www/html/index.php
Line: 316
Function: require_once
Manipulating temperature and salt concentration can have a powerful effect on the separation effectiveness in hydrophobic interaction chromatography (HIC). However, use of temperature as an operating variable in large-scale applications may involve undesirable consequences such as radial heterogeneity of the column temperature. In this study non-ideal effects of heat transfer in HIC columns were analyzed. The radial temperature gradients were measured by thermocouples immersed in a bed packed into a preparative column. The column wall was either thermostatted by a water jacket or left under ambient conditions. The influence of ineffective column thermostatting and of heat losses on the radial temperature profiles was demonstrated and predicted by a model of heat dispersion in a packed bed. To analyze possible positive or negative effects of thermal heterogeneity on band propagation, non-isothermal chromatographic elution of a model protein (alpha-chymotrypsinogen A) was recorded under salt gradient conditions as well as at constant salt concentration. To predict temperature and concentration profiles a model of the column dynamics was used. The model accounted for kinetics of mass and heat transfer. A good agreement between experimental and simulated profiles was achieved. It was shown that by proper selection of the process conditions undesirable temperature effects can be avoided or controlled.
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Source |
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http://dx.doi.org/10.1016/j.chroma.2009.08.007 | DOI Listing |
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