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  • 2000-2004  (4)
  • 1955-1959  (1,648)
  • Industrial Chemistry  (1,059)
  • Chemical Engineering  (583)
  • Nuclear reactions
  • somaclonal variation
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Year
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  • 101
    Electronic Resource
    Electronic Resource
    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 209-212 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: This paper describes general methods for the treatment of binary data which are both precise and convenient. In particular a new and accurate graphical method of determining partial molal quantities is presented.
    Additional Material: 7 Ill.
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  • 102
    Electronic Resource
    Electronic Resource
    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 240-244 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The present investigation is concerned with the dynamic characteristics of a 12-in. diameter continuous agitated-tank reactor vessel. Response of the vessel effiuent temperature to a change in coolant flow rate through an internal cooling surface is the subject of theoretical and experimental study. Experimental data were obtained through the use of frequency and transient response techniques. Studies were made for the passage of vessel-charge fluids with widely differing physical properties. Also data were taken for various conditions of fluid turbulence both inside and outside the internal heat transfer coils. Experimental and theoretical results are graphically compared. Recommendations are presented for the development of theoretical dynamic relationships.
    Additional Material: 6 Ill.
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  • 103
    Electronic Resource
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 145-149 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effect of back mixing of either phase in an extraction column, which decreases the extraction efficiency, is analyzed theoretically by means of an idealized diffusion model that can be characterized by four dimensionless parameters: a Peclet number of each phase, a mass transfer number, and the usual extraction factor. Calculations for a wide range of these parameters were performed on a digital computer.The principal results, presented in a table, will be useful in the design and scale up of extraction columns and in the interpretation of experimental results from extractors and from some reactors in which a first-order reaction occurs.
    Additional Material: 7 Ill.
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  • 104
    Electronic Resource
    Electronic Resource
    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 159-160 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Based on properties which are characteristic of all gases, modifications are developed for an equation of state previously proposed in this journal (1). A specific application of the modified equation is made for the PVT data on carbon dioxide, and considerable improvement over the original equation is shown for densities in the neighborhood of 1.4 times the critical density. The new equation differs from the old equation only by the presence of the A5 and C5 terms, these having originally been taken to be zero.
    Additional Material: 1 Ill.
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  • 105
    Electronic Resource
    Electronic Resource
    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 174-177 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The free-surface model, successfully employed to predict sedimentation, resistance to flow, and viscosity in assemblages of spherical particles, has been extended to the case of flow relative to cylinders. It is shown to be in good agreement with existing data on beds of fibers of various types and flow through bundles of heat-exchanger tubes for cases where it can reasonably be expected to apply. Close agreement in the dilute range with the only theoretical treatment for flow parallel to a square array of cylinders provides interesting validation of the model.
    Additional Material: 2 Ill.
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  • 106
    Electronic Resource
    Electronic Resource
    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 276-276 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Type of Medium: Electronic Resource
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  • 107
    Electronic Resource
    Electronic Resource
    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 181-188 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Experimental studies are described concerning the fluid dynamics, particularly in the turbulent region, of dilute solutions of free-draining, nonassociating, linear polymers; sodium carboxymethylcellulose, ammonium alginate, polyisobutylene, and carboxypolymethylene, all of which are pseudoplastic. These solutions were run in laminar, transition, and turbulent flow in a pipeline flow apparatus designed to permit measurement of dynamic pressure drop and impact pressure by radial traverse.Photographic studies with dye injection used at the tube wall and at the tube center showed that turbulent flow of these pseudoplastic fluids has the following characteristics compared to Newtonian fluids: poor over-all radial mixing, thicker nonturbulent layer at the wall, and decreased rate of formation of horseshoe vortices at the wall.
    Additional Material: 13 Ill.
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  • 108
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 225-234 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An experimental technique for the determination of velocity distributions in two-dimensional laminar flow is described. The method utilizes the optical interference patterns observed in flowing doubly refracting liquids when viewed by transmitted polarized light. The fluid shear-stress distribution may be determined from these interference patterns by methods similar to those employed in solid photoelasticity. Methods are presented for the calculation of velocity distributions from the observed stress distributions. Experiments are described in which the technique was applied to determine velocity profiles in parallel-walled, converging and diverging channels and for flow about a cylindrical obstacle. The doubly-refracting liquids employed were aqueous solutions of an organic dye. Independent experimental checks were obtained in most instances, and these are in satisfactory agreement with the calculated results.
    Additional Material: 14 Ill.
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  • 109
    Electronic Resource
    Electronic Resource
    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 249-256 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The properties of vapor mixtures and liquid solutions which determine phase equilibria are of special importance in separation processes. They include the vapor-phase imperfections; the liquid-phase activity coefficents; and the excess heat, entropy, and free energy of mixing.Correlation of these properties in nonpolar mixtures is relatively simple, but in mixtures of polar and nonpolar compounds the molecular interactions lead to more complex relations. Semiempirical relations reported earlier (3, 4) have been used to calculate the vapor imperfections and to correlate the liquid-phase activity coefficients.Temperature variations of the activity coefficients can reflect the true heat and entropy effects in solution if sufficient vapor-liquid equilibria are available for a careful and consistent treatment. This is illustrated with binary mixtures of benzene and the n-aliphatic alcohols, methanol to pentanol. The results are compared with calorimetric data available in the literature.The consistent set of cross-correlated coefficients provides a basis for calculating both isothermal and isobaric vapor-liquid equilibria at various conditions for the binaries and for certain ternary and multicomponent mixtures without any additional data.
    Additional Material: 20 Ill.
