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  • 1965-1969  (350)
  • 1920-1924
  • 1966  (350)
  • 1920
  • Industrial Chemistry  (294)
  • Biochemistry and Biotechnology  (56)
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  • 1965-1969  (350)
  • 1920-1924
Year
  • 1
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 371-378 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Previous studies indicated that when cells grown in a NaCl-free glucose medium were subjected to a high salt concentration, cellular constituents were released which were metabolized by the cells in preference to glucose. In the present study, cells grown on glucose in high salt medium were subjected to a shock loading of salt-free medium. In this case, the resulting lysate was not used in preference to glucose; the lysate was metabolized only after an acclimation period following glucose utilization. It was shown by injecting chloramphenicol into the reaction liquor during glucose metabolism that new protein synthesis was required in order to metabolize the lysate. This response represents an additional way in which a rapid change in salt concentration can adversely affect biological treatment of waste waters, and a new type of situation in which sequential removal of substrates occurs.
    Additional Material: 2 Ill.
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  • 2
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 337-352 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Oxygen uptake of Penicillium chrysogenum hyphae growing in automatically aerated deep cultures was the subject of local and periodical change. The change depended on the concentration of carbon dioxide which accumulated in the gas phase of system during the evolution of foam bubbles, and which was suddenly liberated when the foam was destroyed. The actual concentration of sunflower oil added as an antifoaming agent also influenced the oxygen uptake of culture.
    Additional Material: 10 Ill.
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  • 3
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 405-431 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 10 Ill.
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  • 4
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 456-460 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 3 Ill.
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  • 5
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 465-471 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The addition of as little as 2 ppb of manganese to ferrocyanide-treated beet molasses during citric acid fermentation by Aspergillus niger NRC A-1-233 caused a 10% reduction in acid yield and undesirable change in the morphology of the organism from the normal pelletlike form to the filamentous from. Still smaller additions (0.4-2ppb) caused undesirable pellet clumping, while greater additions (2-100 ppb) gave further decreases in yield. The yield obtained at 100 ppb was less than 25% of that obtained at 1 ppb or less. None of the other metals tested (Al3+, Ca2+, Co2+, Cu2+, Fe2+, Mg2+, Ni2+, Zn2+) visibly changed pellet morphology, and only Al3+, Fe2+, and Zn2+ at relatively higher concentrations (5-25ppm) reduced acid yield. The adverse effect of manganese on growth and acid production was not affected by addition of the other metals.
    Additional Material: 1 Ill.
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  • 6
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Oxygen Utilization as a scale-up parameter is evaluated in two antibiotic-producing fermentations. This method of scale-up was used in tank-to-tank and in flash-to-flash scale-up studies. Antibiotic yields and cell weight trends were generally duplicated in the replicate runs, with some discrepancy noted in chlortetracycline yields at high aeration levels. The apparatus for measuring oxygen consumption rates and for automatically controlling oxygen utilization, according to a predetermined pattern, is described.
    Additional Material: 9 Ill.
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  • 7
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 581-593 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Biological systems can be used in three types of fuel cell: depolarization (or concentration) cell, product cell, and redox cell. The possibilities and theoretical limitations of each type of cell have been considered in terms of the metabolic activities of microorganisms and the coupling of these to electrochemical systems. The use of cell extracts and enzymes, particularly in an insoluble form, has been discussed.
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  • 8
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 195-215 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In three series of experiments, 3-l., 20-l., and 150-l. bacterial cultures were grown in stirred, deep culture vessels to average bacterial cell densities of 71 × 108, 63 × 108, and 43 × 108 viable organisms per milliliter, respectively, and then infected with phage. The average yield of progeny phage in each case was ca. 3000 mpfu (minimum plaque-forming units) per cell. Thus, the average mass of phage obtained in the 3-l. experiments was not less than 124 mg./l., calculated from the plaque counts, assuming a particle size of 3.6 × 106 Daltons for the μ2 phage. This is about twentyfold higher than is obtainable by conventional methods in aerated, shaken culture flasks. The actual phage yields are probably much higher than the minimum values calculated from plaque counts. For example, in the case of one of our culture lysates which was purified at King's College, the efficiency of plating was shown to be only 19%. The carbon dioxide evolution rate of cultures was measured and used as a guide to the time at which phage should be added. In this way, greater control of cultural conditions was obtained than is possible in shaken flasks. For the best yield of phage per milliliter of culture, the optimum time for phage infection was such that bacterial lysis just prevented the carbon dioxide evolution rate from reaching its potential maximum. The major factor influencing the phage yield per milliliter of culture was the aeration capacity of the culture vessel used. All had maximum aeration capacities much higher than those obtainable in shaken culture flasks. Cultures grown and infected in 3-l. Vessel operated under conditions of low aeration gave poor yields of phage. The reason for this are discussed.
    Additional Material: 1 Ill.
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  • 9
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 453-455 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 1 Ill.
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  • 10
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 461-463 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 1 Ill.
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  • 11
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 25-42 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effects on mass-transfer and overall mixing rates of varying impeller geometry and operating speed have been studied for flat-bladed turbines in laboratory fermentors, in aerated aqueous solutions, and in unaerated and aerated suspensions (1.6% w/v) of paper pulp. In the absence of suspended solid, oxygen absorption rates could be correlated directly with power input. In the pulp suspension, oxygen absorption at a given power input was influenced by impeller geometry and operating speed. The data for the three-phase system can be correlated by a dimensionless equation relating oxygen-transfer rates and mixing times to the geometrical and operating parameters of the impellers.
    Additional Material: 7 Ill.
