Abstract:
A lab-sized test and evaluation system of petroleum products evaporation loss (PPEL) in petroleum products loading tank is built up with reference to field operation process and performance of PPEL. Taking gasoline for example, the vented gasoline vapor mole fraction C
H and its mean value
CH and the total evapo-ration lossage η in the entire course of loading gasoline are measured and calculated and compared with their theoretic minimum values C
H0,
CH0, and η
0, respectively. Some key effect factors on C
H(C
H) and η are analyzed and appraised. The results show that ratio λ of height of the exit of filling gasoline pipeline to tank height, initial vapor mole fraction C
0 in the tank gas space, speed U of filling gasoline, and temperature t of the system influence notably on C
H (
CH) and η, and the increasing grads of
CH with the effect factors at the so-designed tests are about 0.198, 0.167, 0.211 (h·m
-1), 0. 0189 (℃
-1), respectively. At the test of C
0=0 and λ=0.1, the mean vented vapor mole saturation ϕ′/ ϕ′
max is 0.5, which is lower about 0.25 than the ϕ′/ ϕ
′max which is total mean mole saturation at the whole tests of C
0 =0 and λ=0.8. At the whole tests of C
0=0, η=0.192%~0.661% and η
0 = 0.083%~0.229%, but at the test of C
0 =0.56 and λ=0.8, η=0.695%. So, the so-called PPEL is very seriously and harmfully, which will bring about hidden fire acci-dent, environmental pollution, waste and degradation of petroleum products, and so on. Last, some advice is given to lower PPEL.