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This is illustrated in Fig. 1c which shows the effect of changes in x 1 from 0.2 to 2.5 when D is constant (unity).
A step input is a constant input, a unit step, a constant unity.
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Let the scaling function be constant or unity, one can obtain PS or CS.
In the original MM/PBSA approach, E el was calculated with a dielectric constant of unity (ϵ = 1) [7,8].
Compactness constant is unity for a perfect circle, and increases as the basin length increases.
One can get velocity of unobstructed tube by taking R as constant or unity.
The sand flux is calculated using Bagnold's relation with a constant of unity, velocity × height, to show the relative change.
It is noted that D = 2a0 = dist(A1, A2) and now consider the constraint (3.1) with functions s, x, r, t: (A1 ∪ A2) × (A1 ∪ A2) → R+ being constant identically unity.
The experimental results indicate that there is no effect of concentration of polymer on the density of fluid it is all most constant at unity which is of water.
It is constant near unity at low momentum ratios, begins to decay at momentum ratios exceeding 0.1, and attains a decay rate at higher momentum ratios consistent with constant flame height.
The major result is that, in contrast to the various previous claims of extinction Karlovitz number being anywhere between 0.03 and 20, it is found to be constant around unity for the mixtures tested.
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