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  • 110
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 273-273 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Type of Medium: Electronic Resource
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  • 111
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 8S 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Type of Medium: Electronic Resource
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  • 112
    Electronic Resource
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 295-300 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The problem of multicomponent distillation is considered for a column with an arbitrary number of feed streams and an arbitrary number of side-stream withdrawals. The overheads from the side-stream strippers are admitted to the column, introducing the inert stripping medium into the main column. Provisions are made in the calculations for complete heat balancing, inert injection, and internal reflux cooling. The method of computation is that of a previous paper involving the component-by-component technique. Calculations are made on the main column and give first approximations to the side-stream compositions; stripper calculations are then initiated. An alternating procedure is instituted between the main column and the strippers, the successive iterations continuing until a preassigned accuracy in the desired quantities is reached. An extensive numerical problem is worked.
    Additional Material: 3 Ill.
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  • 113
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 367-372 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: After an extensive literature survey the experimental thermal-conductivity data for twelve diatomic gases were utilized to produce an accurate and expedient means of predicting values over extensive ranges of temperature and pressure. Plotting values of k* against TR on logarithmic coordinates produced similarities pointing to the existence of corresponding states behavior for this family of substances with the exception of hydrogen. Because hydrogen cannot be included in a correlation generalized for the diatomic gases, it has been eliminated from this study. Based on atmospheric pressure data, ratios of k*/k*Tc produced a unique relationship with reduced temperature. To include the effect of pressure, residual thermal conductivities were correlated with density for nitrogen and oxygen, the only substances for which high-pressure data exist. These relationships enabled the determination of the thermal conductivity at the critical point. When the value kc = 8.55 × 10-5 cal./sec. cm. °K. for nitrogen was used, au extensive reduced thermal-conductivity correlation was constructed against reduced temperature for parameters of constant reduced pressure. This chart, extending to reduced pressures of 100 and to reduced temperatures of 85, is recommended for the diatomic gases in their gaseous and liquid states.The developed correlation reproduces experimental nitrogen data to within 1.39%. For the other diatomic gases experimental agreement extends from 1.00 to 3.20%. Such agreement indicates that this correlation is more reliable for the diatomic gases than are other generalized plots presented in the literature.
    Additional Material: 6 Ill.
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  • 114
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 394-396 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Fixed-bed kinetic studies were made for Fe+++  -  H+ exchange, with perchlorate as the anion, covering concentrations from 0.5 N to 2.0 N in total cation, flow rates of 5 ml./min. sq. cm. to 45 ml./min. sq. cm. bed depth of 25 to 60 cm., and average resin particle diameters of 0.28 and 0.56 mm. The results are correlated on the assumption of internal diffusion as the rate-controlling step and an essentially irreversible equilibrium.
    Additional Material: 5 Ill.
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  • 115
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 397-402 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In connection with a study of the mechanism of gas absorption the problem arose of predicting absorption rates into laminar liquid jets. A solution to the problem is presented in this paper, which provides an example of the application of fluid dynamics to the analysis of mass transfer in a complex flow system.The water jets considered here issued from circular nozzles of about 1.5-mm diameter, flowed intact downward through an atmosphere of solute gas at average velocities of from 75 to 550 cm./sec. over distances of 1 to 15 cm., and were collected in a receiver slightly larger in diameter than the nozzles. Equations describing the liquid flow near the jet surface are deduced from measurements of jet diameter and analogy to related flow situations. When one uses these equations, absorption rates are predicted from unsteady state diffusion theory with the assumption of interfacial equilibrium. The predicted rates for carbon dioxide at 25°C are in close agreement with experimental determinations over the observed range of contact time of the liquid with gas, namely 0.003 to 0.04 sec.
    Additional Material: 6 Ill.
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  • 116
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 433-435 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In pipeline design, for which one needs a means of ascertaining whether the flow will be laminar or turbulent, the Reynolds number is the criterion for Newtonian fluids. The principal purpose of this study was to formulate a more general criterion to characterize the flow regime and to test this form in application to non-Newtonian fluids.Intuitive physical arguments suggested the use of a local stability parameter which is a function of the ratio of input energy to energy dissipation for an element of fluid. If the parameter is applied to a Newtonian fluid in laminar pipe flow, one finds that it has a maximum value of 0.385 times the critical Reynolds number, or 808. As the criterion is presumed to be general, it is inferred that the value of 808 defines the boundary between stable laminar and stable turbulent pipe flow for all fluids. The inference has been varified for several pseudoplastic fluids.
    Additional Material: 6 Ill.
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  • 117
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 161-164 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The vapor-phase solubilities of carbon tetrachloride, iso-octane, toluene, and n-decane were measured in compressed hydrogen, nitrogen, and carbon dioxide at 50° and 75°C. and at various pressures between 20 and 90 atm. The virial equation of state was used to describe the volumetric properties of the vapor mixtures, and the second virial cross coefficients were evaluated from the solubility data. The results indicate that the vapor phase departs from ideality very quickly for these systems as the pressure increases, particularly at pressures greater than 10 atm.
    Additional Material: 7 Ill.
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  • 118
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 51-54 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Profiles of mean local velocities have been experimentally determined in a smooth, concentric, horizontal annulus having a radius ratio of 0.331. The test fluid was water at room temperature flowing steadily at Reynolds numbers in the viscous, transition, and lower turbulent ranges. The transitional profiles, obtained by means of an impact probe, are summarized and discussed. Limits of the transition zone are established, and variation of the radius of maximum velocity with Reynolds number is confirmed.
    Additional Material: 5 Ill.
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  • 119
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 73-75 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Laminar forced-convection heat transfer in a parallel-plate channel (flat duct) with uniform heat flux at the walls is analyzed. The velocity and temperature distributions, both uniform at the entrance section, develop simultaneously as the fluid flows through the duct. The heat transfer results, obtained for the Prandtl-number range of 0.01 to 50, include the Nusselt-number variation along the channel and the wall-temperature variation corresponding to the prescribed uniform heat flux.
    Additional Material: 8 Ill.
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  • 120
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 122-124 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 3 Ill.
