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Linear relationships between

Linear regression models a linear relationship between two variables or vectors, x and y Thus, in two dimensions this relationship can be described by a straight line given by tJic equation y = ax + b, where a is the slope of tJie line and b is the intercept of the line on the y-axis. [Pg.446]

Multiple linear regression (MLR) models a linear relationship between a dependent variable and one or more independent variables. [Pg.481]

Here again it is possible to find a linear relationship between the log (k/feo) (ko = methyl) values of 2-alkyl- and 2,4-dialkylthiazoles and between the latter value and Tafts Eg parameter (256). The value of 5 for 2,4-dialkylthiazoles is 1.472 with a correlation coefficient of 0.9994. Thus the sensitivity to substituent effects is more marked than in the case of a single substituent in the 2-position. Furthermore, the 4-position is again more sensitive than the 2-position. [Pg.389]

Equations 10.4 and 10.5, which establish the linear relationship between absorbance and concentration, are known as the Beer-Lambert law, or more commonly, as Beer s law. Calibration curves based on Beer s law are used routinely in quantitative analysis. [Pg.386]

When possible, a quantitative analysis is best conducted using external standards. Unfortunately, matrix interferences are a frequent problem, particularly when using electrothermal atomization. Eor this reason the method of standard additions is often used. One limitation to this method of standardization, however, is the requirement that there be a linear relationship between absorbance and concentration. [Pg.420]

Shown here is a fiagram obtained for a solution of 100.0-ppm P04 . Determine h, t, T, f. At, and T. What is the sensitivity of this FIA method (assuming a linear relationship between absorbance and concentration) How many samples can be analyzed per hour ... [Pg.663]

The Fischer-Tropsch process can be considered as a one-carbon polymerization reaction of a monomer derived from CO. The polymerization affords a distribution of polymer molecular weights that foUows the Anderson-Shulz-Flory model. The distribution is described by a linear relationship between the logarithm of product yield vs carbon number. The objective of much of the development work on the FT synthesis has been to circumvent the theoretical distribution so as to increase the yields of gasoline range hydrocarbons. [Pg.164]

The Stress-Rang e Concept. The solution of the problem of the rigid system is based on the linear relationship between stress and strain. This relationship allows the superposition of the effects of many iadividual forces and moments. If the relationship between stress and strain is nonlinear, an elementary problem, such as a siagle-plane two-member system, can be solved but only with considerable difficulty. Most practical piping systems do, ia fact, have stresses that are initially ia the nonlinear range. Using linear analysis ia an apparendy nonlinear problem is justified by the stress-range concept... [Pg.64]

Using this strategy, constmction of multilayer films of - O. fim thickness by self-assembly of methyl 23-ttichlorosilyltticosanoate (MTST) on siUcon substrates has been demonstrated (Fig. 9) (165). The linear relationship between the film thickness and the layer number showed a slope of 3.5 nm /layer. Filipsometry data, absorbance intensities, and dichroic ratios for the multilayers all suggest that the samples were composed of distinct monolayers. However, ir data indicated that there maybe more tilting or disordering of the alkyl chains in the seven-layer sample than for the monolayer samples. [Pg.539]

Reduction of oxygen is one of the predominant cathodic reactions contributing to corrosion. Awareness of the importance of the role of oxygen was developed in the 1920s (19). In classical drop experiments, the corrosion of iron or steel by drops of electrolytes was shown to depend on electrochemical action between the central relatively unaerated area, which becomes anodic and suffers attack, and the peripheral aerated portion, which becomes cathodic and remains unattacked. In 1945 the linear relationship between rate of iron corrosion and oxygen pressure from 0—2.5 MPa (0—25 atm) was shown (20). [Pg.278]

With the addition of increasing amounts of electrolyte this variance decreases and an approximate linear relationship between internal and external pH exists in a 1 Af electrolyte solution. The cell-0 concentration is dependent on the internal pH, and the rate of reaction of a fiber-reactive dye is a function of cell-0 (6,16). Thus the higher the concentration of cell-0 the more rapid the reaction and the greater the number of potential dye fixation sites. [Pg.355]

A sampling of appHcations of Kamlet-Taft LSERs include the following. (/) The Solvatochromic Parameters for Activity Coefficient Estimation (SPACE) method for infinite dilution activity coefficients where improved predictions over UNIEAC for a database of 1879 critically evaluated experimental data points has been claimed (263). (2) Observation of inverse linear relationship between log 1-octanol—water partition coefficient and Hquid... [Pg.254]

