Method for removing liquid from a liquid-solids mixture

• US 4,778,605 A
• Filed: 04/29/1987
• Issued: 10/18/1988
• Est. Priority Date: 04/29/1987
• Status: Expired due to Fees

• Current Assignee: Phillips Petroleum Company (ConocoPhillips)
• Original Assignee: Phillips Petroleum Company (ConocoPhillips)
• Inventors: Limoges, Brian H., Young, Richard K., Anthoney, William R.
• Primary Examiner(s): NOT, DEFINED
• Assistant Examiner(s): Lee, Coreen Y.
• Application Number:
  US07/045,109
• Time in Patent Office: 538 Days
• Field of Search: 210/770, 210/774, 210/806, 210/808, 210/180, 210/184, 210/188, 202/197, 202/175, 203/4, 203/40, 203/91, 159/DIG. 2, 159/DIG. 16, 159/901, 502/107, 502/439
• US Class Current: 210/770
• CPC Class Codes: B01D 35/185 comprising a vaporizing unit
• CPC Class Codes: B01D 36/001 Filters in combination with devices for the removal of gas, air purge systems
• CPC Class Codes: F26B 7/00 Drying solid materials or objects by processes using a combination of processes not covered by a single one of groups F26B3/00 and F26B5/00 F26B1/005, F26B5/04, F26B23/026 take precedence
• CPC Class Codes: Y10S 159/16 Vacuum
• CPC Class Codes: Y10S 159/901 Promoting circulation

Abstract

An apparatus and method are provided wherein liquid is removed from a liquid-solids mixture by employing both filtration and low pressures to achieve vaporization of liquid. The mixture is introduced to a vessel in which the mixture is filtered so that a substantial portion of the liquid is withdrawn from the vessel. The vessel is then depressurized to an extent necessary to vaporize a substantial portion of the remaining liquid. Such vapor is withdrawn from the vessel. During vaporization, the contents of the vessel are agitated and heated.

Claims

1. A method for removing liquid from a liquid-solids mixture comprising the steps of:

(a) introducing the mixture to a vessel;

(b) filtering the mixture within the vessel after step (a) so as to withdraw a substantial portion of the liquid from the vessel through at least one filter;

(c) withdrawing from the vessel, through a first conduit line, gases present in the vessel after step (b) so as to depressurize the vessel to predetermined pressure conditions whereby liquid remaining in the vessel after step (b) tends to vaporize;

(d) maintaining said pressure conditions for a period of time so that a substantial portion of liquid remaining in the vessel after step (b) vaporizes to a vapor;

(e) heating the contents of the vessel during step (d);

(f) agitating the contents of the vessel at least during step (d);

(g) withdrawing the vapor from the vessel through a second conduit line during step (d); and

(h) withdrawing substantially dry solids from the vessel after steps (d) and (g).

2. A method as recited in claim 1, further comprising the step of pressurizing the interior of the vessel with a gas after step (a), and before and during step (b) so as to assist in the flow of liquid through said at least one filter.

3. A method as recited in claim 2, further comprising the step of flowing a gas through the interior of the vessel during at least a portion of steps (d) and (g).

4. A method as recited in claim 3, wherein the vessel has a lower end and an upper end and wherein the vapor is withdrawn in step (g) through the upper end, and wherein in said gas flowing step the gas flows generally upwardly from the lower end of the vessel, through solids which accumulate near the lower end, and through the upper end of the vessel so as to exit the vessel.

5. A method as recited in claim 4 wherein said gas flowing step is performed near the end of step (d).

6. A method as recited in claim 5, wherein the gas employed in said pressurizing and gas flowing steps comprises nitrogen.

7. A method as recited in claim 5 further comprising the step of filtering the vapor during step (g) to prevent withdrawal of entrained solids with the vapor.

8. A method as recited in claim 7, wherein the vessel has an exterior surface which is heated in step (e).

9. A method as recited in claim 8, wherein the solids comprise a propylene polymerization catalyst and the liquid is selected from the group consisting of toluene and hexane.

10. A method as recited in claim 9, wherein the contents of the vessel during step (e) is maintained below about 122°

F.

11. A method as recited in claim 9 wherein the pressure in the vessel is maintained at about 10 mm Hg abs. in step (d).

12. A method as recited in claim 11 wherein the liquid is toluene.