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  • 12
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 85-96 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Previously, the degree of mixing was not felt to be an important consideration in fermentor design. In this study on the continuous propagation of Baker's yeast, it was found that at low dilution rates, i.e., 0.02hr-1, the degree of mixing achieved does effect the cell yield. At low dilution rates, appreciable quantities of sugar can be utilized for endogenous respiration in comparison to that utilized for making cell mass. Poor distribution of the sugar aggravates the balance of sugar utilized for each process. Yields at these low dilution rates can be improved to a limited extent by using a multiple feed-distribution system and better mixing.
    Additional Material: 10 Ill.
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  • 13
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 167-182 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Probabilistic models for the killing of microorganisms are formulated and described. The utility of the models is illustrated by applying them to the optimization of an idealized fermentation process.
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  • 14
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 193-193 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 15
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 217-235 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A brief review of the development of our knowledge about hydrogen bacteria is presented, with emphasis on the characteristics and physiological differences of various Hydrogenomonas species. One species, Hydrogenomonas eutropha, is discussed in greater detail. Nutritional requirements, physical factors affecting growth, and equipment used for culturing 100-ml. shake cultures and 15-1.mass cultures of H. eutropha are described. Cell-free extracts of H. eutropha carry out the oxyhydrogen reaction as demonstrated by the alternate reduction and oxidation of endogenous flavins and cytochromes by molecular hydrogen and oxygen, respectively. Spectra of cell-free extracts of this organism show the presence of cytochromes of the c and b1 types. A cytochrome of the o type was also found, but none of the a cytochromes were detected. The sum of a series of enzymatic reactions shown to be catalyzed by these extracts can account for the oxidation of hydrogen by oxygen.
    Additional Material: 10 Ill.
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  • 16
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 275-286 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Our program on the mass cultivation of basidiomycetes was designed to determine whether these organisms, being more highly differentiated than bacteria, molds, and yeasts, would in turn carry out markedly different reactions on natural products. A discussion of our methods of isolating and characterizing a representative collection of basidiomycetes and of our difficulties in obtaining pure cultures which grew well is presented. Some information we obtained on the growth and types of products that these organisms produced in a synthetic medium is discussed. Our techniques for examining fermentation beers for transformation products from indole compounds and from progesterone are explained, and the types of products we obtained are described.
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  • 17
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 318-320 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 1 Ill.
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  • 18
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 287-296 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Growth of the ciliate, Colpoda steinii, was studied in shake flasks, 30-l., stirred jars, and a conventional 50-gal. stainless-steel fermentor. This organism was growth with either washed or unwashed Escherichia coli cells as the sole food source. Generation times of 3-4 hr. were obtained at 30°C. With average yields of 78% (0.78 g. of protozoa/g. of bacteria). In a 100-l. fermentation, a dry weight concentration of 12.5 g./l. (1.04 × 107 protozoa/ml.) was reached by means of periodic addition of E. coli paste. The influence of bacterial concentration on the growth rate of the protozoa was also investigated. It was found that this relationship could be represented by a Michaelis-Menten equation with a maximum specific growth rate of 0.23 hr. -1 (3-hr. generation time) and a bacterial concentration for half-maximum growth rate of 6.0 mg. (dry wt.)/l.
    Additional Material: 3 Ill.
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  • 19
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 315-317 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 20
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 323-336 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An experimental investigation of the foam separation of E. coli from distilled water suspension using a cationic surface-active agent, ethylhexadecyldimethyl-ammonium bromide (EHDA-Br) is presented. Results are evaluated in terms of total cell count, using a membrane filtration technique. Cell concentrations in the initial suspensions are varied from 5.0 × 105 to 1.0 × 108 cells/ml. Surfactant concentrations in the initial cell suspensions are varied from 0.015 to 0.040 mg./ml., and foaming times are varied from 2 to 20 min. The residual quantity of cells decreases exponentially with foaming time to about 0.02% of the initial quantity after 20 min. The cell enrichment ratio, varying from 10 to 1,000,000, is an inverse power function of the initial surfactant concentration and an exponential function of foaming time. Foaminess decreases with increasing initial cell concentrations, and for an initial surfactant concentration of 0.030 mg./ml., the residual cell concentration is a linear function of the initial cell concentration.
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  • 21
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 11 Ill.
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  • 22
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Presented is a mathematical model for the continuous-flow steady-state bacterial culture which permits the experimental determination of carbon transfer rates within the system by use of radioactive tracer techniques. The transfer rates are specific for hydraulic loading rates, feed concentrations, type of organism, and substrate, and were incorporated within the existing theoretical description of the growth kinetics in order to elucidate the yield relationships. The carbon transfer rate of cells to soluble organic substrate was observed to exhibit a minimum value at or near dilution rate D = 0.5 hr.-1. A maximum effective yield coefficient, Y, was observed at the same value of D. At dilution rates greater and less than D = 0.5 hr.-1, the cell-substrate transfer rate increased, and effective yield coefficient was observed to decrease. The former showed increases of 50-200%, and the latter exhibited decreases of the order of 10%. The magnitude of these variations would seem to be significant in industrial fermentation processes which utilize continuous microbiological cultures. In light of these findings, the results of other researchers were shown to exhibit maximum effective yield at similar dilution rates or process loadings.
    Additional Material: 6 Ill.
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  • 23
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 473-488 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An improved system is presented for measurement of interactions between a number of individual bacterial species. In the procedure, steady-state populations are fed into a common-mixed-culture vessel. Generation times of each species are determined under these conditions and contrasted with generation time in an identical situation in pure culture. Populations for generation time are determined with the aid of differential media. The mechanical system includes three types of peristaltic pumps for media feed and a unit for measurement, recording, and/or control of pH. A new type of anaerobic continuous-culture vessel which can be inoculated, sampled, and fed continuously is also described. A functional test of a three-part system including Streptococcus salivarius, Veilloncella alcalescens, and Staphylococcus aureus is presented. An unusual feature was the finding that, under certain conditions, the generation time of S. Salivarius was less than 10 min.
