Parotid and mandibular salivas, produced at flow rates of 0.055 +/- 0.0038 to 4.45 +/- 0.101 and 0.052 +/- 0.0059 to 4.30 +/- 0.072 ml min-1 respectively by intracarotid infusion of acetylcholine or methacholine, were analysed. During acetylcholine stimulation, the protein concentration ranged from 86.4 +/- 10.17 to 235.0 +/- 23.5 mg l-1 in parotid and from 102.9 +/- 11.54 to 379.6 +/- 38.01 mg l-1 in mandibular saliva. The minimum protein concentrations in parotid and mandibular salivas occurred at 0.5 and 1.0 ml min-1 respectively with the concentration rising progressively at lower and higher flow rates. Both glands maintained constant levels of protein during 90 min of sustained stimulation at constant flow rates of 0.5 and 2.0 ml min-1. The optimum pH for salivary amylase activity lay between 7.4 and 7.9 (mean 7.5-7.6). The amylase activity of parotid saliva ranged between 32.2 +/- 3.81 and 94.5 +/- 24.05 mukat l-1 and the activity/protein ratio was similar at all flow rates (mean, 0.39 +/- 0.049 mukat amylase/mg protein). Amylase levels in arterial plasma were constant within experiments but varied from 8.0 +/- 0.07 to 26.4 +/- 0.24 mukat l-1 between experiments, and were always less than corresponding parotid values. Mandibular amylase activities were low, highly variable or often absent. Methacholine-evoked parotid saliva had lower protein concentrations but similar amylase/protein ratios to acetylcholine-stimulated saliva. Urea concentrations in arterial plasma were constant within experiments but varied from 6.71 +/- 0.092 to 14.2 +/- 0.14 mmol l-1 between experiments.(ABSTRACT TRUNCATED AT 250 WORDS)
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Cardiol Rev
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From the Department of Neurological Surgery, Montefiore Medical Center, Albert Einstein College of Medicine, Bronx, NY.
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School of Chemical & Biomolecular Engineering, Georgia Institute of Technology, Atlanta, Georgia 30322, United States.
Increasing demand for high-purity fine chemicals and a drive for process intensification of large-scale separations have driven significant work on the development of highly engineered porous materials with promise for sorption-based separations. While sorptive separations in porous materials offer energy-efficient alternatives to longstanding thermal-based methods, the particulate nature of many of these sorbents has sometimes limited their large-scale deployment in high-throughput applications such as gas separations, for which the necessary high feed flow rates and gas velocities accrue prohibitive operational costs. These processability limitations have been historically addressed through powder shaping methods aimed at the fabrication of structured sorbent contactors based on pellets, beads or monoliths, commonly obtained as extrudates.
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