Methods and compositions for removing sulfur from liquid hydrocarbons using ammonium adducts
a technology of ammonium adducts and liquid hydrocarbons, which is applied in the petroleum industry, hydrocarbon oil refining, acid salt refining, etc., can solve the problems of significant reduction of the fuel value of the desulfurized end product, high cost and inherent chemical limitations, and the difficulty of hds removal, etc., to achieve convenient dispersibility and facilitate handling
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example 1
[0022] In this example, a preferred amine adduct was prepared and used to desulfurize Saudi crude oil having a sulfur content of 3.16%.
[0023] The amine adduct was prepared by mixing together 20% by weight of solid benzoic acid and 80% by weight of liquid coco-1,3-diaminopropane, followed by moderate mixing. The reaction was slightly exothermic. Next, 2.5 gms. of the resultant adduct product were added to 30 ml. of water, and this aqueous dispersion was added to 120 ml. of Saudi crude oil. The oil / aqueous adduct mixture was then placed in a separatory funnel which was shaken vigorously approximately 100 times. The hydrocarbon and aqueous phases were then allowed to separate, and the hydrocarbon fraction was drawn off and analyzed to determine total sulfur content. The treated hydrocarbon fraction exhibited a sulfur content of 2.32%, constituting a 26.5% sulfur reduction.
example 2
[0024] The desulfurization test of Example 1 was repeated using 6 additional amine adduct products. Specifically, each amine adduct was prepared by reacting coco-1,3-diaminopropane with glacial acetic acid (Sample A), propionic acid (Sample B), boric acid (Sample C), hydroacetic acid (Sample D), adipic acid (Sample E), and succinic acid (Sample F). The respective samples were dispersed in 30 ml. water, and the resulting dispersions were added to 120 ml. of Alaskan crude oil. The above-described separatory funnel treatment was then carried out on each oil sample.
[0025] The results of this series of tests are set forth in FIG. 1. As illustrated, the untreated oil had a sulfur content of 0.905% and the treatment according to the invention resulted in a reduction in sulfur content of from about 49.2 to 66.4%.
example 3
[0026] In this example, Alaskan crude oil having a sulfur content of 0.894% was mixed with distilled water at varying percentages, and the resulting mixtures were each treated with 25 gms. of the amine-benzoic acid composition of Example 1 in 100 ml. of water. The test protocol of Example 1 was then carried out on each sample, giving the following results:
OilAliquotMixingSulfur Content% Sulfur(ml)Water (ml)(ml)Temp (° F.)(wt. %)Reduction1200101200.3406212010101200.23573.712020101200.52541.312030101200.25271.812050101200.23274.0
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