Close-coupling of interreboiling to recovered heat

• US 5,755,115 A
• Filed: 01/30/1996
• Issued: 05/26/1998
• Est. Priority Date: 01/30/1996
• Status: Expired due to Term

• Current Assignee: David B. Manley
• Original Assignee: David B. Manley
• Inventors: Manley, David B.
• Primary Examiner(s): Capossela, Ronald C.
• Application Number:
  US08/593,617
• Time in Patent Office: 847 Days
• Field of Search: 62/620, 62/630
• US Class Current: 62/620
• CPC Class Codes: F25J 2200/50 using multiple (re-)boiler-condensers at different heights of the column
• CPC Class Codes: F25J 3/0209 Natural gas or substitute natural gas
• CPC Class Codes: F25J 3/0233 separation of CnHm with 1 carbon atom or more
• CPC Class Codes: F25J 3/0238 separation of CnHm with 2 carbon atoms or more

Abstract

The present invention is an improvement in distillation column interreboiling. Previously, hot bottoms streams could be used to heat interreboilers, although heat recovery was limited by approach temperatures of a stream losing sensible heat to a stream gaining sensible heat and heat of vaporization. The present invention expands the number of stages between the draw and return stages for an interreboiler, thus increasing the heat recovery from the bottom stream and reducing hot utilities to the reboiler, among other important advantages. The present invention is shown for NGL deethanization.

Claims

1. A process for interreboiling a column comprising:

(a) an interreboiler, connected to the column at draw and return stages in a stripping section of the column, to heat and return a column sidedraw;

(b) locating the draw stage of the interreboiler at least 2 theoretical stages above the return stage; and

(c) interreboiling in the interreboiler during the operation of the column to effect indirect heat transfer from a stream of two or more components to a column stream from the draw stage and passing through the interreboiler.

2. The process of claim 1 wherein less than 10 theoretical stages are located between the draw and return stages in the column.

3. The process of claim 1 wherein the column produces a bottom stream that indirectly heats the interreboiler.

4. The process of claim 1 wherein the bottom stream provides all heating used in the interreboiler.

5. The process of claim 4 wherein the column is a deethanizer separating a feed consisting essentially of ethane, propane, isobutane, normal butane and gasoline range components.

6. The process of claim 5 wherein the column is operated at over about 200 psia.

7. The process of claim 6 wherein the temperatures of the process stream from the column in the interreboiler compared to the temperatures of the stream of two or more components in the interreboiler at each point of indirect heat transfer in the interreboiler are never more than about 30°

F. apart.

8. The process of claim 4 wherein a heavy key component of the column feed is less than about 40 volume percent of the bottom stream.

17. The process of claim 4 wherein a heavy key component of the column feed is less than about 40 volume percent of the bottom stream.

9. A process for interreboiling a column comprising:

(a) a plurality of interreboilers, each connected to the column at draw and return stages in a stripping section of the column, wherein each heats and returns a column sidedraw;

(b) locating the draw stage of each interreboiler at least 2 theoretical stages above the return stage of that interreboiler;

(c) locating the draw and return stages so that no draw or return stage of one interreboiler is between the draw and return stage of any other interreboiler; and

(d) interreboiling in the interreboilers during the operation of the column wherein in each interreboiler indirect heat transfer from a stream of two or more components heats a column stream from the draw stage respective to and passing through the interreboiler.

10. The process of claim 9 wherein less than 10 theoretical stages are located between the draw and return stages in the column for each interreboiler.

11. The process of claim 9 wherein the column produces a bottom stream that indirectly heats the interreboilers.

12. The process of claim 9 wherein the bottom stream provides all heating used in the interreboilers.

13. The process of claim 12 wherein the bottom stream first heats an interreboiler connected lowest in the column and then sequentially heats other interreboilers connected above the lowest interreboiler in the column.

14. The process of claim 12 wherein the column is a deethanizer separating a feed consisting essentially of ethane, propane, isobutane, normal butane and gasoline range components.

15. The process of claim 14 wherein the column is operated at over about 400 psia.

16. The process of claim 15 wherein, within each interreboiler, temperatures of the process stream from the column in the interreboiler compared to the temperatures of the stream of two or more components in the interreboiler at each point of indirect heat transfer in the interreboiler are never more than about 30°

F. apart.