    Additional Material: 7 Ill.
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  • 24
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The requirements of the continuous analysis of effluent gas streams from aerated flash and tank fermentors are described, as are instrumental devices for measuring the oxygen and carbon dioxide content of fermentor gases. The use of a specially designed sequential gas sample for monitoring four fermentations simultaneously and a system for precise control of low air flow and pressure is explained. Equations for calculating carbon dioxide production or oxygen consumption rates and respiratory quotients are given. A discussion of the operating characteristics of a device for automatic translation of aeration data between fermentors is presented.
    Additional Material: 7 Ill.
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  • 25
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 595-619 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 8 Ill.
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  • 26
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 43-54 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Power requirements in the agitation of non-Newtonian fermentation broths with and without aeration were measured by a strain gage-type dynamometer. Broth from the production of gluc-amylase by Endomyces species and carboxymethyl cellulose solutions were used as non-Newtonian fluids. In gas-liquid agitation systems, the correlation between Pg and P02 ND3/Q0.56 observed by Michel and Miller was found to be applicable to non-Newtonian fluids in laminar and transition regions. This was particularly true for fluids with apparent viscosities larger than 300 cp. The impeller diameter and impeller blade width had considerable effects on power consumption in a nongassed system. It was suggested, therefore, that Pg/P0 should be correlated by a dimensionless term involving some impeller-size factors.
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  • 27
    Electronic Resource
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 97-108 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Dissolved oxygen measurements were made in pilot (20 and 250 l.) and production scale (15,000 l.) novobiocin fermentations. Bulk mixing was found to be incomplete in pilot tanks with turbine impellers of D/T = 0.40 (where D is impeller diameter, and T is tank diameter) but appeared homogeneous with impellers of D/T = 0.69. In the former case, the respiration rate was presumably limited by insufficient oxygen supply in areas of poor bulk mixing, whereas, in the latter case, the major resistance was between the bulk of the liquid and the cell (intraclump resistance). Higher agitator speeds decreased the gas-liquid resistance proportionally more than they reduced the liquid-cell resistance. In production fermentors, dissolved oxygen measurements indicated that bulk mixing was complete with each of the three impeller sizes tested (D/T = 0.28, 0.33, and 0.43), but that the respiration rate was again limited, mainly by a resistance between the bulk of the liquid and the cell.
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  • 28
    Electronic Resource
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 117-134 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A system of automatic control of substrate inflow into an aerated culture of microorganisms which depend on oxygen-absorption rate (OAR) has been devised and tested. As the control variable, dissolved oxygen concentration (DOC), which shows the equilibrium between OAR and oxygen-uptake rate in the microbial culture, was chosen. If the equilibrium is disturbed by changes in OAR, then the oxygen-uptake rate is changed by substrate limitation. The DOC is measured by means of a Clark-type polarographic electrode, and the signal is used to actuate the substrate inflow valve or pump. The oxygen-uptake rate changes of microorganisms, after the addition or exhaustion of substrate in the medium, are so rapid that they can be used for this type of control.Fundamental equations were derived and graphical solutions for the control system parameters were suggested for the steady-state relations between DOC, oxygen-uptake rate, specific growth rate, substrate concentration, KLa, and concentration of microorganisms. The system is stable in the entire range of the uptake rates up to nearly the maximum attainable in unlimited substrate conditions, and can be operated in batch feed or continuous flow modifications. It was experimentally tested with the yeast Saccharomyces cerevisiae. The complete utilization of aeration-system capacity of the fermentor was achieved with high yeast yield and no alcohol formation. The quality of the product was excellent.
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  • 29
    Electronic Resource
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 135-151 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Foam separation of microorganisms has been investigated with varying success by many workers, usually at high rates of gas flow. Microflotation was developed to overcome some of the disadvantages inherent in these high gas-flow-rate processes and is introduced in this paper as a new technique for the foam separation of microorganisms at low gas-flow rates. With microflotation, a stable surface phase is produced by adding an insoluble collector such as a long-chain fatty acid or amine. The formation of an insoluble surface phase eliminates the need for high foaming. Low rates of gas flow are used resulting in a more efficient separation and a less voluminous and drier surface phase upon which to collect the microorganisms. The efficiency of this technique is also improved by using flotation aids such as frothers and flocculents. Frothers are used to improve the collector properties of the surfactant and to refine further the small bubbles produced by a very fine sparger. Small concentrations of flocculents, such as alum, are used to partially agglomerate the organisms and provide sites for adsorption of collector. The work described in this paper is preliminary in nature, designed to illustrate that a low flow-rate process may be used to separate microorganisms and to stimulate further research. The applications discussed are removal of the bacterium, Escherichia coli, and alum, and two species of algae, Chlamydomonas reinhardtii and Chlorella ellipsoidea, using stearylamine without alum. The frother used was ethanol.
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  • 30
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 189-191 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 31
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966), S. 297-313 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Observations on quantitative relationships between oxygen diffusion rate and product formation were made with penicillin, bacitracin, and gluconic acid. For penicillin and gluconic acid formation, no toxic oxygen concentration could be achieved in the broth, whereas concentration above approximately 7 mg. O2/l. suppressed the bacitracin yield to an ever increasing extent. The intensity of mixing was measured by means of distributing a dye. With penicillin formation as an example, it was shown that the antibiotic yield is not only dependent on maintenance of a certain oxygen diffusion rate, but also on ensuring a necessary minimal mixing.
