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Liquid viscosity measurement practical report
Introduction to viscosity lab
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EXPERIMENT NO. 8
AIM: Determination of Viscosity of Lubricating oil at different temperatures by Redwood Viscometer No.1 or 2
THEORY:
Viscosity is one of the most important properties of lubricating oil. The formation of a constant fluid film of a lubricating between the moving surface under particular condition of load, speed and lubricant supply is depend upon the viscosity of lubricating oil. If the viscosity of the oil is too low the fluid lubricant film cannot be maintained between the moving surfaces as results of which excessive wear may takes place. On the other hand if the viscosity of lubricating oil is too high excessive friction due to the shearing of oil itself would result. Hence it is essential to have knowledge of the viscosity of lubricating oil.
Viscosity is a measure of the internal resistance to motion of a fluid and is mainly due to the forces of cohesion between the fluids molecules.
Absolute viscosity may be defined as the tangential force per unit area required to maintained unit velocity gradient between two parallel planes in the fluid at unit distance apart. It is denoted by eta (η). Its unit in CGS system is poise and centipoises.
The ratio of absolute viscosity to density for any fluid is known as its absolute kinematics viscosity. It denoted by (u). And its units are stokes & centistokes.
Kinematics
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Engle Viscometer in Europe & Say bolt viscometer in the USA. In these viscometers, a fixed volume of the liquid is allowed to flow through a capillary tube of specified dimension under given set of condition the time of flow is measured at particular temperature. The viscosity of the oil so determined in the time unit is sometimes called as relative viscosity. The kinematics viscosity of the oil is calculated centistokes from the time taken by the oil to flow through the standard orifice of the instrument with help of the following
He began experimenting with a cup that would regulate the flow of oil onto moving parts of industrial machines.
They just forgot to mention the other effects of fluids in nature. “The influence of the fluid on a body moving through it depends not only on the body’s velocity but also on the velocity of the fluid,” this is called relative velocity ( ). The relative velocity of a body in a fluid has an effect on the magnitude of the acting forces. For example, as a long distance runner is running into a head wind, the force of the fluid is very strong. If the runner is running with the help of a tail wind, the current’s force is reduced and may even be unnoticeable.
Fig. 2(A) shows the phase diagrams of IPM, water, and surfactant mixtures at the ratios of 60:40, 65:35, and 70:30 (v/v), respectively. Fig. 2(B) shows the phase diagrams of ethyl oleate, water, and surfactant mixtures at ratios of 90:10, 95:5 and 100:0, respectively. Filled circles mean self-emulsifying points, and black areas represent the self-emulsifying regions. In other area, the compositions showed inverted emulsion, gel-like form, or phase-separation. In general, when the oil content in the oil and surfactant mixtures is ≤30%, the condition of the mixtures changed from water-in-oil emulsion to a clear gel-like form and then to microemulsion. Otherwise, the dispersions showed phase separation, this result was similar to the results previously studied by Guo et al. [16]. Our finding showed that IPM + surfactant mixture (65:35, v/v) and ethyl oleate + surfactant mixture (90:10, v/v) showed the most self-emulsifying regions (Fig. 2). Overall, in contrast to IPM + surfactant mixture (65:35, v/v), ethyl oleate + surfactant mixture (90:10, v/v) showed finer emulsion in larger self-emulsifying range. These results indicate that ethyl oleate and Tween 80:Carbitol (90:10, v/v) were identified as the optimal oil
In classical fluid dynamics, the Navier-Stokes equations for incompressible viscous fluids and its special (limiting) case the Euler equations for inviscid fluids are sets of non-linear partial differential equations that describes the spatiotemporal evolution of a fluid (gas). Both equations are derived from conservative principles and they model the behavior of some macroscopic variables namely: mass density, velocity and temperature.
It is the ratio of distance travelled by solute and the distance moved by solvent.
The shear viscosity is a transport coefficient for momentum in inhomogeneous flows. This transport coefficient, which is widely used to describe both plasmas and fluids, relates two hydrodynamic quantities: shear stress and shear rate. The shear stress Pxy is the off-diagonal element of a pressure tensor, and the shear rate γ is the transverse gradient of the flow velocity u. For a flow in the y direction,
The equipment they are using was not originally designed for the lower viscosity of Greasex.
kinematic viscosity is normally expressed in terms of centistokes, ρ is mass density in gm/〖cm〗^3 (Druk et al,
The Bernoulli’s equation was mainly derived for ideal fluids i.e zero viscous fluids hence they are frictionless. But all the fluids are real and has some viscosity and hence offer resistance to flow. When the fluid is flowing there will always be some losses across the sections and Bernoulli’s equation considers all the losses.
Slime, has a different viscosity, based on the amount of strength you apply when playing with it. Slowly placing your hands on the slime is being described as a small amount of weight being applied to the slime, they will feel thin and water-like, letting you sink your hand into the jelly like substance. Punching it, or throwing it against a wall,
When the Reynolds number is less than 10 .... it is considered laminar, when it is greater than 100 it is considered turbulent. The areas in between are defined as transitional and can go either way.
In industry, the performance specifications for a particular pump may be known, but the tests are usually based on water as the pumping medium. For liquids of significantly higher viscosity than water, these performance curves may only be accurate at certain flow rates, or they might not be valid at all, and it might be necessary to recalibrate the specifications for higher viscosity liquids.
it is closely related to the force and rate of the heartbeat and the diameter and elasticity of the
Position. SVV was determined using radial Flotrac sensor and femoral PiCCO plus catheter. The decrease in SVV found using Flotrac and PiCCO plus were significant and also the correlation between found between the two SVVs were significant. He also found that SVV measured using FloTrac has lower threshold for prediction than the other.
- the effect of Viscosity on liquid flow (turbulent/laminar) I have consulted my teachers for guidance and I have also looked very carefully into the "the Suggestions papers" which contain many possible investigations which have been done in the past. I opted to choose neither of them but many aspects I will be looking into in my investigation are similar to those in the papers.