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  • 121
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 10M 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 122
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 155-158 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The available experimental density data for hydrogen have been complied to produce a reduced density correlation for the liquid and gaseous states. This investigation has utilized fifty-seven sources of data, extending from the early studies of Amagat (1880) to the recent contributions of Johnston, Keller, and Friedman (1954).Based on the concept of a reduced density, a correlation for hydrogen has been developed ranging in temperature from the melting point (14°K.) to 3,300°K. and in pressure as high as 2,550 atm. This correlation provides continuity between the liquid and gaseous phases; whereas existing equations of state fail to describe the experimental behavior in the transitional region, particularly near the critical point.Four hundred and eighty-five experimental points covering the entire region were checked to establish the reliability of this correlation, which reproduced the experimental data to within 0.49%.
    Additional Material: 3 Ill.
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  • 123
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 165-168 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Transient absorption rates of oxygen into water have been measured by passing a laminar jet through the pure gas for contact times varying from 0.8 to 11.8 msec. The absorption rate is significantly lower than the theoretical value corresponding to no interfacial resistance, if a diffusivity of 2.20 × 10-5sq. cm./sec. at 22.2°C. is used for comparison. The available evidence indicates that this diffusivity is about correct and that the lowered rate may be caused by an interfacial resistance described by an interfacial transfer coefficient equal to 0.6 cm./sec. This resistance is small enough to be neglected in most gas absorbers.
    Additional Material: 6 Ill.
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  • 124
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 290-294 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In a determination of the effect of solute concentration on gas-phase mass transfer rates carbon tetrachloride was vaporized at three different concentration levels in a short 4.0-in.-diameter column packed with 0.5-in. Raschig rings.The experimental data indicate that previous mass transfer correlations should be modified to include a term (PBM/PT)2/3 and that the Schmidt number should be evaluated at average film conditions.The correlation found is suitable for predicting gas-phase mass transfer coefficients which can be combined with effective interfacial areas reported previously to obtain volumetric mass transfer coefficients for any gas-liquid-solute system.
    Additional Material: 10 Ill.
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  • 125
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 304-309 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The pyrolysis of ethane (including the equilibrium behavior and the tendency to form secondary products) has been reproduced by calculations based on a reaction mechanism which includes the reverse of the chain propagating reactions as well as other hitherto neglected elementary reactions. Reverse reactions are important even at low conversion (1%); hence previous investigations of initial reaction rate have doubtful fundamental significance. Values of rate constants used in the calculations were taken mostly from the literature. Consideration was limited to reactions of methyl, ethyl, and hydrogen free radicals with ethane and its primary pyrolysis products. The results can be incorporated into reactor performance calculations to replace empirical reaction rate correlations and thus widen the range of conditions over which the calculations are reliable.
    Additional Material: 9 Ill.
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  • 126
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    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 5 (1959), S. 325-330 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An analytical solution has been obtained for the longitudinal fully developed laminar flow between cylinders arranged in triangular or square array. Numerical results for the pressure drop and the friction factor are given over a wide range of spacing-to-diameter ratios. For large spacings the results can be represented by a single expression independent of the type of array. Plots are also given of velocity distributions and of the variation of the local shear stress around the periphery of a cylinder.
    Additional Material: 11 Ill.
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  • 127
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    AIChE Journal 5 (1959), S. 348-353 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Initiation of the oxidation of hydrocarbons, an important part of many flame systems' remains largely unsolved. This paper reports a study of the oxidation of butane under conditions that yield information on the homogeneous initiation reactions.A sequential reaction mechanism is proposed involving activation of an oxygen molecule followed by attack on a butane. This leads to rate equations which accurately describe the observed butane decomposition rates. Activation energies have been calculated from experimental data with this equation and are found to check values obtained from the literature and from theoretical considerations.The tentative initiation mechanism is used to explain the existence of three classes of products in the exit gases: hydrocarbons other than butene, butene, and oxygenated products.Under some operating conditions periodic cool flame phenomena are observed, and their effect on the course of the reaction has been explained.
    Additional Material: 9 Ill.
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  • 128
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    AIChE Journal 5 (1959), S. 373-378 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Mathematical relationships based on material balance and rate equations have been derived for the study of ion exchange kinetics in a fixed-bed operation. Numerical techniques for the solution of the systems possessing equilibrium relationships of the Freundlich-adsorption isotherm type have been developed, and numerical results have been obtained with the use of a digital computer. The resulting numerical solutions have been found to be dependent on parameters involving time, position, and the relative resistances of the liquid and resion phases. The numerical solutions are presented in both tabular and graphical forms.
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  • 129
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    AIChE Journal 5 (1959), S. 384-390 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: It is shown in a series of illustrative examples how the conversion efficiency of many reactions can be markedly affected by the type of reactor used, even though the temperatures, catalyst, and basic kinetics are already fixed by the chemistry of the process.For such purpose graphical and analytic criteria are developed which permit the selection of a continuous stirred tank or tubular reactor system to obtain the most advantageous conversion of raw material to desired product. When a continuous stirred tank reactor process is preferable, the optimum number of reactor stages for maximum conversion is one. An example is given of a case where a combination of a continuous stirred tank and a tubular reactor is advantageous.A new graphical method of reactor design for simple or complex reactions is also introduced. This method utilizes continuous stirred tank reactor data directly rather than batch data or kinetics analyses.Reactions are classified according to the kinetic and stoichiometric characteristics which determine the allowable design procedures and the differences in the compostions paths occurring in batch, tubular, or continuous stirred tank reactors.The mathematical analysis of continuous stirred tank reactor systems for complex reactions leads to a set of difference equations. For cases of zero- or first-order reactions these are readily solved as illustrated in examples, even when several independent components influence the reaction kinetics.
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  • 130
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    AIChE Journal 5 (1959), S. 407-409 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 6 Ill.
