초록 ▼

A liquid-liquid contacting apparatus is disclosed. The apparatus is useful in extracting mercaptans from a hydrocarbon stream such as cracked gasoline by nonturbulent countercurrent contacting of the hydrocarbon stream with an aqueous caustic solution. The denser liquid phase flows downward from an

A liquid-liquid contacting apparatus is disclosed. The apparatus is useful in extracting mercaptans from a hydrocarbon stream such as cracked gasoline by nonturbulent countercurrent contacting of the hydrocarbon stream with an aqueous caustic solution. The denser liquid phase flows downward from an upper phase separation zone through a connecting cylindrical contacting zone into a lower phase separation zone. Liquid withdrawal and addition means communicate with each separation zone. A mass of fibrous contacting strands is suspended in the contacting zone. The contacting strands are preferentially wetted by either of the two liquid phases to provide a large surface area which enhances extraction capacity.

대표청구항 ▼

A liquid-liquid contacting apparatus which comprises: (a) a vertical enclosed outer vessel having a unitary cylindrical sidewall and an upper and lower end, said vessel having a means defining an upper phase separation zone located at the upper end of said vessel, a means defining a lower phase sepe

A liquid-liquid contacting apparatus which comprises: (a) a vertical enclosed outer vessel having a unitary cylindrical sidewall and an upper and lower end, said vessel having a means defining an upper phase separation zone located at the upper end of said vessel, a means defining a lower phase seperation zone located at the lower end of said vessel and means extending vertically between said upper and said lower phase seperation zones defining an intermediate contact zone having a height equal to at least one-third of the overall height of said outer vessel and having a smaller diameter than the diameter of the unitary cylindrical sidewall; (b) restraining means located within said lower phase separation zone and supporting means located within said upper phase separation zone; (c) a mass of contacting strands extending vertically between said supporting means and said restraining means in attachment with said supporting means and said restraining means to prevent vertical movement, said restraining means positioning said contacting strands at an inclination to the vertical axis of said intermediate contacting zone of between 1 and 10 degrees; (d) said supporting means including a first liquid distribution means which communicates with a first liquid inlet conduit and which is located in said upper phase separation zone, said first liquid distribution means distributing a fluid onto said contacting strands; (e) a second liquid distribution means which communicates with a second liquid inlet conduit and which is located in said lower phase separation zone, said second liquid distribution means being positioned below said restraining means; (f) a first liquid outlet conduit communicating with said upper phase separation zone positioned at a point above said first liquid distribution means; and, (g) a second liquid outlet conduit communicating with said lower phase separation zone positioned at a point below said second liquid distribution means.