High efficiency/low pressure catalytic cracking spray nozzle assembly

Patent metadata

Field	Value
Publication number	US-10201794-B2
Application number	US-201415023472-A
Country	US
Kind code	B2
Filing date	Sep 18, 2014
Priority date	Sep 20, 2013
Publication date	Feb 12, 2019
Grant date	Feb 12, 2019

Abstract

A gas assisted liquid spray nozzle assembly having a nozzle body that defines a mixing zone, a liquid inlet communicating with the mixing zone from an end, and a pressurized gas inlet communicating with the mixing chamber from an upstream side. The liquid inlet includes a liquid injector extending into the nozzle body having a liquid inlet extension passage and a plurality of discharge orifices adjacent a closed downstream end which define an impingement surface for directing liquid into the mixing zone in transverse relation to a central axis of the mixing zone. The nozzle body and liquid injector define a plurality of concentrating gas discharge passages at respective locations of the injector liquid discharge orifices for causing individual pressurized gas to directly interact with transversely directed liquid into the mixing zone for enhanced atomization and ultimate discharge from a downstream spray tip.

First claim

The invention claimed is:

1. A catalytic cracking system comprising: a riser, a spray nozzle assembly having a nozzle body supported within a wall of the riser for discharging atomized liquid hydrocarbon into the riser, said nozzle body defining a mixing zone and an elongated barrel extension zone longer in length than the mixing zone extending downstream and in communication with said mixing zone extending through-said riser wall, a liquid hydrocarbon inlet outside said riser wall connected to a liquid hydrocarbon supply for directing a pressurized liquid hydrocarbon into said mixing zone, a steam inlet outside said riser wall connected to a pressurized steam supply for directing pressurized steam into said mixing zone, said liquid hydrocarbon inlet communicating with an elongated liquid injector disposed upstream of said barrel extension zone extending into the mixing zone along a central axis of the mixing zone, said nozzle body defining an annular gas chamber upstream of said barrel extension zone communicating with said steam inlet and surrounding said liquid injector, said liquid injector having a liquid inlet extension passageway and a plurality of discharge orifices adjacent to a downstream end of said extension passageway for directing liquid hydrocarbon from said extension passageway into the mixing zone in transverse relation to the central axis of the mixing zone, said nozzle body and liquid injector defining a plurality of individual concentrating steam discharge passages at a downstream end of said gas chamber each at a location of and aligned with a respective injector liquid discharge orifice for causing individual pressurized steam streams to directly interact with liquid hydrocarbon transversely directed into said mixing zone from the liquid injector discharge orifices and for directing atomized liquid hydrocarbon through said barrel extension zone, and a spray tip mounted at a downstream end of said barrel zone having a discharge orifice through which atomized liquid hydrocarbon directed through said barrel zone is discharged in a predetermined spray pattern.

2. The catalytic cracking system of claim 1 in which said steam inlet communicates with said mixing zone through a side wall of the nozzle body.

3. The catalytic cracking system of claim 1 in which said liquid injector has a closed downstream end which defines an internal impingement surface against which liquid hydrocarbon directed through said liquid injector extension passageway impinges and is transversely directed outwardly through said liquid injector discharge orifices.

4. The catalytic cracking system of claim 3 in which said impingement surface is defined by a plurality of said liquid injector discharge orifices extending transversely through the liquid injector adjacent a downstream end thereof.

5. The catalytic cracking system of claim 3 in which said impingement surface is defined by an x-configuration of said injector liquid discharge orifices.

6. The catalytic cracking system of claim 1 in which said liquid hydrocarbon inlet includes an orifice member that defines a predetermined sized liquid inlet passage, and said liquid injector is a separate tubular member mounted downstream of said orifice member.

7. The catalytic cracking system of claim 1 in which said plurality of concentrating steam discharge passages are defined between said liquid injector and a ring disposed within said nozzle body about said liquid injector at a downstream end of said annular gas chamber.

8. The catalytic cracking system of claim 7 in which said liquid injector is formed with external flats across said liquid discharge orifices, and said concentrating steam passages are defined between said external flats of said injector and an interior of said ring.

9. The catalytic cracking system of claim 1 in which said liquid injector is supported within said nozzle body at a downstream end by an annular wall which defines a downstream end of said annular gas chamber, and said plurality of concentrating steam discharge passages communicate between said annular gas chamber and said barrel extension zone.

10. The catalytic cracking system of claim 9 including a ring supported within said annular wall, and said plurality of concentrating steam discharge passages are defined between said ring and a downstream end of said elongated liquid injector.

11. The catalytic cracking system of claim 10 in which said ring extends upstream of said annular wall.

12. The catalytic cracking system of claim 10 in which said liquid injector is formed with external flats across said injector liquid discharge orifices, and said concentrating steam discharge passages are defined between said external flats and said ring.

13. The catalytic cracking system of claim 1 in which said injector liquid discharge orifices define a flat internal impingement surface perpendicular to said central axis of said mixing zone against which pressurized liquid hydrocarbon directed through said liquid extension passageway impinges and is transversely directed.

14. The catalytic cracking system of claim 1 in which said nozzle body is in the form of a one piece hollow cylindrical tubular member.

15. The catalytic cracking systems claim 1 in which said liquid injector is disposed within said nozzle body at a location outside said riser wall.

Assignees

• Spraying Systems Co

Inventors

• Lacroix Mark

Classifications

• B01J8/1827 Primary

  the fluidising gas being a reactant · CPC title

• C10G11/18

  according to the "fluidised-bed" technique · CPC title

• B01J2208/00902

  Nozzle-type feeding elements · CPC title

• B01J8/1818

  Feeding of the fluidising gas (B01J8/44 takes precedence) · CPC title

• B05B1/044

  Slits, e.g. narrow openings defined by two straight and parallel lips; Elongated outlets for producing very wide discharges, e.g. fluid curtains (B05B1/046 takes precedence) · CPC title