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  • 32
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    Biotechnology and Bioengineering 8 (1966) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 33
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    Biotechnology and Bioengineering 8 (1966), S. 353-369 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 9 Ill.
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  • 34
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    Biotechnology and Bioengineering 8 (1966), S. 464-464 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 35
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Polysaccharide gum was made by fermentation with Xanthomonas campestris NRRL B-1459 in a medium of glucose, minerals, and distillers' solubles. The effect of distillers' solubles on growth rate can be described by the familiar saturation equation. Although a quasistoichiometric relationship was observed between nitrogen utilization and growth, total nitrogen supply was not growth limiting, nor was polymer formation growth associated. Cell growth primarily took place in the early part of the fermentation; polysaccharide biosynthesis occurred throughout the fermentation. Glucose was converted to polysaccharide at a fairly constant yield, which was 70-80% of glucose consumed, under optimum conditions. The kinetic patterns observed indicate that multistage continuous fermentation will be suitable for polysaccharide production.
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  • 36
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    Biotechnology and Bioengineering 8 (1966), S. 549-565 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A stable mixed yeast culture designated as Culture 4, consisting of Candida intermedia and Candida lipolytica was investigated. The culture was judged stable based on uniformity of fermentation results and the nearly constant ratio of the two organisms at the completion of fermentations. However, the ratio of the two organisms at different times during the fermentation was not determined. The mixed culture grew more rapidly on n-alkanes than did C. intermedia; C. lipolytica did not grow on unsupplemented mineral salt-n-alkane medium. Solid n-alkanes were dissolved in 2,6,0,14-tetramethylpentadecane (pristane) for investigation as carbon sources. With Culture 4, on n-alkanes ranging from pentadecane (C15) through octacosane (C28), cell yields were 74.2-89.5%; generation times were 3.0-8.0 hr. during the exponential growth phase. The fastest growth rates and highest cell yields were obtained with docosane (C22) as substrate. The cells obtained contained 6.75-8.81% nitrogen and 1.9-13.4% lipid. Crude protein yields were 34.4-47.6%. The oxidation of n-alkanes by C. intermedia was studied manometrically with resting whole cells. The alkaneoxidizing system of this organism appears to be constitutive and nonspecific for alkane substrates.
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  • 37
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    Biotechnology and Bioengineering 8 (1966), S. 631-632 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 38
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 39
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The Meta-Stat gas monitor, a component instrument which automatically monitors and controls the pH and gas content of the liquid phase in suspension cell-culture systems, has been developed to provide continuous pH control within ± 0.015 units, as well as continuous oxygen control within 0.5% of the preset level in the range of 0-40% O2.
    Additional Material: 10 Ill.
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  • 40
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    Biotechnology and Bioengineering 8 (1966), S. 567-580 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A mixed yeast culture (Culture 4) was grown on representative gas oil samples as well as paraffin wax. Culture 4 was found to utilize n-paraffinic hydrocarbons almost quantitatively from most gas oil fractions; significant alteration of other hydrocarbon components was not detected. Generation times of 4.0-9.0hr. were typical during the exponential growth phase in fermentations with various gas oil fractions. Cell yields were 70-90% based on n-paraffin utilization. The culture appeared to exhibit maximum efficiency of n-alkane removal in the C19 to C24 range. The cells recovered from the fermentations contained 8.8-9.3% nitrogen. Paraffin wax also served as a suitable carbon source when dissolved in 2,6,10,14-tertramethylpentadecane (pristane). However, substrate utilization appeared to be incomplete.
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  • 41
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    Biotechnology and Bioengineering 8 (1966), S. 3-24 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Scale-up of a mixing process in fermentation involves breaking the process down into individual but interrelated steps. The effect of mixing on gas-liquid absorption, fluid shear rates, blending, and heat transfer allows each to be considered separately. A method of estimating the mixer size required in a full-scale system from pilot studies illustrates the application of a particular technique.
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  • 42
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    Biotechnology and Bioengineering 8 (1966), S. 71-84 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A model system, utilizing shear-sensitive protozoa, has been developed for characterizing the disruptive forces in agitated systems. The model system gives a measure of the maximum shear stresses in the apparatus being tested, and is particularly useful when tissue fragility is a factor in fermentor design. The time dependency of protozoan disruption is shown and discussed. Breakdown data in conventional stirred vessels and a laminar shear device are presented and discussed.
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  • 43
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    Biotechnology and Bioengineering 8 (1966), S. 153-165 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The design and operation of a permanently-piped plant for sterilizing 10-200 l. of tissue-culture media is described. The plant is sterilized in situ by steam injection, the filtration rate is 2-3 l./min., and the turn-around time for volumes of 100 l. is about 3 hr.
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  • 44
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 8 (1966) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 45
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    Biotechnology and Bioengineering 8 (1966), S. 237-245 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Extremely halophilic bacteria, which are able to grow in, and require, saturated or near-saturated salt solutions are both of historical interest and of practical importance as food spoilage organisms. In addition, because of the environment in which they live, their membranes, enzymes, and ribosomes have unusual or unique properties that make them especially worthy of physiological study. A simple method for growing large quantities of extreme halophiles is described, and various growth media, both complex and synthetic are discussed.
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  • 46
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    Biotechnology and Bioengineering 8 (1966), S. 259-273 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A chemically defined medium for Micromonospora purpurea has been devised, consisting of glucose, a nitrogen source, calcium carbonate, magnesium sulfate, dibasic potassium phosphate, and the required trace quantities of iron, copper, zinc, and manganese. Using washed cell inocula, dry mycelial weights of more than 16 mg./ml. were obtained in 7-day shaken-flask fermentations. Nutrient requirements for M. purpurea are discussed and growth data presented. Sucrose, maltose, starches and dextrins could be substituted for glucose, and resulted in good growth of the organism. A number of amino acids and inorganic nitrogen-containing compounds were capable of utilization as sole nitrogen sources. Weekly serial transfers of the culture in defined medium have shown no diminution in mycelial weights over a four-month period.