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  • 131
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    AIChE Journal 5 (1959), S. 319-324 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The formation of air bubbles at constant pressure at submerged orifices was investigated for several liquids. The frequency of formation of the bubbles was determined by the use of a stroboscope, and the rate of gas flow was measured with conventional rotameters. Several orifices having diameters ranging from 0.0794 to 0.397 cm. were employed, and the gas flow rate was varied from about 0.1 cc. (at standard conditions)/sec. to about 150 cc./sec. It was found that the formation of bubbles could be correlated with the physical variables of the system by the application of Newton's second law of motion to the bubble at the instant just prior to its release from the orifice.
    Additional Material: 9 Ill.
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  • 132
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    AIChE Journal 5 (1959), S. 339-344 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Transformation are obtained which reduce the system of differential equations for certain types of diffusion-controlled reactions to the equation for pure diffusion.Simple relationships between the diffusion rate with and without reactions are presented for reversible unimolecular reactions, certain types of reversible bimolecular reactions, and irreversible reactions between species with equal diffusivities. It is shown that these relationships are independent of geometry, hydrodynamics, or boundary conditions, and so the mass transfer coefficient in the presence of reactions can be obtained from the coefficient in the absence of reactions without an explicit knowledge of the mass transfer mechanism.The reaction factor for irreversible reactions with equal diffusivities, obtained by others for specific mass transfer mechanisms, is found to be quite general and essentially independent of the mechanism.Some data on the absorption of sulfur dioxide in a laminar water jet is considered.
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  • 133
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    AIChE Journal 5 (1959), S. 506-509 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: After application of a biochemical technique, size distribution of liquid drops from air bubbles blown through water and a butanol and glycerine solution filled to a certain depth in a glass cylinder 9.6 cm. in diameter and 47 cm. in length was measured.The initial vertical velocity of drops was estimated from the experimental results, with reference to its trajectory.
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  • 134
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    AIChE Journal 5 (1959), S. 524-532 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: This paper illustrates the use of analytical methods for the design of a flow-control system. Linearized equations are derived and a complete analysis is made of the control of the system. The effect of controller modes and process time constants is investigated. The calculations show that there is an optimum value of the process time constant for optimum response.
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  • 135
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    AIChE Journal 5 (1959), S. 7S 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 136
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    AIChE Journal 5 (1959), S. 564-564 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 1 Ill.
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  • 137
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    AIChE Journal 5 (1959), S. 453-457 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A differential type of flow reactor, 0.25-in. I.D., was used to study the kinetics of the hydrogenation of ethylene on an alumina-supported nickel catalyst. This is apparently the first investigation made above atmospheric pressures. Data were obtained from 14.7 to 70 1b./sq. in. abs. and feed compositions from 40 to 90 mole % hydrogen. Measurements at temperatures from 30° to 80°C. indicated an apparent activation energy of 11,600 cal./g.-mole.It was found that the activity of the catalytic surface was reduced by exposure to ethylene, or mixtures containing an excess of ethylene, owing to the formation of acetylene residues. Pretreatment of the catalyst at temperatures of 170°C. with mixtures of ethylene and hydrogen stabilized the catalyst so that reliable rate data could be obtained.The rate measurements at 70°C. were correlated by an equation. While the mechanism of the reaction cannot be determined from the data, the rate expression and other kinetic studies suggest a process in which hydrogen is adsorbed on the small fraction of the surface not occupied by acetylenic residues and the reaction takes place between this adsorbed hydrogen and ethylene in the gas phase.
    Additional Material: 7 Ill.
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  • 138
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    AIChE Journal 5 (1959), S. 474-482 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Relationships are developed for establishing the most economic values of the major variables of a liquid-extraction process, including the concentrations of solute in recycled solvent and rejected raffinate, the solvent-to-feed ratio, and for mixer-settlers certain of the design features. Consideration is given to costs of extraction and solvent recovery, as well as to the value of unextracted solute and lost solvent. For the design of mixer settlers scale-up relationships are developed to permit prediction of the stage efficiency of a large extractor from experimental data taken on a small scale. These are expressed in terms of a scale-up index relating the relative size of the mixer with the volumetric rates of liquid flow. It is shown that the cost of multistage extractor increases with scale up in a different fashion from the stage efficiency, depending upon the scale-up index used. A detailed study of the costs for a typical case led to the development of economic scale-up indexes which, because they cover nearly a fivefold ratio of fixed to operating costs, are of fairly general utility. The common practice of scaling up with equal holding times on the large and small scale is shown to be amply safe from the point of view of stage efficiency to be realized on the large scale but usually uneconomic.Simplification of the complete system of equations permits rapid estimation of the most economic circumstances for any type of countercurrent extractor of which the cost per stage is proportional to Qg.
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  • 139
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    AIChE Journal 5 (1959), S. 496-501 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The vapor-phase reaction between ethylene oxide and water to form glycols has been carried out under a wide range of conditions with particles of polystyrene-sulfonic acid ion exchange resins used as catalysts. The rates observed appeared to be directly proportional to the product of the partial pressure of ethylene oxide and the amount of water sorbed by the resin. By use of the Brunauer, Emmett, and Teller equation to describe the amount of water sorbed by the resin, the experimental data were correlated over a sixty-fold range of reaction rates with a mean deviation of 15%.To obtain data of value in elucidating reaction mechanisms, the reactor was usually run under “differential” conditions, that is low conversions. However in a few runs conversions of as high as 54% were obtained for a contact time of 0.02 sec. The ratio of ethylene glycol to higher glycols (selectivity) obtained varied between 73 and 99% but was usually above 80% under conditions of high conversion. However it could also be reduced forcibly to produce higher glycols as the major product, if desired.
