Tek-Tips is the largest IT community on the Internet today!

Members share and learn making Tek-Tips Forums the best source of peer-reviewed technical information on the Internet!

  • Congratulations JAE on being selected by the Eng-Tips community for having the most helpful posts in the forums last week. Way to Go!

Crude Oil Blending

Status
Not open for further replies.

S.G

Petroleum
Joined
Dec 22, 2022
Messages
64
Location
AE
Dear All,

I found below in a test paper. but still searching for the API/ASTM crude reference which puts why API’s cannot be averages into understandable language???

Question 1

Equal volumes of a 30°API, 20°API, and 15°API crude are blended to produce a feed to refinery. Estimate the °API of the resulting blend. Clearly state your assumptions and comment on your result. (Hint: Would °API blend linearly?) 15 pts
Answer:
Blend: Equal volumes of 30°API, 20°API, and 15°API
°API = 141.5/SG60oF - 131.5

°Theoretically APIs cannot be averaged, but SGs can be, assuming that the volume change upon mixing the three crudes is negligible.
Determine SG of each crude, calculate average SG, and use this value to calculate the blend °API.

30= 141.5/SG1–131.5, 20= 141.5/SG2–131.5, 15=141.5/SG3 – 131.5
SG1 = 0.876 SG2 = 0.933 SG3= 0.966

SGavg = AVG (0.876:0.933:0.966)
SGavg = 0.925

°APIblend = 141.5/0.863 – 131.5
°APIblend = 21.4

Note that the blend °API is not a simple a mean of the component °API’s (AVG 30:20:15) = 21.7. Although the difference appears to be small, it is important to use the precise °API in several calculations and correlations that are used to predict the quality and yield of refinery products.
 
Status
Not open for further replies.

Part and Inventory Search

Sponsor

Back
Top