Process for the purification of a cracking gas stream in an oil scrub column

Patent metadata

Field	Value
Publication number	US-10160702-B2
Application number	US-201415022308-A
Country	US
Kind code	B2
Filing date	Aug 5, 2014
Priority date	Sep 25, 2013
Publication date	Dec 25, 2018
Grant date	Dec 25, 2018

Abstract

A process for removing a petroleum spirit fraction and also an oil fraction from a cracking gas stream in an oil scrub column, wherein, the ratio of the amount of substance of the petroleum spirit fraction recycled into the benzene section at the top per unit time to the amount of substance of the cracking gas introduced into the oil section per unit time is in a range from 1:16 to 1:10, preferably 1:12 to 1:10.

First claim

The invention claimed is:

1. A process for purification of a cracking gas stream in an oil scrub column having a shell extending along a longitudinal axis and enclosing an interior of the column, the interior being subdivided into a petroleum spirit section and an oil section arranged below the petroleum spirit section along the longitudinal axis, said process comprising:
introducing an amount of a cracking gas stream into the oil section wherein the cracking gas stream passes from bottom to top of the oil section along the longitudinal axis through second mass transfer trays of the oil section which are arranged one above another, and wherein a liquid, hydrocarbon-containing second scrubbing medium flows in said oil section in countercurrent to the cracking gas stream in order to separate out an oil fraction from the cracking gas stream,
said second mass transfer trays each having a plurality of runoff elements extending parallel to and at a distance from one another, wherein each runoff element has first and second runoff surfaces along which a second scrubbing medium runs downward and which converge along the longitudinal axis towards the petroleum spirit section and meet, and in so doing form an edge extending transversely to the longitudinal axis,
passing the cracking gas stream, after traversing the second mass transfer trays of the oil section, into the petroleum spirit section, wherein the cracking gas stream flows along the longitudinal axis from bottom to top of petroleum spirit section through first mass transfer trays of the petroleum spirit section, said first mass transfer trays being arranged one above another and being sieve trays, bubble trays and/or valve trays, and wherein a liquid, hydrocarbon-containing first scrubbing medium flows in said petroleum spirit section in countercurrent to the cracking gas stream in order to remove a petroleum spirit fraction from the cracking gas stream,
withdrawing the cracking gas stream from a top of the petroleum spirit section,
withdrawing the petroleum spirit fraction from the petroleum spirit section,
recycling an amount of the petroleum spirit fraction as the first scrubbing medium into the top of the petroleum spirit section,
wherein the amount of the petroleum spirit fraction recycled into the petroleum spirit section per unit time and the amount of the cracking gas introduced into the oil section per unit time are at a ratio of from 1:16 to 1:10.

2. The process according to claim 1 , further comprising recycling a portion of the petroleum spirit fraction onto one of the first mass transfer trays.

3. The process according to claim 2 , wherein said portion of the petroleum spirit fraction is recycled to the second-lowermost, third-lowermost or fourth-lowermost first mass transfer tray.

4. The process according to claim 1 , wherein the petroleum spirit fraction is drawn off from a chimney tray that separates the petroleum spirit section from the oil section or from a lowermost first mass transfer tray that separates the petroleum spirit section from the oil section.

5. The process according to claim 1 , wherein
said oil section is subdivided into a light oil section and a heavy oil section, which is arranged below said light oil section along the longitudinal axis, a plurality of second mass transfer trays are arranged in each of the light oil section and the heavy oil section, wherein the cracking gas stream is guided through the second mass transfer trays of the heavy oil section and subsequently through the second mass transfer trays of the light oil section, and
wherein the second mass transfer trays in the heavy oil section are supplied with a liquid, hydrocarbon-containing third scrubbing medium to separate out a heavy oil fraction from the cracking gas stream, and the second transfer trays in the light oil section are supplied with said liquid, hydrocarbon-containing second scrubbing medium to separate out a light oil fraction from the cracking gas stream.

6. The process according to claim 1 , wherein the petroleum spirit section has 6 to 8 first mass transfer trays.

7. The process according to claim 1 , wherein t the oil section has 10 to 20 second mass transfer trays.

8. The process according to claim 5 , wherein the light oil section has 6 to 12 second mass transfer trays.

9. The process according to claim 5 , wherein the heavy oil section has 4 to 8 second mass transfer trays.

10. The process according to claim 5 , wherein
the oil scrub column has a first liquid distributor arranged in the light oil section, wherein by means of said first liquid distributor the second mass transfer trays are supplied with the second scrubbing medium, wherein the first liquid distributor introduces the second scrubbing medium onto the edges of the runoff elements of an uppermost second mass transfer tray of the light oil section so that the second scrubbing medium flows off from the respective runoff element via the runoff surfaces at both sides of the respective edge,
the oil scrub column has a second liquid distributor is arranged in the heavy oil section, wherein by means of said second liquid distributor the second mass transfer trays of the heavy oil section are supplied with the third scrubbing medium, wherein the second liquid distributor introduces the third scrubbing medium onto the edges of the runoff elements of an uppermost second mass transfer tray of the heavy oil section, so that the third scrubbing medium flows off from the respective runoff element via the runoff surfaces at both sides of the respective edge.

11. The process according to claim 10 , wherein the first and/or the second liquid distributors each have a plurality of cutouts through which the respective scrubbing medium is introduced onto the edges of the runoff elements of the respective uppermost second mass transfer tray, where the cutouts are each arranged perpendicularly above an edge of an assigned runoff element.

12. The process according to claim 10 , wherein the first and/or the second liquid distributors each have a plurality of final distributor channels which extend along the column cross section and extend transversely to the runoff elements.

13. The process according to claim 12 , wherein the final distributor channels each have a base which extends transversely to the longitudinal axis, and two side walls starting from said base, where said side walls each have an upper rim, and where the cutouts are designed in the form of vacancies at the upper rim of each sidewall.

14. The process according to claim 13 , wherein the first and/or second liquid distributors have at least two preliminary distributor channels, which are parallel to one another and arranged above the final distributor channels along the longitudinal axis, wherein said final distributor channels are charged with the respective scrubbing medium by means of said preliminary distributor channels, and wherein the preliminary distributor channels extend along the column cross section and extend transversely to the final distributor channels.

15. The process according to claim 14 , wherein each of the preliminary distributor channels each has a base which extends transversely to the longitudinal axis, and two side walls starting from said base, where said side walls each have an upper rim, at which cutouts are designed in the form of vacancies via which the respective scrubbing medium is led into respectively one assigned final distributor channel, wherein these cutouts of the preliminary distributor channels are arranged in each case perpendicularly above an assigned final distributor channel, and the preliminary distri

Assignees

• Linde Ag

Inventors

• Alzner Gerhard
• Matten Christian

Classifications

• B01D3/143 Primary

  by two or more of a fractionation, separation or rectification step · CPC title

• B01D53/1487

  Removing organic compounds · CPC title

• B01D3/163

  Plates with valves · CPC title

• C10K1/18

  hydrocarbon oils {(C10K1/165 takes precedence)} · CPC title

• B01D2252/20

  Organic absorbents · CPC title