Feed nozzle assembly

Patent metadata

Field	Value
Publication number	US-9873096-B2
Application number	US-201013519140-A
Country	US
Kind code	B2
Filing date	Dec 3, 2010
Priority date	Dec 29, 2009
Publication date	Jan 23, 2018
Grant date	Jan 23, 2018

Abstract

The present subject matter relates to a feed nozzle assembly 100 for atomizing a heavy hydrocarbon feed by mixing the hydrocarbon feed with a diluent and an atomizing media. The feed nozzle assembly 100 includes at least one primary mixing chambers 101 for receiving the liquid hydrocarbon feed and the diluent to create a primary mixture. The primary mixture is than forwarded to a secondary mixing chamber 102 . The secondary mixing chamber extends to a tertiary mixing chamber 103 . A steam inlet 110 is provided to inject streams of steam to the secondary mixing chamber 102 and to the tertiary mixing chamber 103 through a first opening and a second opening, respectively, located within the steam inlet 110.

First claim

We claim:

1. A feed nozzle assembly comprising:
at least one primary mixing chamber to receive a liquid hydrocarbon and a diluent to produce a primary mixture;
a secondary mixing chamber flow connected to the primary mixing chamber to receive the primary mixture;
a tertiary mixing chamber forming part of the feed nozzle assembly and being flow connected to the secondary mixing chamber; and
a steam inlet that includes:
a first opening located at about one end of the secondary mixing chamber to inject first streams of steam into the secondary mixing chamber;
a second opening formed by a cylindrical member coupled to the steam inlet, said second opening being located at about the tertiary mixing chamber to inject second streams of steam into the tertiary mixing chamber; and
a perforated plate disposed in the secondary mixing chamber to receive steam, wherein:
the perforated plate further includes a first set of orifices and a second set of orifices, the first set of orifices and the second set of orifices dividing the steam into the first streams of steam and the second streams of steam, the first set of orifices acting as the first opening and injecting the first streams of steam into the secondary mixing chamber; and
the cylindrical member is coupled to the second set of orifices to receive the second streams of steam from the second set of orifices.

2. The feed nozzle assembly as claimed in claim 1 , wherein the cylindrical member comprises a sparging means to inject streams of steam into the tertiary mixing chamber.

3. A process for atomizing a liquid comprising:
injecting a quantity of a diluent and a liquid hydrocarbon feed into a primary mixing chamber to form a primary mixture;
introducing the primary mixture and a first streams of steam into a secondary mixing chamber forming part of a feed nozzle assembly to generate a secondary mixture wherein said first streams of steam is introduced in the secondary mixing chamber by means of a first opening provided in a steam inlet; and
directing the secondary mixture and a second streams of steam into a tertiary mixing chamber forming part of the feed nozzle assembly to generate a tertiary mixture wherein said second streams of steam is introduced in the tertiary mixing chamber by means of a second opening provided in the steam inlet.

4. The process as claimed in claim 3 , wherein the directing the secondary mixture comprises pressurizing the secondary mixture by the injecting of the streams of steam into the secondary mixing chamber to move the secondary mixture into the tertiary mixing chamber.

5. The process as claimed in claim 3 , further comprising:
dividing the tertiary mixture into a plurality of tertiary mixture streams; and
directing the plurality of tertiary mixture streams to a plurality of nozzle orifices provided in a nozzle tip region and stabilizing the plurality of tertiary mixture streams within the nozzle tip region to produce a spray comprising a plurality of droplets of the liquid hydrocarbon feed.

6. The process as claimed in claim 3 , wherein the plurality of droplets of the liquid hydrocarbon feed has a droplet size of about 85 microns to 200 microns.

Assignees

• De Bidyut
• Kasliwal Pankaj Kumar
• Bhattacharyya Debasis
• Krishnan Venkatachalam
• Rajagopal Santanam
• Indian Oil Corp Ltd

Inventors

• De Bidyut
• Kasliwal Pankaj Kumar
• Bhattacharyya Debasis
• Krishnan Venkatachalam
• Rajagopal Santanam

Classifications

• B01J4/002 Primary

  Nozzle-type elements (nozzle-type reactors B01J19/26) · CPC title

• B01F5/0256 Primary

  Operations & Transport · mapped topic

• B01F25/23 Primary

  Mixing by intersecting jets · CPC title