Method for removing petroleum acid in hydrocarbon oil by using membrane dispersion extractor
An extractor and membrane dispersion technology, which can be used in refining by dialysis, solvent extraction of liquid solutions, etc., can solve the problems of strong corrosiveness, low deacidification effect, and large equipment investment.
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Embodiment 1
[0019] Composition of deacidification solvent (by weight percentage)
[0020] Table 1 Composition of deacidification solvent
[0021] name
Ammonia concentration%
Auxiliary concentration%
water%
Deacidification solvent 1
1
20 (alcohol)
79
Deacidification solvent 2
3
30 (alcohol)
67
Deacidification solvent 3
5
40 (alcohol)
55
Deacidification solvent 4
8
45 (alcohol)
47
Deacidification solvent 5
10
50 (alcohol)
40
Deacidification solvent 6
12
55 (alcohol)
33
Deacidification solvent 7
15
60 (alcohol)
25
Deacidification solvent 8
13
70 (alcohol)
17
Deacidification solvent 9
11
65 (alcohol)
24
Deacidification solvent 10
2
0.02 (sodium petroleum acid)
97.98
Deacidification solvent 11
4
0.2 (sodium petroleum acid)
95.8
Deacidification solvent 12
9
2 (Sodium Petroleum A...
Embodiment 2
[0026] Deacidification solvent 4: 8% ammonia + 45% alcohol + 47% water;
[0027] Ordinary third-line distillate oil: the acid value is 4.6mgKOH / g;
[0028] The constant third-line distillate continuous phase with an acid value of 4.6mgKOH / g and a temperature of 50°C and the above-mentioned deacidification solvent 4 dispersed phase with a temperature of 10°C are passed through the The respective metering pumps are sent into the flat ceramic membrane with a membrane pore size of 0.05 μm, and the flow rate of the dispersed phase is 0.5L / cm 2 h, the pressure difference between the dispersed phase and the continuous phase is 0.06MPa, the mixture of the continuous phase and the dispersed phase stays in the membrane device for 0.5 seconds and then enters the phase separation and clarification tank, and after 1min settling time at room temperature, petroleum acid is removed The purified oil and the aqueous solution containing ammonium petroleum acid are completely separated in two ph...
Embodiment 3
[0030] Deacidification solvent 3: 5% ammonia + 40% alcohol + 55% water;
[0031] Diesel: the acidity is 37mgKOH / 100ml;
[0032] The continuous phase of diesel oil with an acidity of 37mgKOH / 100ml and a temperature of 20°C and the above-mentioned deacidification solvent 3 dispersed phase at a temperature of 15°C, according to the volume ratio of the continuous phase to the dispersed phase of 47:1, are respectively pumped through their respective metering pumps. The flow rate of the dispersed phase is 0.5L / cm in the flat stainless steel sintered membrane with a pore size of 0.05 μm 2 h, the pressure difference between the dispersed phase and the continuous phase is 0.08MPa, the mixture of the continuous phase and the dispersed phase stays in the membrane device for 0.4 seconds and then enters the phase separation and clarification tank. After 45 seconds of settling time at room temperature, the oil is removed The purified oil of acid and the aqueous solution containing ammonium...
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