Flash zone draw tray for coker fractionator

• US 4,549,934 A
• Filed: 04/25/1984
• Issued: 10/29/1985
• Est. Priority Date: 04/25/1984
• Status: Expired due to Term

• Current Assignee: Conoco Incorporated 1000 South Pine Ponca City OK
• Original Assignee: Conoco Incorporated (ConocoPhillips)
• Inventors: Janssen, Harry R., Graf, Harlan G., Kurdy, George A.
• Primary Examiner(s): Woo, Jay H.
• Assistant Examiner(s): McGurk, Mike
• Application Number:
  US06/603,869
• Time in Patent Office: 552 Days
• Field of Search: 196/98, 196/100, 196/102, 196/133, 196/140, 208/131, 208/106, 208/48 R, 208/358, 208/350, 201/28
• US Class Current: 196/98
• CPC Class Codes: C10B 55/00 Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material cracking oils C10G
• CPC Class Codes: C10G 7/00 Distillation of hydrocarbon oils
• CPC Class Codes: C10G 7/06 Vacuum distillation
• CPC Class Codes: C10G 9/005 Coking (in order to produce liquid products mainly)

Abstract

An internal draw tray is added to the flash zone of a coker fractionator below the coker vapor inlet to collect condensed coke drum overhead components and to keep the condensed material separate from the fresh feed to the coker furnace.

Claims

1. In a delayed coking unit comprising a coker furnace, at least two coking drums, fresh feed line means, coker transfer line means extending from said furnace to said drums, a coker fractionator, vapor line means extending from said drums to said fractionator, and means in said fractionator for condensing the heavier components of vapor entering said fractionator from said vapor line means, the improvement comprising:

(a) an internal draw tray (50) in said coker fractionator, said tray being below the vapor line means inlet to said coker fractionator and below said means for condensing the heavier components of vapor and being adapted to collect said condensed vapor components, and

(b) means for removing from said coker fractionator and said coking unit said condensed vapor components collected on said internal draw tray.

2. A delayed coking unit in accordance with claim 1 wherein the fresh feed line means is provided for feeding fresh feed to the bottom of said fractionator below said internal draw tray and for transferring fresh feed from the bottom of said fractionator to said coker furnace.

3. A delayed coking unit in accordance with claim 1 wherein said means for condensing the heavier components of vapor comprises means for contacting said vapor with liquid hydrocarbons.

4. A delayed coking unit in accordance with claim 1 wherein said means for condensing the heavier components of vapor comprises indirect heat exchange means.

5. A delayed coking unit in accordance with claim 1 wherein said means for condensing the heavier components of vapor comprises spray nozzles adapted to spray liquid hydrocarbons into said fractionator in contact with said vapor.

6. A delayed coking unit in accordance with claim 5 including a heavy coker gas oil draw tray in said fractionator above said internal draw tray (50) and above said spray nozzles, a heavy coker gas oil line for removing heavy coker gas oil from said heavy coker gas oil draw tray, heat exchanger means for cooling heavy coker gas oil in said heavy coker gas oil line, and a heavy coker gas oil return line for returning cooled heavy coker gas oil to said spray nozzles.

7. A delayed coking unit in accordance with claim 6 including a distillate line for adding distillate which is lighter than heavy coker gas oil to said fresh feed line means as recycle to said coker furnace.