Catalytic cracking spray nozzle with internal liquid particle dispersion ring

Patent metadata

Field	Value
Publication number	US-9925508-B2
Application number	US-201415036238-A
Country	US
Kind code	B2
Filing date	Oct 3, 2014
Priority date	Nov 12, 2013
Publication date	Mar 27, 2018
Grant date	Mar 27, 2018

Abstract

A gas assisted spray nozzle assembly having a nozzle body in the form of a hollow tubular member, such as a single cylindrical pipe section, which defines a mixing zone and a downstream barrel extension zone. A liquid inlet and an impingement pin are supported by the tubular member in opposed relation to each other at the mixing zone, and a pressurized gas inlet is provided at an upstream end of the tubular member. An annular dispersion ring is fixedly supported within the tubular member downstream of the impingement pin for defining an annular ledge for directing a peripheral portion of pressurized gas stream and liquid atomized in the mixing zone radially inwardly for facilitating continued intermixing of the liquid and pressurized gas stream as they proceed through the barrel zone for discharge from the spray nozzle.

First claim

The invention claimed is:

1. A catalytic cracking system comprising:
a riser;
a spray nozzle assembly supported within a wall of the riser for discharging atomized liquid hydrocarbon into the riser;
said spray nozzle assembly including a nozzle body which defines a cylindrical mixing zone and an elongated cylindrical barrel extension zone in downstream coaxial communication with the mixing zone,
a liquid hydrocarbon inlet supported by said nozzle body through which a pressurized liquid hydrocarbon stream is directed into said mixing zone,
an impingement pin supported by said nozzle body and extending into said mixing zone having an impingement surface in substantial alignment with the liquid hydrocarbon inlet against which a liquid hydrocarbon stream directed into said mixing zone from said liquid hydrocarbon inlet impinges and is transversely directed;
a steam inlet mounted in an upstream end of said nozzle body through which pressurized steam is directed into said mixing zone along a central axis of the mixing zone for atomizing the liquid hydrocarbon directed into said mixing zone,
a spray tip mounted at a downstream end of said barrel extension zone having a discharge orifice through which atomized liquid hydrocarbon is discharged in a predetermined spray pattern,
a cylindrical dispersion ring separate from said nozzle body fixedly supported to an inside cylindrical surface of said nozzle body downstream of said impingement pin which defines the end of said mixing zone and the beginning of said barrel extension zone, said dispersion ring defining an annular radial ledge having a radial depth of less than ⅛ the internal diameter of the mixing zone for directing a peripheral portion of the atomized liquid hydrocarbon radially inwardly for continued intermixing of the atomized liquid hydrocarbon as it proceeds through the barrel extension zone for discharge from the spray tip without substantially impeding the flow of atomized liquid hydrocarbon from the mixing zone to and through the barrel extension zone.

2. The catalytic cracking system of claim 1 in which said impingement pin is disposed about midway between the steam inlet and said dispersion ring.

3. The catalytic cracking system of claim 1 in which said dispersion ring has a radial depth of about 1/10 the internal diameter of the nozzle body.

4. The gas catalytic cracking system of claim 1 in which said barrel extension zone has an axial length between 2 and 10 times the axial length of the mixing zone.

5. The catalytic cracking system of claim 1 in which said nozzle body is a one piece section of steel pipe.

6. The catalytic cracking system of claim 5 in which said nozzle body is formed with a first opening adjacent the upstream end thereof that receives said liquid hydrocarbon inlet and a second opening in opposed relation to the first opening for receiving said impingement pin.

7. The catalytic cracking system of claim 1 in which said steam inlet is coupled to a supply of pressurized steam.

8. The catalytic cracking system of claim 1 in which said dispersion ring is positioned an axial distance (L) downstream of a center of the impingement pin less than the diameter of the mixing zone.

9. The catalytic cracking system of claim 8 in which said dispersion ring is positioned an axial distance (L) downstream of a center of the impingement pin a distance of about ¾ of the diameter of the mixing zone.

10. The catalytic cracking system of claim 1 in which said mixing zone and barrel extension zone are cylindrically configured, and said dispersion ring has an inside diameter less than the diameters of said mixing and barrel extension zones.

11. The catalytic cracking system, of claim 1 in which said mixing zone and barrel extension zone are cylindrically configured with similar inside diameters, and said dispersion ring has an inside diameter less than the inside diameters of said mixing and barrel extension zones.

Assignees

• Spraying Systems Co
• Technip Process Tech Inc

Inventors

• Lacroix Mark
• Gbordzoe Eusebius Anku
• Santner Chris Robert

Classifications

• B01J2208/00902

  Nozzle-type feeding elements · CPC title

• B05B1/044 Primary

  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

• B05B7/0483

  with gas and liquid jets intersecting in the mixing chamber · CPC title

• B01J8/24 Primary

  according to "fluidised-bed" technique (B01J8/20 takes precedence) · CPC title

• B05B7/0012

  Apparatus for achieving spraying before discharge from the apparatus · CPC title