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  • 140
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    AIChE Journal 5 (1959), S. 514-523 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The origin of interfacial turbulence, spontaneous agitation of the interface between two unequilibrated liquids, has been explained in terms of classical flow, diffusion, and surface processes. The essence of the explanation is the long-known though much neglected Marangoni effect, wherein movement in an interface is caused by longitudinal variations of interfacial tension. It is proposed that interfacial turbulence is a manifestation of hydrodynamic instability, which is touched off by ever present, small, random fluctuations about the interface.A simplified mathematical model has been analyzed in order to detail the mechanism of the “interfacial engine” which supplies the mechanical energy of interfacial turbulence. In its present form the analysis incorporates several drastic simplifications, though ways of removing some of these have been suggested. The groundwork has been laid for the more elaborate analyses that are needed for a decisive test of the theory.The analysis shows how some systems may be stable with solute transfer in one direction yet unstable with transfer in the opposite direction, a striking result. It also suggests that interfacial turbulence is usually promoted by (1) solute transfer out of the phase of higher viscosity, (2) solute transfer out of the phase in which its diffusivity is lower, (3) large differences in kinematic viscosity and solute diffusivity between the two phases, (4) steep concentration gradients near the interface, (5) interfacial tension highly sensitive to solute concentration, (6) low viscosities and diffusivities in both phases, (7) absence of surface-active agents, and (8) interfaces of large extent.That some of these effects have been observed in the laboratory lends credence to the theory.
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  • 141
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    Chemie Ingenieur Technik - CIT 31 (1959) 
    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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  • 142
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 18-20 
    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 einer thermischen Spaltanlage wird aus methan-haltigem Koksofengas Synthesegas erzeugt. Hierbei fällt Ruß an. Aus dem wasserdamfhaltigen Spaltgas wird er mit Schlauchfiltern abgeschiden. Das Gas is dadurch maschinenrein, der Ruß wird in verkaufsfähiger Form gewonnen. Über Betriebsversuche Gas ist dadurch maschinenrein, der Ruß wird in verkaufsfähiger Form gewonnen. Über Betriebsversuche Gas ist dadurch maschinenrein, der Ruß wird in verkaufsfähiger Form gewonnen. über Betriebsversuche mit verschiedenen Filtersystemen wird berichtet.
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  • 143
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 1-11 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Reaktionstechnische Berechungen gewinnen eine immer größere Bedeutung für die Praxis. Die Schwierigkeiten, die dabei auftreten, Können bei der Beschaffung der Ausgangsdaten, beim mathematischen Ansatz oder bei der numerischen Rechnung liegen. Die modernen elektronischen Rechenmaschinen ermöglichen es heute, sehr umfangreiche und komplizierte Berechnungen in kurzer Zeit auzuführen, so daß der große Umfang mancher reaktionstechnischer Berechnungen kein Hindernis mehr darstellt. Die Genauigkeit der Ausgangsdaten und die Gültigkeitsgrenzen des mathematischen Ansatzes müssen aber bei jedem speziellen Problem sorgfältig diskutiert werden. An Hand von Beispielen für thermodynamische und kinetische Berechnungen und der Berechnung eines optimalen Reaktionsapparates werden diese Geischtspunkte diskutiert.
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  • 144
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 12-17 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Es gibt - über die ganze Welt verteilt - nur etwa zehntausend lngenieure und Physiker, die sich mit der Erforschung extrem schneller Vorgänge befassen. Alle Zwei Jahre versammeln sich einige Hundert von ihnen, um in einer internationalen Tagung neue Fors chungsergebnisse, auf apparativem Gebiet wie auch auf dem Sektor der Anwenungen, auszutauschen. Die IV. Tagung dieser Art, die vom 22. bis 26. September 1958 in Köln stattfand, war deshalb besonders interessant, weil zum ersten Mal Forscher ausder Sowjetunion, wo die Kurzzeitphotographie im Zusammenhang mit der Entwicklung von Raketen, nuklearen Waffen und Fusionsreaktoren beträchtlich vorangetrieben wurde, ihre neuen Geräte vorstellten und die westlichen Kollegen mit den von ihnen erzielten Leistungen überraschten.
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  • 145
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 20-21 
    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 Kreislaufmahlung und der später entwickelten Umlaufhomogenisierung wird dem Zerkleinerungs- bzw. Mischvorgang ein Trennvorgang nachgeschaltet, wodurch eine Energieersparnis erreicht wird.
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  • 146
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 22-30 
    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 in einer früheren Arbeit angestellten Optimalbetrachtungen über die Anreicherung von schwerem Wasser in Heiß-Kalt-Kolonnen werden auf eine aus mehreren Heiß-Kalt-Kolonnenpaaren bestehende Trennkaskade ausgedehnt. Außerdem werden die mit der Erhöhung der Deuterium-Ausbeute durch ein als Abstreifsystem wirkendes HeißKalt-Kolonnenpaar und die mit dem Einsatz einer Übertragungskolonne zusammenhängenden Fragen diskutiert.
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  • 147
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    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Es wird das in der industriellen Anlage des Commissariat francais pour I'Energie Atomique in Marcoule angewandte Verfahren zur Abtrennung des Plutoniums aus den bestrahlten Uran-Brennstoffelementen sowie die Reinigung des Urans und Plutoniums und die Konzentrierung der Spaltprodukte beschrieben.
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  • 148
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 33-35 
    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 Schwächung von β-Strahlen ist abhängig vom Flächengewicht und vom Verhältnis Ordnungszahl Z/Atomgewicht A des durchstrahlten Mediums. Dies ermöglicht die Messung des Flächengewichts bei konstantem Z/A-Verhältnis, bzw. des Z/A-Verhältnisses bei konstantem Flächengewicht. Die zweite Möglichkeit ist die Grundlage der C/H-Messung in aromatischen Kohlenwasserstoffen; dabei wird der Strahler fest mit einem Schwimmer verbunden, dessen Auftrieb in Abhängigkeit von der Dichte des flüssigen Mediums automatisch ein konstantes Flächengewicht über dem Strahler herstellt, so daß das Meßergebnis nur vom C/H-Verhältnis abhängig ist. In flüssigen Kohlenwasserstoffen wird auf diese Weise ein kontinuierlich arbeitender Nachweis des Wasserstoff-Gewichtanteils auf ± 0,16% erreicht.