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  • 47
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    Biotechnology and Bioengineering 8 (1966), S. 321-321 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 48
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    Biotechnology and Bioengineering 8 (1966) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 49
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    Biotechnology and Bioengineering 8 (1966), S. 1-1 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 50
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    Biotechnology and Bioengineering 8 (1966), S. 55-69 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: By means of gas-absorption experiments in a stirred vessel, with various depths of liquid above a properly positioned single-opening pipe-type gas sparger, conclusions are reached about relative contributions to the overall absorption rate by localized actions near the sparger tip, in the impeller region, and from bubbles distributed in the bulk volume of the fluid. Results are discussed for difficulty soluble gases (oxygen in water and chlorine in water) and a substantially soluble gas (chlorine in benzene). In all cases, dissolution rates in the vicinity of the sparger and impeller were significantly large compared with those near free bubbles.
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  • 51
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    Biotechnology and Bioengineering 8 (1966), S. 109-115 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The performance of a multiple-rod mixing impeller was compared to that of conventional turbine impellers in viscous novobiocin beers. The advantages of the multiple-rod impeller were found to be: (1) the power requirement was independent of changes in apparent viscosity of the fermentation beer; and (2) it gave the same novobiocin yield and oxygen-availability rate at about one-half of the power required by turbines.
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  • 52
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    Biotechnology and Bioengineering 8 (1966), S. 183-188 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A versatile and simple continuous-culture apparatus is described. With this apparatus, independent control of limiting growth factors and other nutrilites is possible and the conditions of each experiment are reproducible. In view of the synchronized speed of the feeder syringes, flow variation troubles are not encountered. The device allows the performance of growth experiments at different dilution rates simultaneously in a single run which makes the comparison of the results more reliable. The operation of the device has been tested successfully with a study of adenine deaminase induction in yeast.
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  • 53
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    Biotechnology and Bioengineering 8 (1966), S. 247-258 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The insect pathogen Bacillus popilliae Dutky causes a fatal milky disease of Japanese beetle larvae. Spores of the bacterium offer a biological means of controlling this insect. While satisfactory sporulation in vitro has not yet been accomplished, conditions have been developed for the proliferation of vegetative cells in shaken flasks and aerated fermentors. Vegetative cultures are maintained by frequent transfer or by lyophilization. Media based on yeast extract are used routinely, but corn steep liquor and casein hydrolyzates afford comparable yields of 5 × 108 cells/ml. in 16-24 hr. Nutritional requirements have been established for growth in a synthetic medium. Oxygen availability affects the pathway of carbohydrate catabolism and is necessary for optimal growth. In rapidly growing cultures, a short period of maximum viability is characteristically followed by rapid death of the cells. When inoculum size and transfer time are suitably manipulated, viable cell yields reach 1-2 × 109/ml. Alternative methods of propagation, including the addition of particulate carbon, and procedures designed either to neutralize acids or to remove metabolic products by dialysis, do not markedly enhance the yield of cells per volume of medium, although viability may be prolonged.
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  • 54
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    Biotechnology and Bioengineering 8 (1966), S. 621-624 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 1 Ill.
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  • 55
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    Biotechnology and Bioengineering 8 (1966), S. 379-388 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A multiphase project has been planned to develop a new biological process capable of economically treating high BOD wastes. Herein is presented the results of the first phase of the program, in which the feasibility of growing concentrated microbial cultures was investigated and the oxygen and power requirements for maintaining such cultures were determined. An example is given of the scale-up of power requirements for oxygen transfer in a prototype system.
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  • 56
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    Biotechnology and Bioengineering 8 (1966), S. 625-629 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 5 Ill.
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  • 57
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 10-13 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Sollen in der Hochtemperatur-Pyrolyse flüssige Kohlenwasserstoffe gespalten werden, so darf die Drall-Komponente des Brennergases einen gewissen Wert nicht überschreiten. Das Brennergas würde sonst die größeren Öltröpfchen, die nicht vollständig verdampfen, an die Wand des Reaktors schleudern, wo sie eine Koksschicht bilden. Die Differentialgleichung für die Bewegung eines Tröpfchens in einem rotierenden Gasstrom wird aufgestellt und mit Hilfe eines Analogrechners gelöst. Daraus ergibt sich der Drall, der bei der Konstruktion von Brennkammern für flüssige Kohlenwasserstoffe zulässig ist.
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  • 58
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 279-287 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Der Verlauf einer heterogenen chemischen Reaktion bei laminarer Strömung und gleichmäßiger Geschwindigkeit über den Rohrquerschnitt wird berechnet und mit dem in einer früheren Arbeit untersuchten Reaktionsablauf bei ausgebildeter parabolischer Geschwindigkeitsverteilung verglichen. Außerdem wird die heterogene chemische Reaktion in Kugelschüttungen berechnet. Vorausgesetzt werden ein isothermer Reaktionsablauf und ein Reaktionsgesetz erster Ordnung.
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  • 59
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 1-10 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Ein Verfahren der Chemischen Werke Witten zur Herstellung von Terephthalsäure-dimethylester durch Luftoxidation von p-Xylol in flüssiger Phase hat in der Industrie eine beachtliche Bedeutung erlangt. Es wird die Entwicklung des Verfahrens beschrieben. Aus dem Reaktionsablauf wurden neue Erkenntnisse über den Oxidationsmechanismus gewonnen. Charakteristische Zwischenprodukte sind der p-Toluylsäure-methylester und der Terephthalsäure-monomethylester.
