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Dive into the research topics where Robert W. Silman is active.

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Featured researches published by Robert W. Silman.


Biotechnology Letters | 1984

CMCase production by Spicellum roseum in liquid and solid culture

Robert W. Silman; John E. McGhee; Rodney J. Bothast

SummaryCMCase was produced by 7 strains of Spicellum roseum in both liquid and wheat bran solid substrate cultures. No growth occurred above 35°C. Maximum enzyme production occurred at 30°C, whereas best enzyme activity occurred at pH 5.0 and 50°C. In liquid cultures of S. roseum, NRRL strains 13103, 13104, and 13106 produced activities of ca. 1.1, 1.5, and 1.5 mg glucose per hr/ml culture supernate at 1 week and 2.9, 1.5, and 2.1, respectively at 3 weeks compared to Trichoderma reesei NRRL 11236 (MCG77), which produced activities of 2.8 and 1.3 at 1 and 3 weeks.


Enzyme and Microbial Technology | 1991

Viability and initial kinetic parameters for dry yeast inocula in batch fermentations

William L. Bryan; Robert W. Silman

A simple method for estimating viability of dry yeast inocula and the initial kinetic parameters, μm (h−1) and νm (h−1), for batch fermentations was developed based on broth assays during the exponential growth phase. Ethanol concentrations of shake-flask broths, determined by assay or calculated from mass loss, were fitted with an exponential growth/production equation as a model. Medium (400 ml, 200 g l−1 sucrose) was inoculated with commercial dry yeast products (Saccharomyces cerevisiae) and fermented at 25°C. Some were presaturated with CO2 for mass loss measurements. A lag period of approximately 15 min was observed before the yeast started producing ethanol. Initial kinetic parameters were similar to published values.


Enzyme and Microbial Technology | 1990

Rolling-sphere viscometer for In situ monitoring of shake-flask fermentations

William L. Bryan; Robert W. Silman

Abstract A rolling-sphere viscometer (RSV) was constructed and evaluated for monitoring apparent viscosities of fermentation broths in shake flasks or test tubes. The apparatus was calibrated by measuring translational velocities of magnetic stainless steel spheres (0.16–0.95 cm diameter) rolling in Newtonian viscosity standards (50–12,500 mPa·s) on surfaces inclined 20° to 70°. The method was applied to fermentation broths of Aureobasidium pullulans. Apparent viscosities fit the power-law equation. Maximum viscosities and minimum power-law indices were reached within 4 to 6 days fermentation time, followed by a decrease in viscosity.


Biotechnology Techniques | 1988

Continuous estimation of viscosity, fluid density, surface tension, and heat output during fermentations

Robert W. Silman

Currently, sensors for measuring fluid density, surface tension, viscosity, and heat output are rarely if ever used in estimating conditions continuously in microbial cultures. Measurement of fluid density and surface tension can be accomplished with differential air pressure-based sensors. Fluid viscosity can be estimated by measuring differential fluid pressures. These three sensors, as tested with cultures, were comprised of glass and rubber tubing, a gas supply for density and surface tension and a peristaltic pump for viscosity. The heat output was estimated with an infrared detector spaced two inches from the bottom surface of a solid-state culture flask.


Biotechnology and Bioengineering | 1980

Enzyme formation during solid‐substrate fermentation in rotating vessels

Robert W. Silman


Weed Technology | 1996

Fermentation Strategies for Improving the Fitness of a Bioherbicide

Mark A. Jackson; David A. Schisler; Patricia J. Slininger; C. Douglas Boyette; Robert W. Silman; Rodney J. Bothast


Biotechnology and Bioengineering | 1979

Production of aflatoxin in corn by a large-scale solid-substrate fermentation process

Robert W. Silman; H. F. Conway; R. A. Anderson; E. B. Bagley


Biotechnology and Bioengineering | 1984

Ethanol production by Zymomonas mobilis in fed‐batch fermentations

Robert W. Silman


Horttechnology | 1997

Using Ultra-high Carbon Dioxide Levels Enhances Plantlet Growth In Vitro

Brent Tisserat; Christopher Herman; Robert W. Silman; Rodney J. Bothast


Biotechnology and Bioengineering | 1980

Hydrolysis of raffinose in a hollow‐fiber reactor using an unrefined mixture of α‐galactosidase and invertase

Robert W. Silman; L. T. Black; J. E. McGhee; E. B. Bangley

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Rodney J. Bothast

National Center for Agricultural Utilization Research

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Brent Tisserat

National Center for Agricultural Utilization Research

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E. B. Bagley

United States Department of Agriculture

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John E. McGhee

United States Department of Agriculture

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L. T. Black

United States Department of Agriculture

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William L. Bryan

United States Department of Agriculture

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C. Douglas Boyette

United States Department of Agriculture

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David A. Schisler

National Center for Agricultural Utilization Research

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E. B. Bangley

United States Department of Agriculture

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H. F. Conway

United States Department of Agriculture

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