Second Order Effects in Non-Newtonian Lubrication Theory. A General Perturbation Approach

1982 ◽  
Vol 104 (2) ◽  
pp. 234-242 ◽  
Author(s):  
Patrick Bourgin

This paper is a theoretical investigation into the problem of the isothermal laminar flow of a Rivlin-Ericksen fluid of complexity n between arbitrary two bidimensional surfaces separated by a small gap. Nonlinear viscosity effects and normal-stress effects have both been taken into account. It had been recently proved that the use of a method of resolution similar to that of Reynolds imposes to reduce the field of rheological models; a “generalized Reynolds equation,” available for Stokesian fluids was then derived. Returning now to the most general differential fluid, an analytic approximate solution has been searched under the form of perturbation expansions for the normal stress and velocity fields, respectively. The corresponding set of differential equations has been given. An example has been worked out in order to compare our approximate solution with an exact solution which exists in the considered particular case. At that occasion, a discussion is opened about the choice of adequate boundary conditions at the ends of the lubricant film.

2018 ◽  
Vol 30 (1) ◽  
pp. 013103
Author(s):  
Byung Chan Eu

1951 ◽  
Vol 18 (2) ◽  
pp. 163-172
Author(s):  
H. D. Conway ◽  
L. Chow ◽  
G. W. Morgan

Abstract This paper presents a method of analyzing the stress distribution in a deep beam of finite length by superimposing two stress functions. The first stress function is chosen in the form of a trigonometric series which satisfies all but one of the boundary conditions—that of zero normal stress on the ends of the beam. The principle of least work is then used to obtain a second stress function giving the distribution of normal stress on the ends which is left by the first stress function. By superimposing the two solutions, all the boundary conditions are satisfied. Two particular cases of a given type of loading are solved in this way to investigate the stresses in a deep beam and their deviation from the ordinary beam theory. In addition, an approximate solution by the numerical method of finite difference is worked out for one of the two cases. Results from the two methods are compared and discussed. A method of obtaining an exact solution to the problem is given in an Appendix.


Wear ◽  
1987 ◽  
Vol 116 (2) ◽  
pp. 237-248 ◽  
Author(s):  
N.M. Bujurke ◽  
M. Jagadeeswar ◽  
P.S. Hiremath

2017 ◽  
Vol 92 ◽  
pp. 84-91 ◽  
Author(s):  
Wei-Tao Wu ◽  
Nadine Aubry ◽  
James F. Antaki ◽  
Mehrdad Massoudi

1969 ◽  
Vol 36 (3) ◽  
pp. 634-635 ◽  
Author(s):  
R. I. Tanner

The calculation of increased bearing capacity due to large viscoelastic or normal stress effects is carried out exactly for plane slider bearings with a second-order fluid lubricant.


CORROSION ◽  
1969 ◽  
Vol 25 (8) ◽  
pp. 345-349 ◽  
Author(s):  
F. H. COCKS ◽  
J. F. RUSSO ◽  
S. B. BRUMMER

Abstract The stress corrosion behavior of an Al-Zn-Mg-Cu alloy (7075) has been investigated. Under certain conditions of surface preparation, corrosion alone is found to cause a major diminution in subsequent stress corrosion life. For example, in 7075 in the T651 temper with an as-machined surface finish, the deleterious effect of corrosion is independent of the application of load during the first 80% of its normal stress corrosion life. Only during the last 20% of the normal stress corrosion period is it necessary to apply a load. It is during this latter period that true stress corrosion, as normally defined, can be said to occur. These observations do not result from residual tensile stresses in the material; rather, they are shown to be due to disruption of the grain boundary structure at the surface by machining. The beneficial effects of shot peening and other mechanical surface treatments probably also derive from similar distortions.


2014 ◽  
Vol 6 ◽  
pp. 179394 ◽  
Author(s):  
Na Xu ◽  
Jinjia Wei

The time-dependent shear-induced nonlinear viscosity effects of dilute surfactant solutions (CTAC/NaSal) at constant shear rate were tested by using the rheometer Couette cell. The apparent viscosity evolution curve can be divided into five stages: weak shear-thickening (Stage I), weak shear-thinning and plateau (Stage II), sharp shear-thickening (Stage III), oscillating adjustment (Stage IV), and rough plateau (Stage V). In Stage I, the stretching effects of shear flow lead to the weak increase in apparent viscosity at the inception of shearing. The apparent viscosity curve firstly decreases in Stage II and then levels off. The apparent viscosity plateau is caused by the forming and slipping of micellar lumps at the inner cylinder wall surface. Once the volume of lump exceeds a certain degree, the nucleation process of forming SIS is triggered, which is the beginning of Stage III and then the apparent viscosity increases sharply. The variations of apparent viscosity in adjusting period are rather complicated in Stage IV, and the variations mainly depend on the situation of SISs network. In Stage V, coupled with obvious oscillations, the apparent viscosity maintains a basically constant plateau value, indicating that the SISs network is fully developed and saturated at the corresponding shear rate.


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