Ratio task

The cross-half (easy) and within-half (difficult) discriminations in a size ratio task (Spinillo Bryant, 1991). 

The task that we gave the children was to say which box was represented in the picture, and we argued that this was a genuine ratio task since the child could only solve it on the basis of the blue-white size ratio. We had eliminated other cues like shape and absolute size. 

Schematic illustrations of the effect of temperature and surface density (time) on the ratio of two isotopes, (a) shows that, generally, there is a fractionation of the two isotopes as time and temperature change the ratio of the two isotopes changes throughout the experiment and makes difficult an assessment of their precise ratio in the original sample, (b) illustrates the effect of gradually changing the temperature of the filament to keep the ratio of ion yields linear, which simplifies the task of estimating the ratio in the original sample. The best method is one in which the rate of evaporation is low enough that the ratio of the isotopes is virtually constant this ratio then relates exactly to the ratio in the original sample.

The desired air—fuel volume ratio is usually seven or more, depending on the stoichiometry. Burners of this general type with many multiple ports are common for domestic furnaces, heaters, stoves, and for industrial use. The dame stabilizing ports in such burners are often round but may be slots of various shapes to conform to the heating task. 

In the current review, the term effectiveness of air distribution will be used to describe the ratio of the occupied zone area (where thermal comfort and contaminant concentration are within ranges required by standards and codes) to the total occupied zone area. This hygienic criterion allows one to judge how well the HVAC system fulfills its main task—creating thermal comfort conditions and controlling contaminants in the occupied zone. 

Conveying systems normally use air as the transport medium to convey granular, crushed, or pulverized materials. Modelling the flow of pneumatic conveying and calculating its pressure loss is a problematic task. The greatest problem arises from the fact that different mass flow ratios, solid flow rate divided by the gas flow rate, imply different flow types in pneumatic conveying. Each of these flow types, which can be classified in many different ways, requires its own specific model in order to provide a concrete calculation method. 

A major task of chemical analysis is to determine the formulas of compounds. The formula found by the approach described here is the simplest formula, which gives the simplest whole-number ratio of the atoms present. For an ionic compound, the simplest formula is ordinarily the only one that can be written (e.g., CaCl2, Cr203). For a molecular compound, the molecular formula is a whole-number multiple of the simplest formula, where that number may be 1,2. 

Usually the dtric add outweighs the biomass by a ratio of 5 1. The initial task is to remove the mycelium from the medium, a process usually carried out by rotary filtration. The wet biomass is crushed and rewashed to obtain most of the 15% dtric add contained within and the washings are added to the spent medium. 

Practical application also requires knowledge of the weight-to-weight ratio because the amount of phosphonate needed for a special task is of economic interest. A commonly used method is the Hampshire test [307]. One to two grams of the product is solved in 100 ml of distilled water and then 10 ml of a sodium carbonate solution (2%) is added. This solution is titrated by 0.25 M solution of calcium acetate at pH 12 until permanent turbidity occurs [308], The best means for testing of commercial sequestrants is often to choose conditions of practical relevance because in practical applications a great many parameters have to be taken into account [309]. 

An important experimental task therefore remains to determine at least around the stoichiometrical composition, the variation of Kp with the composition. At high pressures the maximal yield of ammonia may occur at a hydrogen-nitrogen ratio different from three. 

Assume that we have a program we will run on np processors and that this program has a serial portion and a parallel portion. For example, the serial portion of the code might read in input and calculate certain global parameters. It does not make any difference if this work is done on one processor and the results distributed, or if each processor performs identical tasks independently this is essentially serial work. Then the time t it takes the program to run in serial on one processor is the sum of the time spent in the serial portion of the code and the time spent in the parallel portion (i.e., the portion of the code that can be parallelized) is t = tg + tp. Amdahl s law defines a parallel efficiency, Pe, of the code as the ratio of total wall clock time to run on one processor to the total wall clock time to run on np processors. We give a formulation of Amdahl s law due to Meijer [42] ... 

Yaksh TL, Rudy TA (1977) A dose ratio comparison of the interaction between morphine and cyclazocine with naloxone in rhesus monkeys on the shock titration task. Eur J Pharmacol 46(2) 83-92... 

The maximum amount of water used in constraints (9.8) and (9.9) is calculated using constraint (9.10). Constraint (9.10) defines the maximum amount of water that can be used for a task in a processing unit while still removing the required mass load and obeying the limiting inlet and outlet concentrations. The maximum amount of water is the ratio of the mass load added to the water by the task in the processing unit to the difference between the maximum inlet and outlet concentrations. 

As Levenspiel points out, the optimum size ratio is generally dependent on the form of the reaction rate expression and on the conversion task specified. For first-order kinetics (either irreversible or reversible with first-order kinetics in both directions) equal-sized reactors should be used. For orders above unity the smaller reactor should precede the larger for orders between zero and unity the larger reactor should precede the smaller. Szepe and Levenspiel (14) have presented charts showing the optimum size ratio for a cascade of two reactors as a function of the conversion level for various reaction orders. Their results indicate that the minimum in the total volume requirement is an extremely shallow one. For example, for a simple... 

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