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  • 149
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 36-43 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Schwere Blechpackungen, Trommeln und Fässer, werden in Deutschland vorwiegend von der chemischen Industrie als Verpackungsmittel für ihre mannigfachen Erzeugnisse verwendet. Der Oberflächenschutz dieser Behälter, die im Inlandverkehr vielfach als Leihgebinde laufen, ist für die Wirtschaft ein ernstes Problem, da jährlich eine beträchtliche Zahl von Behältern durch Korrosion unbrauchbar wird, und infolgedessen immer wieder erhebliche Beträge für die Neubeschaffung aufgewendet werden müssen. Im folgendessen immer wieder erhebliche Beträge für die Maßnahmen besprochen, mit denen man einen möglichst befriedigenden Oberflächenschutz dieser Gebinde erreichen kann; dabei wird auf neuere Entwicklungen in den USA besonders eingegangen.
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  • 150
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 54-58 
    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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  • 151
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 59-62 
    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: 8 Ill.
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  • 152
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 50-54 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Einige von Tigerschiöld und Rumpf angegebene Formeln für die Festigkeit von Pellets auf Grund von Kapillarkräften oder Salzbrücken werden an Preßlingen aus Tonerde nachgeprüft. Die Festigkeit ergibt sich als proportional zur Oberflächenspannug der Pelletisierungsflüssigkeit und umgekehrt proportional zur Korngröße, übereinstimmend mit der Theorie. Salzablagerungen findet man bevorzugt an der Oberfläche der Pellets, weil dort die Verdunstung am stärksten ist.
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  • 153
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 43-49 
    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 Wirksamkeit elektrischer Entstaubungsanlagen wird durch das Rücksprühen (Rückionisation) bei der Abscheidung von Stäben mit extrem hohem elektrischem Widerstand herabgesetzt. Das Rücksprühen an Schichten elektrisch niedergeschlagenen Staubes bei 150 °C an Eisensulfat, Eisenoxyd, Zinkoxyd, Steinkohle, Braunkohle, Zement, Magnesiumoxyd und Flugasche wurde untersucht. Nach den Ergebnissen wird die Rückionisation durch hohen Staubwiderstand, hohe Stromdichte und geringe Schichtdicke des niedergeschlagenen Staubes begünstigt. Besonders kräftiges Rücksprühen ist z. B. an Schichten von etwa 0,2 mm Dicke von Stäuben, deren spezifischer Widerstand größer als 2 · 1012 Ohm cm ist, zu beobachten.
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  • 154
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 62-62 
    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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  • 155
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 65-66 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 156
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 63-64 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 157
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 67-67 
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    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 158
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 68-72 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 159
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    Chemie Ingenieur Technik - CIT 31 (1959) 
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    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 160
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 80-80 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Von der Süddeutsche Kalkstickstoff-Werke AG, Trostberg, wurde in Zusammenarbeit mit der Maschinenfabrik Fellner & Ziegler, Frankfurt, eine Anlage zur kontinuierlichen Herstellung von Kalkstickstoff errichtet. Nach der dabei angewandten neuen Arbeitsweise wird aus fein gemahlenem Carbid im Gleichstromverfahren pulverförmiger Kalkstickstoff bei erheblich verbesserten Ausbeuten und Verbauchszahlen erzeugt.Das neue Verfahren wurde in den Versuchsbetrieben der Südd. Kalkstickstoff-Werke AG, Trostberg, in Zusammenarbeit mit den Herren Dipl.-Ing. Fischer, Dr.-Ing. Kronacher und Ing. Schücker entwickelt.
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  • 161
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 73-79 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Es wird ein Überblick über die Eigenschaften der Radial-, Axial- und Wirbelkonvektion in Gaszentrifugenrotoren gegeben, und es wird geschildert, wie die zunehmende Erkenntnis dieser Strömungsarten im Laufe der Zeit die Methodik der Gaszentrifugierung beeinflußt hat. Über einen Vorläfer der heutigen Gegenstromzentrifuge wird erstmals berichtet, desgleichen über Ergebnisse und Verlauf der Forschungsvorhaben des Instituts auf dem Gebiet der Gaszentrifugierung.
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  • 162
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    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Es werden Unterlagen für eine wirtschaftlich günstige Ausführung eines Sumpfphasereaktors zusammengestellt. Bei heterogenen Sumpfphasereaktionen müssen sehr verschiedene Maßnahmen zur Verbesserung des Umsatzes ergriffen werden, je nachdem ob der Hauptreaktionswiderstand bei Diffusionsvorgängen oder bei der eigentlichen chemischen Reaktion liegt. Um die optimalen Reaktionsbedingungen möglichst schnell auffinden zu können, muß man zunächst den geschwindigkeitsbestimmenden Teilschritt der Gesamtumsetzung durch geeignete Versuche ermitteln. Ein entscheidendes Charakteristikum zur Aufklärung ist einerseits die Temperatur- und andererseits die Druck- bzw. Konzentrationsabhängigkeit der Umsetzungsgeschwindigkeit. Die bei Gasphasereaktionen entwickelte Theorie heterogener Reaktionen läßt sich nutzbringend auch auf Reaktionen in flüssiger Phase anwenden.
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  • 163
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    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Es wird eine Anlage beschrieben, die es gestattet, die Trocknungsgeschwindigkeit als Funktion des mittleren Feuchtigkeitsgehaltes der Probe selbsttätig aufzuschreiben. Zur Ermittlung des Feuchtigkeitsgehaltes und der Trocknungsgeschwindigkeit wird die Gewichtsabnahme beim Trocknen durch Verdrängung einer Flüssigkeitsmenge gleichen Gewichts laufend kompensiert. Mit Hilfe eines mechanisch-elektrischen Differenzenverfahrens wird die Gewichtsabnahme pro Zeiteinheit, d. h. also die Trocknungsgeschwindigkeit, bestimmt und auf einem Schreiber registriert. Der Papiervorschub des Schreibers wird nicht von der Zeit, sondern von der Gewichtsabnahme der Probe und damit nach Einführen entsprechender Umrechnungsfaktoren vom mittleren Feuchtigkeitsgehalt gesteuert. Für die Registrierung wurde ein Kompensationsschreiber mit zwölf Meßstellen benutzt, der außer der Trocknungsgeschwindigkeit noch andere bei der Trocknung interessierende Größen registriert.
