초록 ▼

Sulfur-bearing liquid hydrocarbon feedstocks such as kerosene undergo desulfurization and deodorization by contacting such feedstocks with sodium hydride at normal atmospheric pressure and at elevated temperatures. The resulting liquid is further contacted with a mineral acid such as sulfuric acid a

Sulfur-bearing liquid hydrocarbon feedstocks such as kerosene undergo desulfurization and deodorization by contacting such feedstocks with sodium hydride at normal atmospheric pressure and at elevated temperatures. The resulting liquid is further contacted with a mineral acid such as sulfuric acid and an alkaline neutralizing agent such as caustic soda. The liquid may also be contacted with an oxidizying agent such as sodium hyprochlorite prior to being contacted with the neutralizing agent and with a dehydrating agent such as soda ash after being contacted with the neutralizing agent.

대표청구항 ▼

A process for producing a substantially sulfur-free liquid hydrocarbon having a boiling range of about 150°-200°C., an aromatic content between about 15-18 percent by weight, and a flash point of 38°-43°C., from sulfur-bearing hydrocarbon liquid boiling in the kerosene range, which comprises the ste

A process for producing a substantially sulfur-free liquid hydrocarbon having a boiling range of about 150°-200°C., an aromatic content between about 15-18 percent by weight, and a flash point of 38°-43°C., from sulfur-bearing hydrocarbon liquid boiling in the kerosene range, which comprises the steps of: (a) contacting the sulfur-bearing liquid hydrocarbon with sodium hydride in an amount ranging from about 0.01 to about 5 percent by weight based on the weight of the sulfur-bearing liquid hydrocarbon, in the liquid phase and in a hydrogen free environment at normal atmospheric pressure, and heating the mixture to boiling to form an insoluble sulfide sludge and a hydrocarbon liquid having a reduced sulfur content; (b) distilling said hydrocarbon liquid formed in step (a) and collecting a fraction boiling in the range of about 150°-200°C.; (c) contacting the hydrocarbon fraction from step (b) with sulfuric acid and permitting the mixture of said hydrocarbon and said acid to separate into an acid fraction and hydrocarbon fraction, said contacting being conducted at normal atmospheric pressure; (d) contacting the hydrocarbon fraction from step (c) sequentially with an alkaline oxidizing agent, a strong alkaline neutralizing agent, and a hot wash water to form a substantially sulfur-free hydrocarbon fraction and an aqueous fraction; and, (e) recovering said sulfur-free hydrocarbon fraction.