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  • 60
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 137-145 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Zur Berechnung von Verweilzeitspektren bei stationärem Transport wird das Diffusionsmodell als stochastischer Prozeß eingeführt. Der Zusammenhang zwischen Mittelwert und Streuung des Verweilzeitspektrums und den Transportgrößen des Diffusionsmodells wird in Strenge allgemein ermittelt. Die Untersuchung zeigt, daß die zeitliche Verteilungsdichte des aus dem Bilanzgebiet austretenden Spurstoffes der idealen Stoßmarkierung i.a. nicht mit der zeitlichen Verteilungsdichte der Konzentration an der Meßstelle übereinstimmt. Am Beispiel einer Modellkugelmühle werden die Rechnungen praktisch angewandt.
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  • 61
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 357-366 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Hohlrührer sind hohl ausgebildete und an einer Hohlwelle angebrachte Rührer, die gleichzeitig zum Rühren und zum Fördern von Gasen dienen. Mit einem Hohlrührer von niedriger spezifischer Wellenleistung wurde die Abhängigkeit des Soges und der Wellenleistung von den kinematischen, stofflichen und geometrischen Einflußgrößen untersucht. Es stellte sich heraus, daß neben Rührerdrehzahl und -durchmesser nur noch die Viscosität der Flüssigkeit und die Flüssigkeitshöhe über dem Rührer einen stärkeren Einfluß auf den Sog und die Wellenleistung ausüben. Die dimensionslosen Ausdrücke für Sog und Wellenleistung sind im wesentlichen nur eine Funktion der Froude-Zahl. Unter betrieblichen Bedingungen läßt sich an Stelle des dimensionslosen Ausdruckes für den Sog ein solcher für die durchgesetzte Gasmenge einführen, der ebenfalls eine Funktion der Froude-Zahl ist und eine schnelle Bestimmung des jeweiligen Gasdurchsatzes ermöglicht. Dabei ergeben sich optimale Werte für Rührerdrehzahl und -durchmesser, bei denen die zugehörige Wellenleistung ein Minimum erreicht.
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  • 62
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 380-390 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 63
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 397-403 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Produktionsanlagen der Chemie können durch Überholung des Produktes, des chemischen Verfahrens, der verfahrenstechnischen Prozeßführung oder durch unzureichende Kapazität veralten. Die einzelnen Apparate unterliegen dem technischen Verschleiß, während vollständige Produktionsanlagen der Gefahr einer wirtschaftlichen Überholung in Verbindung mit der Ertrags- und Gewinnentwicklung ausgesetzt sind. Die überholte Anlage muß mit klarer Einschätzung der wirtschaftlichen Folgen weiterbetrieben, vorübergehend oder endgültig stillgelegt werden. Eine Vorausschätzung der Überholungsrisiken und der wirtschaftlichen Lebensdauer bereits bei der Planung der Anlagen ist nur begrenzt möglich. In Teil II dieser Arbeit werden Kosten und Rentabilität von Einzelapparaten und vollständigen Anlagen in Abhängigkeit von Nutzungsdauer und Stillegungszeit untersucht. Dabei werden vor allem die grundlegenden Zusammenhänge geklärt, während konkrete Zahlenwerte für jeden Betrieb unterschiedlich sind und daher nicht mitgeteilt werden.
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  • 64
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 423-428 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Die Farbe anorganischer Pigmente kann variiert werden durch Veränderung der Absorptionskonstanten (Einbau farbgebender Kationen) oder der Streu-Konstanten; diese wiederum wird von Brechugsindex, Teilchengröße, -form- und -verteilung sowie von der Pigmentvolumenkonzentration beeinflußt. Farbton und spektrale Farbdichte roter α-Fe2O3-Pigmente hängen linear von der Teilchengröße und der Verteilungsbreite ab. Bei gleicher Teilchengröße und farbtongleicher Wellenlänge nimmt die spektrale Farbdichte bei Abnahme der Standardabweichung In σg sehr stark zu.
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  • 65
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 229-234 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Zu den vielfältigen Möglichkeiten der Zerkleinerung gehört auch das Desagglomerieren auf Walzenstühlen und in Knetmaschinen. Dabei werden in hochviscosen Medien suspendierte Feststoffteilchen durch Strömungskräfte beansprucht und zerkleinert, sofern die Beanspruchung die Festigkeit der Teilchen überschreitet. Diese Beanspruchung von Agglomeraten wurde in einer Versuchsapparatur nachgeahmt. Dabei konnten die Ergebnisse einer früheren Arbeit bestätigt werden, in der das Verhalten und die Beanspruchung einer Kugel in einer langsamen, zähen Scherströmung rechnerisch untersucht worden war.
    Additional Material: 11 Ill.
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  • 66
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 127-133 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Die medizinische Technik bestimmt in steigendem Maße die Fortschritte und Erfolge der chirurgischen, experimentellen und allgemeinen Medizin. Am Beispiel der künstlichen Nieren und Herz-Lungen-Maschinen wird gezeigt, daß die technisch-physikalische Grundkonzeption dieser Apparate mit den Problemstellungen und Forschungsthemen der Verfahrenstechnik vieles gemeinsam hat und die Mitarbeit des Verfahrens-Ingenieurs geradezu herausfordert.
    Additional Material: 11 Ill.