The assignment of bands has been carried out using ab initio calculations, unfortunately using the erroneous Ehrlich geometry (Section 4.04.1.3.1). There is a linear relationship between the calculated energy levels (eigenvalues) and the experimental ones IEexp = 0.37 + 0.75IE<,aic, (c.c.) = 0.994. [Pg.205]

This linear relationship between stress and strain is a very handy one when calculating the response of a solid to stress, but it must be remembered that most solids are elastic only to very small strains up to about 0.001. Beyond that some break and some become plastic - and this we will discuss in later chapters. A few solids like rubber are elastic up to very much larger strains of order 4 or 5, but they cease to be linearly elastic (that is the stress is no longer proportional to the strain) after a strain of about 0.01. [Pg.32]

The next simplifieation is to assume that there is a linear relationship between a ehange in power and a ehange in valve position. This is even less aeeurate than tlie previous metliod, but ean still yield reasonable results if tlie expander typieally runs in the same operating eonditions and, for example, the bypass valve is usually elosed. However, due to the nonlinear eharaeterisities, this method ean eause signifieant over or under reaetion depending on aetual FCCU operating eonditions. [Pg.419]

The glass transition temperature of a random copolymer usually falls between those of the corresponding homopolymers since the copolymers will tend to have intermediate chain stiffness and interchain attraction. Where these are the only important factors to be considered a linear relationship between Tg and copolymer composition is both reasonable to postulate and experimentally verifiable. One form of this relationship is given by the equation... [Pg.63]

Whereas the glass transition of a copolymer is usually intermediate between those of the corresponding homopolymers this is not commonly the case with the melting points. Figure 4.12 shows the effect of copolymerising hexamethylenesebacamide with hexamethyleneterephthalamide. Only when the monomer units are isomorphous, so that the molecules can take up the same structure, is there a linear relationship between melting point and composition (as with hexamethyleneadipamide and hexamethyleneterephthalamide). [Pg.72]

The copolymers are prepared using a mixture of dimethyl terephthalate and dimethyl naphthalate. Published data indicates a reasonably linear relationship between and copolymer composition on the lines discussed in Section 4.2, e.g. Tg for a 50 50 copolymer is about 100°C which is about mid-way between Tg figures for the two homopolymers. In line with most other copolymers there is no such linearity in the crystalline melting point (T, ). As comonomer levels are introduced drops from the values for both homopolymers and indeed crystallisation only readily occurs where one of the components is dominant, i.e. 80%. Thus commercial copolymers are usually classified into two types ... [Pg.723]

From Eq. (3.44), one expects a linear relationship between Qp and Qja and a corresponding relationship for Qp and Qfjb- Indeed, this has been observed experimentally (Fig. 3.58) [3.144]. [Pg.157]

Parkyns and Quinn [20] showed a linear relationship between methane uptake at 25 C, 3.4 MPa and the Dubinin-Radushkievich micropore volume from 77 K nitrogen adsorption for porous carbons,... [Pg.287]

It is clear that a graph of ln(V j-) or In(k ) against 1/T will give straight line. This line will provide actual values for the standard enthalpy (AH ), which can be calculated from the slope of the graph and the standard entropy (AS ), which can be calculated from the intercept of the graph. These types of curves are called van t Hoff curves and their important characteristic is that they will always give a linear relationship between In(V r) and (1/T). However, it is crucial to understand that the distribution... [Pg.49]


See other pages where Linear relationships between is mentioned: [Pg.564]    [Pg.723]    [Pg.836]    [Pg.2882]    [Pg.506]    [Pg.251]    [Pg.682]    [Pg.71]    [Pg.148]    [Pg.411]    [Pg.442]    [Pg.363]    [Pg.249]    [Pg.286]    [Pg.392]    [Pg.158]    [Pg.196]    [Pg.312]    [Pg.86]    [Pg.522]    [Pg.7]    [Pg.190]    [Pg.239]    [Pg.116]    [Pg.360]    [Pg.132]    [Pg.153]    [Pg.407]    [Pg.108]    [Pg.110]   


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Linear relationship

Linear relationship between the concentrations

Linear relationship between variables

Linearized relationship

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