Fractionation system

• US 4,395,310 A
• Filed: 07/14/1981
• Issued: 07/26/1983
• Est. Priority Date: 07/14/1981
• Status: Expired due to Fees

• Current Assignee: Exxon Research and Engineering Company (Exxon Mobil Corporation)
• Original Assignee: Exxon Research and Engineering Company (Exxon Mobil Corporation)
• Inventors: Idenden, John E.
• Primary Examiner(s): Sever, Frank
• Application Number:
  US06/283,231
• Time in Patent Office: 742 Days
• Field of Search: 203/1, 203/2, 203/24, 203/26, 203/21, 203/23, 203/25, 203/DIG. 18, 203/DIG. 4, 203/DIG. 8, 585/800, 202/160, 208/DIG. 1, 196/132, 62/26, 62/30, 62/21, 62/37
• US Class Current: 203/2
• CPC Class Codes: B01D 3/007 Energy recuperation; Heat pumps
• CPC Class Codes: B01D 3/14 Fractional distillation or use of a fractionation or rectification column
• CPC Class Codes: B01D 3/322 Reboiler specifications
• CPC Class Codes: C07C 7/04 by distillation
• CPC Class Codes: Y10S 203/04 Heat pump
• CPC Class Codes: Y10S 203/08 Waste heat
• CPC Class Codes: Y10S 203/19 Sidestream
• CPC Class Codes: Y10S 208/01 Automatic control

Abstract

A method for decreasing the external energy input to a fractionation system is disclosed. The method utilizes a compression zone communicating with either the overhead fraction or the bottoms fraction from a fractionation zone. The method is directed at regulating the rate of energy addition and/or removal to the fractionation zone by at least one of the fractions returned to the fractionation zone to maintain the separated fractions within the desired limits.

Claims

1. A method for reducing the energy input to a fractionation system comprising a fractionation zone, a reboiler zone communicating with the fractionation zone, and a compression zone communicating with the fractionation zone and the reboiler zone, said method comprising:

A. introducing a hydrocarbon feed into the fractionation zone, the fractionation zone adapted to separate the feed into an overhead fraction and a bottoms fraction;

B. passing at least a portion of the bottoms fraction from the fractionation zone through a reboiler zone for reheating prior to returning bottoms fraction to the fractionation zone;

C. passing overhead fraction through a compression zone wherein the overhead fraction is compressed;

D. passing substantially all the overhead fraction from the compression zone through the reboiler zone, the compressed overhead fraction transferring heat to the bottoms fraction;

E. returning an overhead fraction consisting of a liquid phase quantity and a vapor phase quantity to the fractionation zone;

F. monitoring the composition of at least one of the fractions separated in the fractionation zone; and

,

G. regulating the rate of said liquid phase quantity of the overhead fraction returned to the fractionation zone sufficient to thereby reduce the energy input to the fractionation system as compared to a fractionation system having no compression zone.

2. The method of claim 1 wherein the overhead fraction from the fractionation zone is preheated prior to entering the compression zone by the overhead fraction from the reboiler zone.

3. The method of claim 2 wherein at least a portion of the overhead fraction returned to the fractionation zone is further heated by an external heat source.

4. The method of claim 2 wherein a portion of the overhead fraction from the reboiler zone is removed after preheating the overhead fraction from the fractionation zone.