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  • 67
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 627-630 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Der Wirkungsgrad der Stromaufnahme nach Laden bei verschiedenen Stromdichten und Temperaturen wurde an positiven und negativen Platten von Blei-Akkumulatoren bestimmt, indem die entnehmbare Strommenge gemessen wurde. Es zeigte sich, daß der Wirkungsgrad der Ladereaktion mit sinkender Temperatur und steigender Stromdichte abnimmt, da ein immer größerer Teil des Ladestromes zur Sauerstoff- bzw. Wasserstoff-Entwicklung verwendet wird. Dabei ist die negative Elektrode empfindlicher als die positive, sowohl gegen Temperaturerniedrigung als auch gegen Stromerhöhung. Der Wirkungsgrad der Ladereaktion sinkt nicht infolge einer Verschiebung der Gleichgewichtspotentiale ab, sondern auf Grund kinetischer Hemmungen.
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  • 68
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 651-652 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 2 Ill.
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  • 69
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 649-651 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Eine Übertragungsleitung ohne Induktion und mit vollkommener Isolierung bildet ein elektrisches Analogiemodell der Diffusion und gestattet es, quantitative die Konzentrationsänderungen einer diffundierenden Substanz innerhalb einer homogenen Phase nachzuahmen. Es läßt sich für potentiostatische, potentiokinetische, galvanostatische und galvanokinetische Untersuchungen elektrochemischer Diffusionsvorgänge heranziehen und ist auch auf Wechselstrommessungen anwendbar, wenn man die Kreisfrequenz und die Impedanz berücksichtigt.
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  • 70
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 1183-1186 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Quer angeströmte Rohre von Rohrbündel-Wärmeaustauschern können durch Wirbelablösung zu Schwingungen angeregt werden, die in ungünstigen Fällen zur Beschädigung oder Zerstörung der Rohre führen. Durch einfaches Abschätzen von Erreger- und Eigenfrequenzen lassen sich konstruktive Maßnahmen angeben, wie derartige Schäden zu vermeiden sind. Von großem Einfluß sind der Abstand der Umlenkbleche sowie die richtige Kombination von Rohrdurchmesser und Wanddicke des Rohres.
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  • 71
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 1201-1202 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 1 Ill.
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  • 72
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    Chemie Ingenieur Technik - CIT 38 (1966) 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 73
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 1287-1295 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Die Hauptbestandteile des Fuselöls (Isoamylalkohol und 2-Methyl-butanol-1) lassen sich nach Überführung in die Chloride durch extraktive Destillation mit 1,2-Dibrom-3-chlorpropan als Zusatzstoff trennen. Das Verfahren erfordert aber gläserne Kolonnen, da sich der Zusatzstoff unter dem katalytischen Einfluß von Metallen zersetzt. Die Chloride können ferner durch Flüssig/flüssig-Extraktion mit dem System 1,2-Dibrom-3-chlorpropan/Glykol + Methanol getrennt werden, jedoch liegt der Trennfaktor mit 1,09 nur wenig über 1. Eine vollständige Trennung der Alkohole in die reinen Komponenten gelang durch präparative Gaschromatographie mit Triäthanolamin oder Nonylphenol als stationärer Phase. Die Dichte, der Brechungsindex und die optische Drehung der reinen Isomeren sowie die daraus hergestellten Chloride wurden neu ermittelt und mit Literaturwerten verglichen.
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  • 74
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    Source: Wiley InterScience Backfile Collection 1832-2000
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    Notes: Mit 114 ausländischen von insgesamt 502 Ausstellern wiese diese dritte Ausstellung für die Chemie und Erdöl-Industrie im Londoner Olympia erstmals internationale Beteiligung auf, während die beiden vorigen - 1958 und 1962 - noch rein nationale Veranstaltungen gewesen waren. Der ausländische Besucher wird jedoch vor allem die Gelegenheit benutzt haben, einen Eindruck von der Leistungsfähigkeit der englischen Industrie auf diesem Gebiet zu gewinnen. Da zudem bereits 1967 die nächste ACHEMA in Frankfurt a. M. stattfindet, werden in diesem Bericht vor allem neuere Entwicklungen englischer Firmen besprochen. Eine vollständige Aufzählung aller Aussteller und ihrer Erzeugnisse ist nicht möglich. - Über den zusammen mit der Ausstellung veranstalteten Vierten Kongreß der Europäischen Föderation für Chemie-Ingenieur-Wesen berichten wir ebenfalls in diesem Hefts. S. 1310..
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  • 75
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 1202-1203 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 76
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 1215-1218 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 5 Ill.
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  • 77
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 1224-1224 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 78
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 1229-1240 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Der Wärmeübergang vom Schneckenmantel einspindeliger Schnecken mit gleichmäßigem Profil auf Newtonsche Flüssigkeiten wird durch Versuche mit Silicon-Ölen systematisch untersucht. Das Auswertungsverfahren wird mathematisch begründet, und die Ergebnisse werden auf ihre strömungsphysikalischen Ursachen zurückgeführt. Von besonderer Bedeutung für den Wärmeübergang erweist sich der Anströmwinkel, mit dem die Strömungslinien der Spaltströmung zwischen Spindelkamm und Schneckenmantel den Spindelkamm überqueren. Zur Berechnung der Wärmeübergangszahlen wird ein Nomogramm angegeben. Die Untersuchung zeigt, daß die drei wichtigsten verfahrenstechnischen Aufgaben einer Schneckenmaschine - Fördern, Homogenisieren und Wärmeaustausch - bei optimaler Nutzung unterschiedlich ausgelegte Schneckenmaschinen erfordern.
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  • 79
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 1265-1270 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Ein Festbett aus Stahlkugeln von 42 mm Dmr. wurde mit einem Fließbett aus Glaskugeln von 40 und 60 μm Dmr. kombiniert, und an dem kombinierten System wurden Druckverlust und Vermischung gemessen. Die Glaspartikel wurden erst beim Siebzigfachen der Lockerungsgeschwindigkeit aus dem Fließbett-Festbett-System ausgetragen. Die radiale Vermischung war so gering wie im Festbett allein, die Rückvermischung unterblieb vollständig. Der Koeffizient der axialen Vermischung hat dagegen dieselbe Größenordnung wie in reinen Fließbetten. Die axiale Vermischung ist im kombinierlen System jedoch ausschließlich auf Konvektion (Ungleichmäßigkeit der Anströmgeschwindigkeit) zurückzuführen und nicht - wie beim reinen Fließbett - auf Diffusion.
