Baker developed

R. P. Tye and C. F. Baker, "Development of Experimental Data on Cellular Plastic Insulations Under Simulated Wiater Exposure Conditions," ia Ref 33. 

D. R. Palo, J. D. Holladay, R. T. Rozmiarek, C. E. Guzman-leong, Y. Wang, J. Hu, Y.-H. Chin, R. A. Dagle, E. G. Baker, Development of a soldier-portable fuel cell power system. Part I a bread-board methanol fuel processor, J. Power Sources... 

Dustless (agglomerated) flour— The older types of flour were very dry and dusty, and tended to ball up in large masses when mixed with liquids. Furthermore, it is believ that many professional bakers developed allergies to wheat as a result of the chronic inhalation of airtxjrne flour dust. 

Although a tremendous number of fermentation processes have been researched and developed to various extents, only a couple of hundred ate used commercially. Fermentation industries have continued to expand in terms of the number of new products on the market, the total volume (capacity), and the total sales value of the products. The early 1990s U.S. market for fermentation products was estimated to be in the 9-10 x 10 range. The total world market is probably three times that figure, and antibiotics continue to comprise a primary share of the industry. Other principal product categories are enzymes, several organic acids, baker s yeast, ethanol (qv), vitamins (qv), and steroid hormones (qv). 

R. W. Baker and co-workers. Membrane Separation Systems, Recent Developments and Future Directions, Noyes Data Corp., Park Ridge, N.J., 1991. 

P. J. Baker, ed.. National Institute of Allergy and Infectious Diseases, The Jordan Report, Accelerated Development of Vaccines, 1993, NIH, Bethesda, Md. 

A. J. Baker and T. W. Jeffries, Status of Wood Hydrolysisfor Ethanol Production, Report of U.S. Department of Agriculture, Porest Service, for U.S. Agency for International Development Support Bureau, Office of Energy (TMR Authorization No. 81—89), Washington, D.C., June 1981. 

For fully developed incompressible horizontal gas/hquid flow, a quick estimate for Ri may be obtained from Fig. 6-27, as a function of the Lockhart-MartineUi parameter X defined by Eq. (6-131). Indications are that liquid volume fractious may be overpredicled for liquids more viscous than water (Alves, Chem. Eng. Prog., 50, 449-4.56 [19.54]), and uuderpredicted for pipes larger than 25 mm diameter (Baker, Oil Gas]., 53[12], 185-190, 192-195 [1954]). 

Some 20 years after the pressure for the creation of the new interdisciplinary laboratories was first felt, one of the academics who became involved very early on. Prof. Rustum Roy of Pennsylvania State University, wrote eloquently about the underlying ideal of interdisciplinarity (Roy 1977). He also emphasised the supportive role played by some influential industrial scientists in that creation, notably Dr. Guy Suits of GE, whom we have already encountered, and Dr. William Baker of Bell Laboratories who was a major force in pushing for interdisciplinary materials research in industry and academe alike. A magisterial survey by Baker (1967), under the title Solid State Science and Materials Development, indicates the breadth and scope of his scientific interests. 

Baker, A.A., Bonded Composite Repair of Metallic Aircraft Components — Overview of Australian Activities, AGARD (Advisory Group for Aerospace Research and Development) Conference of Composite Repair of Military Aircraft Structures, 3-5 October 1994, Seville. 

A computer program (TWOPHASE) was developed that uses the Lockliart-Matinelli correlation and determines the total pressure drop based on the vapor phase pressure drop. The total length of the unit depends on the nature of the Reynolds numher. The program also calculates the gas-liquid phase regime employing a modified Baker s map [33]. Table 7-13 gives the results of the two-phase pressure drop. 

Baker and his colleagues (1983) compared the Strehlow et al. (1979) curves to experimental data, then applied them in research programs, accident investigations, and predictive studies. They developed the methods for use of Strehlow s curves. 

Baker et al. (1975) developed a method, presented below, for predicting blast effects fiom the rupture of gas-filled pressure vessels. They include a method for calculating the overpressure and impulse of blast waves from the rupture of spherical or cylindri-... 

Baker et al. (1978a) developed a method which can predict blast pressures in the near field. This method is based on results of numerical simulations (see Section 6.3.1.1) and replaces Step 5 of the basic method (Figure 6.20). The refined method s procedure is shown in Figure 6.25. 

A computer program was developed based upon theoretical considerations. The results of a parameter study were used to compose a diagram (Figure 9.7) for use in determining initial velocity for vessels tilled with an ideal gas (Baker et al. 1978a and 1983). The scaled pressure P on the horizontal axis of Figure 9.7 is determined by... 

General accounts of prototropic tautomerism have been presented by Ingold and Baker" these include an outline of the historical development of the subject in which heteroaromatic compounds are discussed incidentally, and, therefore, such a historical account will not be given here. Of historical interest are Eistert s book on tautomerism and mesomerism which was published in 1938, a review on — NH-CO— tautomerism by Arndt and Eistert published in 1938, and Heller s account of heterocyclic tautomerism which appeared in 1925. Although more recent works on heterocyclic chemistry (e.g., references 9-11) have dealt incidentally with tautomerism, no unified... 

Bioprocess plants are an essential part of food, fine chemical and pharmaceutical industries. Use of microorganisms to transform biological materials for production of fermented foods, cheese and chemicals has its antiquity. Bioprocesses have been developed for an enoimous range of commercial products, as listed in Table 1.1. Most of the products originate from relatively cheap raw materials. Production of industrial alcohols and organic solvents is mostly originated from cheap feed stocks. The more expensive and special bioprocesses are in the production of antibiotics, monoclonal antibodies and vaccines. Industrial enzymes and living cells such as baker s yeast and brewer s yeast are also commercial products obtained from bioprocess plants. 

Finally, I wish to make the point that I was invited to review the results of my own group in this chapter. Many other workers have made important contributions to the organoborane area in recent years. However, progress even within my own group has been so rapid that I could not include all of our own developments in this review. Consequently, I must.apologize to other authors for having restricted this chapter primarily to the topics that have occupied the attention of my students and associates. Fortunately, in my recently published Baker Lectures, Boranes in Organic Chemistry (Cornell Univ. Press, Ithaca, New York, 1972) it has been possible to provide a fuller, more complete treatment. 

The intuitive notion behind a dominance condition, D, is that by comparing certain properties of partial solutions x and y, we will be able to determine that for every solution to the problem y(y) we will be able to find a solution to Yix) which has a better objective function value (Ibaraki, 1977). In the flowshop scheduling problem several dominance conditions, sometimes called elimination criteria, have been developed (Baker, 1975 Szwarc, 1971). We will state only the simplest ... 

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