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  • 164
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 101-105 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Luftgekühlte Wärmeaustauscher werden in der chemischen Industrie nunmehr auch bei der Kondensation von chlorierten Produkten und bei Substanzen mit niedrigem Siedepunkt verwendet. Auch Vakuumdestillationsanlagen bis zu 2 Torr wurden mit luftgekühlten Wärmeaustauschern ausgerüstet, wobei niedriger Druckverlust wichtig ist. Neue konstruktive Lösungen erzielte man mit der Anordnung der Luftkondensatoren auf den Kolonnenköpfen und mit der Kombination eines Kondensators mit einem Kühler.
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  • 165
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 105-108 
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Es wird eine ausgeführte Siloanlage für Kunststoffpulver beschrieben, deren Gestaltung sich aus folgender Aufgabenstellung ergab: In mehreren Fabrikationsanlagen werden verschiedene Polymerisate erzeugt. Diese sollen zu einem zentralen Silogebäude gefördert werden, dort zu großen Einheiten zusammengefaßt, in Säcke oder Kesselwagen oder Kesselwagen abgefüllt und versandt werden.
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  • 166
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Mit Hilfe der Dimensionsanalyse wird eine im Reaktionsrohr ablaufende festkatalysierte Gasphasereaktion in bezug auf die Rohrweite und auf die Rohrlänge untersucht. Die Ergebnisse zeigen, daß es für eine gegebene Reaktion eine optimale Rohrweite gibt, die sich mit der Reynoldsschen Zahl ändert. Ebenso wird die Rohrlänge von der Reynoldsschen Zahl bestimmt. Durch Einführung der Halbwertslänge und eines Umsatzkoeffizienten wird die Extrapolation von kleinen Rohrlängen auf große möglich.
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  • 167
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 118-123 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 168
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 123-126 
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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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  • 169
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    Source: Wiley InterScience Backfile Collection 1832-2000
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    Notes: Nachdem in Teil I die pH-Messung in stark sauren und alkalischen Lösungen und in Teil II die bei hohen Temperaturen und Drucken sowie bei tiefen Temperaturen diskutiert wurde, soll nun im abschließenden Teil III die pH-Messung in nichtwäßrigen und wasserarmen Medien erörtert werden.
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  • 170
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 126-126 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 171
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 126-128 
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    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 172
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 129-130 
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    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 173
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    Chemie Ingenieur Technik - CIT 31 (1959) 
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    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 174
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 130-132 
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    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 175
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 133-138 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Es werden Aufgabenstellung und Eigenarten der Dekontaminierungstechnik sowie die wichtigsten Dekontaminierungsverfahren - mechanische Abtrennung, chemische Fällung, Verdampfung und lonenaustausch - besprochen.
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  • 176
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 139-145 
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    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In den letzten Jahren hat sich der Anwendungsbereich für radioaktive Stoffe in der Chemie und Technik stark erweitert. Es werden einige Beispiele beschrieben, wie die Messung von Strömungsgeschwindigkeiten in Rohren, die Markierung von Grenzzonen zwischen verschiedenen Chargen, die Bestimmung von Mischungsvorgängen sowie von Durchlaufzeiten, Volumen und Durchsatz bei technischen Prozessen.
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  • 177
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 145-148 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abluft aus Einrichtungen, die zu Emissions-Zentren radioaktiver Stäube werden können, muß mit größter Sorgfalt gereinigt werden. Die Vorschriften über die Prüfung von Luftfiltern für diese Zwecke beziehen sich auf Teststäube mit Teilchen-Durchmessern in der Größenordnung von 0,1 μ. Dies ist durch den Abscheide-Mechanismus der technisch verwendbaren Filter bedingt. Es werden Beispiele für Filter-Anlagen zur Abscheidung radioaktiver Stäube gebracht.
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  • 178
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 148-153 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Trotz der großen praktischen Bedeutung wurde bisher noch kaum versucht, Wärme- und Stoffaustausch zwischen zwei fluiden Phasen zusammenfassend darzustellen. Es zeigt sich jedoch, daß mit drei in vielen Fällen zulässigen Voraussetzungen das Problem sich soweit vereinfachen läßt, daß es sich in einer Ebene abbilden läßt. Es werden Diagramme angegeben, aus denen die stationäre Aufstiegsgeschwindigkeit von Gasblase und für den laminaren Bereich auch die äußeren Wärme- und Stoffübergangszahlen abzugreifen sind. Auch wird eine Gleichung angegeben, die wenigstens als Anhalt für die Berechnung der äußeren Wärmeübergangszahl im turbulenten Gebiet dienen kann.
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  • 179
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    Source: Wiley InterScience Backfile Collection 1832-2000
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    Notes: Die Stoffübergangszahl zwischen Dampfblase und Flüssigkeit wurde an vier Flüssigkeitsgemischen in beiden Austauschrichtungen gemessen. In Übereinstimmung mit früheren Messungen von A. Frank an Stickstoff/Sauerstoff-Mischungen zeigte sich in allen Fällen eine höhere Stoffübergangszahl in derjenigen Richtung, in der die Oberflächenspannung durch den Stoffaustausch erhöht wird.
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  • 180
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 155-163 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Die bei den verschiedenen Verfahren benutzten Schaltungen und Anordnungen der Druckdestillation von Ammoniak-Wasser werden beschrieben; dabei wird auch die Frage behandelt, ob für die Beheizung der Kolonne unmittelbare Dampfeinblasung in den Kolonnensumpf oder ein besonderer Wärmeaustauscher zweckmäßiger ist. Zur Berechnung derartiger Ammoniak-Kolonnen, insbesondere zur Bestimmung der Rücklaufwärme und der theoretischen Bodenzahl von Abtriebs- und Verstärkungssäule, läßt sich mit Vorteil das bekannte i,ζ-Diagramm von Merkel und Bosnjakovic verwenden.