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  • 80
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 1323-1323 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 81
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 1320-1322 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 82
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 134-136 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Durch Nachbilden der Methan-Chlorierung auf einem Analogrechner wird gezeigt, wie sich bei Mehrstufenreaktionen die zunächst durch die Reaktionskinetik festgelegten Produktmengen durch wählbare Rückführung einzelner Zwischenprodukte wunschgemäß ändern lassen. Mit einer geeigneten Kostenfunktion kann dann das wirtschaftliche Optimum ermittelt werden.
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  • 83
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 151-154 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Zur Messung des Siedegleichgewichtes der Gemische HF/SO2 und HF/H2O/HSO3F bei Drücken von 1 bis 3 Atm wurden Versuche an einer neuen Apparatur vorgenommen, die durch den Umlauf von Dampf und Flüssigkeit gekennzeichnet ist. Die erhaltenen Temperatur-Zusammensetzungs-Diagramme werden kritisch geprüft, z. B. durch Nachrechnen der Grenzneigung von Siede- und Taulinien und durch Berechnen von Aktivitätskoeffizienten.
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  • 84
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 180-181 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 2 Ill.
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  • 85
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 187-189 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 86
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 197-198 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 87
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    Chemie Ingenieur Technik - CIT 38 (1966) 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 88
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 250-254 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Bei der Optimierung nach unterschiedlichen wirtschaftlichen Gesichtspunkten ist die genaue Erfassung des Trends von Funktionen in einem einzugrenzenden Bereich von besonderer Bedeutung. Mit dem hier erläuterten Begriff der Progression ist dies für verschiedenartige Modellfunktionen in gleicher Weise möglich, wie an Beispielen aus der Verfahrenstechnik erläutert wird. Ausschlaggebend für wirtschaftliches Optimieren sind die Erfolgsfunktionen. Faßt man die unterschiedlichen, beim Optimieren von Anlagen zu berücksichtigenden Funktionen zusammen, so kann man mit Hilfe ihrer Progressionen und einer verbindlichen Bedingungsgleichung klären, ob überhaupt oder unter welchen Umständen bestimmte wirtschaftliche Forderungen erfüllbar sind.
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  • 89
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 69-72 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Der bekannte Zusammenhang zwischen dem stationären Reaktionsverlauf in einem Durchflußreaktor und dessen Verwellzeitverteilung werden grundsätzlich vektoranalytisch diskutiert. Die Berechnung dieses Problems erstreckt sich auf Durchflußreaktoren beliebiger geometrisch-hydrodynamischer Beschaffenheit bei unvollständiger Segregation.
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  • 90
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 82-82 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 91
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 87-88 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 92
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 97-98 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 93
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 154-159 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In der optischen Pyrometrie ermittelt man im allgemeinen die schwarze Temperatur, die ziemlich weit unterhalb der wahren Temperatur liegt. Folgende Verfahren werden besprochen, mit denen man unmittelbar die wahre Temperatur messen kann: photoelektrische Messung der Farbtemperatur, Polarisations-Pyrometrie unter geneigter Beobachtungsrichtung und Emissionsausgleich durch Aufprojektion.
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 145-150 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Kernbrennstoffe, in denen z. B. Molybdän, Niob usw, enthalten sind, lassen sich nach den sauren Aufschlußverfahren nur schwierig aufbereiten, da der erhaltene voluminöse Molybdänoxidhydrat-Niederschlag sehr viel Brennstoff adsorbiert und sich schlecht abscheiden läßt. Durch ein oxidierendes, alkalisches Schmelzaufschlußverfahren, z. B. mit NaNO3, NaNO3/NaOH oder NaNO3/Na2CO3, wird dagegen das Molybdän in lösliches Alkalimolybdat übergeführt, während der Brennstoff selbst einen kristallinen, leichtfiltrierbaren Niederschlag bildet, der nur noch geringe Mengen ( 〈 1%) Molybdän enthält. Beim Schmelzaufschluß sind die Brennstoff-Verluste niedriger als beim sauren Aufschluß, und ein Teil der radioaktiven Spaltprodukte wird bereits im „Head-end-Proze“ abgetrennt.
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  • 95
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 192-196 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 7 Ill.
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  • 96
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 202-204 
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    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 97
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 112-117 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An siedende Flüssigkeiten können extrem hohe Wärmestromdichten bis zu 6000 kW/m2 Heizfläche bei mäßigen Temperaturdifferenzen übertragen werden. Kleine Abweichungen von diesen hohen Wärmestromdichten können jedoch je nach Art der Energiezufuhr entweder zu einem plötzlißchen Temperaturanstieg der Heizfläche oder zu einer plötzlichen Verringerung der Wärmestromdichte führen. Die Temperatur kann so stark ansteigen, daß die Heizfläche schmilzt (burn-out). Die Widerstandsgerade des Verdampfers läßt sich aber so wählen, daß diese im allgemeinen unerwünschten Erscheinungen vermieden werden.
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 184-186 
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    Source: Wiley InterScience Backfile Collection 1832-2000
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 181-183 
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    Source: Wiley InterScience Backfile Collection 1832-2000
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    Chemie Ingenieur Technik - CIT 38 (1966), S. 186-186 
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    Source: Wiley InterScience Backfile Collection 1832-2000
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