- Kin. Viscosity Calculator - blend of Petroleum Products
Following article is mainly for gasoil, how to predict blended product Kin. Viscosity.
Kin. Viscosity like Flash point is not an additive property.
How to predict Kin. Viscosity of resultant product after blending two stocks ? or how to get volume required of products to get desired blended product Kin. Viscosity ?
Kin. Viscosity like Flash point is not an additive property.
How to predict Kin. Viscosity of resultant product after blending two stocks ? or how to get volume required of products to get desired blended product Kin. Viscosity ?
Many times Viscosity improvement is desired by blending higher Viscosity petroleum product to lower Viscosity Product at Petroleum storage depots.
Following table and formula can be used to predict the desirable variable figure of kin. Viscosity or volume of product. In the table below against Kin. Viscosity (cSt) viscosity blending number "A" is listed in next column.
Formula :
Formula :
Ar * 100 = (V1 * A1 ) + (V2 *A2)
A for Resultant KV * 100
= ( Volume % of Stock1 * A for Stock1 ) + ( Volume % of Stock2 * A for Stock2 )
= ( Volume % of Stock1 * A for Stock1 ) + ( Volume % of Stock2 * A for Stock2 )
Kin. Viscosity is in cSt and it is at any given temperature.
Where Viscosity blending number A can be taken from table against Kin. Viscosity.
Where Viscosity blending number A can be taken from table against Kin. Viscosity.
Kin. Visc
|
A
|
Kin. Visc
|
A
|
Kin. Visc
|
A
|
Cst
|
Cst
|
Cst
|
|||
1.4
|
119.6
|
3.6
|
66.6
|
5.8
|
49.5
|
1.6
|
110.1
|
3.8
|
64.4
|
6
|
48.5
|
1.8
|
102.3
|
4
|
62.4
|
6.2
|
47.5
|
2
|
95.8
|
4.2
|
60.5
|
6.4
|
46.6
|
2.2
|
90.3
|
4.4
|
58.8
|
6.6
|
45.7
|
2.4
|
85.6
|
4.6
|
57.2
|
6.8
|
44.9
|
2.6
|
81.5
|
4.8
|
55.7
|
7
|
44.1
|
2.8
|
77.8
|
5
|
54.3
|
7.2
|
43.3
|
3
|
74.5
|
5.2
|
53.0
|
7.4
|
42.6
|
3.2
|
71.6
|
5.4
|
51.8
|
7.6
|
41.9
|
3.4
|
69.0
|
5.6
|
50.6
|
7.8
|
41.2
|
Above table is based on equation
Viscosity Blending Index = 147.3 X (Kin. Visc)(-0.62)
The above is clear from the following examples:
Ex 1: KV of Blend
Stock1, KV= 1.8 cSt, vol=50 %, From table Blending number A for 1.8 = 102.3
Stock2, KV= 6.4 cSt, vol=50 %, From table Blending number A for 4.8 = 55.7 ,
Then from equation Ar* 100 = (50 * 102.3) + (50 * 55.7)
Solving Ar = 79
From the table, nearest Resultant KV is 2.7 at Blending number Ar of 79
Ex 2: Stock1, KV= 2.8 cSt, vol=20 %, From table Blending number A for 2.8 = 77.8
Stock2, KV= 6.4 cSt, vol=80 %, From table Blending number A for 6.4 = 46.6 ,
Then from equation Ar* 100 = (20 * 77.8) + (80 * 46.6)
Solving Ar = 52.8
From the table, nearest Resultant KV is 5.28 at Blending number Ar of 52.8
Notes : Above calculations predict nearly accurate Kin. Viscosity of blended product, however, usual precautions are must for margin in KV to take care non-homogeneity of mixture and layering in petroleum product tank.
For Excel sheet of above as calculator follow link
https://rjpatelioc-petroleum.blogspot.in/2017/04/kin-viscosity-gasoil-excel-calculator.html
For Excel sheet of above as calculator follow link
https://rjpatelioc-petroleum.blogspot.in/2017/04/kin-viscosity-gasoil-excel-calculator.html
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