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  • 181
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 174-175 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Der Bericht beruht auf den Eindrücken, die während eines 20monatigen Aufenthaltes in den USA gewonnen wurden. Der Autor arbeitete dort an der Brown University in Providence an wärmetechnischen Forschungsaufgaben. Darüber hinaus hatte er Gelegenheit, andere Universitäten und Forschungsstätten aufzusuchen.
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  • 182
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    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Untersucht wurde der Wärmeübergang an Wasser in Rohren mit künstlich aufgerauhten Innenoberflächen. Durch solche kleinen periodisch angebrachten Rauhigkeiten läßt sich der Wärmeübergang wesentlich erhöhen, während der Druckverlust weniger ansteigt.
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  • 183
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    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Der Zusammenhang zwischen dem Wärmeübergang und der Bewegung der Feststoffteilchen wird für das Fließbett und das Moving Bed untersucht. Für den Mechanismus des Wärmeüberganges im Fließbett ergibt sich: Die Kontaktzeit der Feststoffteilchen an einer wärmeaustauschenden Fläche bestimmt den Wärmeübergang; er steigt mit abnehmender Kontaktzeit an und strebt gegen einen Optimalwert. Dieser ist durch das Vorhandensein einer Gasschicht zwischen der Austauschfläche und den körnigen Feststoffteilchen bedingt. Entgegen einer oft vertretenen Ansicht ist die Gasgeschwindigkeit ohne direkten Einfluß auf den Wärmeübergang. Weiter wird über Versuche berichtet, bei denen bisher wenig untersuchte Einflußgrößen in Fließbetten, wie z. B. der Gasdruck und die Gasverteilung sowie die Feststoffzirkulation, verändert wurden.
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  • 184
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    Source: Wiley InterScience Backfile Collection 1832-2000
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    Notes: Es wird an einigen Beispielen gezeigt, daß Normen eine große Hilfe bei der Planung verfahrenstechnischer Anlagen sind.
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  • 185
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 183-191 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Nach Definition der Kenngrößen für die Teilchengröße und Teilchenform werden die verschiedenen Meßverfahren zu ihrer Bestimmung und zur Erfassung der Korngrößen-Verteilungsfunktion kritisch miteinander verglichen und ihre Möglichkeiten und Grenzen aufgezeigt, so daß sich für ein bestimmtes Problem die geeignetste Methode auswählen läßt.
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  • 186
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 192-194 
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    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Es wird eine neue Formel für das Trockenmischen pulverisierter Materialien beschrieben, die offenbar die meisten Einflüsse berücksichtigt, die einen Mischvorgang bestimmen und die bisher nicht zufriedenstellend erfaßt wurden. Die Gleichung läßt sich ganz allgemein auf Mischvorgänge und vermutlich auch auf Trennvorgänge anwenden.
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  • 187
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 195-201 
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    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Zunächst werden möglichst anschaulich die Grundgleichungen der Plastizitätstheorie dargestellt und dann die Definition des Grenzverhaltens gegeben. Darauf wird gezeigt, wie mit Hilfe des Grenzverhaltens obere und untere Grenzen für die äußere Belastung ermittelt werden können. Nach einfachen Anwendungsbeispielen werden die Gleichungen für den rotationssymmetrischen Körper aufgestellt und auf den Fall der Kreisplatte angewendet.
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  • 188
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 213-218 
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    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 189
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    Notes: Es wird eine hydrodynamische Dichtung für rotierende Wellen beschrieben, die mit ganz geringen Leckverlusten von unter 5 g im Jahr arbeitet. Die Dichtung besteht im wesentlichen aus einem Gewindeteil, das innerhalb einer Buchse umläuft und das mittels des Gewindes Sperrflüssigkeit entgegen dem Druck im Innern der Dichtung fördert. Diese Dichtung wird als Viskodichtung bezeichnet. Es gelingt, durch besondere konstruktive Maßnahmen auch bei stillstehender Welle vollständige Dichtheit zu erreichen. Die Dichtung verdient Interesse, z. B. bei der Verwendung giftiger Gase in der chemischen Industrie. Es werden zunächst die möglichen Bauarten mit Einzelgewinde oder gegenläufigem Gewinde beschrieben und dann die Gleichungen für den Sperrdruck und den Leistungsbedarf abgeleitet. Danach wird ein Beispiel einer solchen Dichtung für den Fall einer technischen Anwendung in einem Atomreaktor durchgerechnet. Sodann wird der Einfluß der Eigenschaften auf die Bauweise geschildert und abschließend die Darstellung von Versuchsergebnissen mit dimensionslosen Kennzahlen für die Dichtung erörtert.
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 225-226 
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    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 218-224 
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    Source: Wiley InterScience Backfile Collection 1832-2000
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    Additional Material: 22 Ill.
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 226-226 
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 227-228 
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    Source: Wiley InterScience Backfile Collection 1832-2000
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 228-228 
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 229-230 
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 228-228 
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 230-233 
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    Chemie Ingenieur Technik - CIT 31 (1959), S. 234-236 
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    Type of Medium: Electronic Resource
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  • 200
    ISSN: 0009-286X
    Keywords: Chemistry ; Industrial Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Es wird eine Übersicht über alle Bauarten und die wichtigsten Daten für Baugröße, Drehzahl und Betriebsverhalten der einstufigen Ausführungen gegeben. Insbesondere werden die grundlegenden Gesetzmäßigkeiten behandelt und die charakteristischen Eigenschaften der axialen und radialen Ausführungen einander gegenübergestellt.
    Additional Material: 14 Ill.
    Type of Medium: Electronic Resource
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