Spray nozzle manifold

• US 8,444,061 B2
• Filed: 09/04/2008
• Issued: 05/21/2013
• Est. Priority Date: 09/04/2007
• Status: Active Grant

• Current Assignee: Air Products and Chemicals Incorporated (Linde Plc)
• Original Assignee: Shell Oil Company (Shell Plc)
• Inventors: Van Den Berg, Robert, Harteveld, Wouter Koen, Heinen, Hans Joachim, Von Kossak-Glowczewski, Thomas Paul
• Primary Examiner(s): Tran, Len
• Assistant Examiner(s): JONAITIS, JUSTIN M
• Application Number:
  US12/204,592
• Publication Number:
  US 20090121039A1
• Time in Patent Office: 1,720 Days
• Field of Search: 239104-123, 239418-4345, 239/290, 239/294, 239/416.5
• US Class Current: 239/105
• CPC Class Codes: B05B 12/18 using fluids, e.g. gas streams
• CPC Class Codes: B05B 12/36 Side shields, i.e. shields extending in a direction substantially parallel to the spray jet
• CPC Class Codes: B05B 15/55 using cleaning fluids
• CPC Class Codes: B05B 7/0466 with means for deflecting the central liquid flow towards the peripheral gas flow
• CPC Class Codes: B05B 7/0475 with means for deflecting the peripheral gas flow towards the central liquid flow B05B7/0458 takes precedence
• CPC Class Codes: F28C 3/08 with change of state, e.g. absorption, evaporation, condensation generating steam under pressure F22
• CPC Class Codes: Y02E 20/18 Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]

Abstract

A spray nozzle manifold comprising a first co-axial passage for supply of an atomization gas, a second co-axial passage present in said first passage for supply of a liquid, more than one laterally spaced nozzle for atomization and spraying liquid in a direction away from the longitudinal axis of the manifold attached to the first passage, said nozzles having an inlet for liquid fluidly connected to said second passage, an inlet for atomization gas fluidly connected to the first passage, a mixing chamber wherein atomization gas and liquid mix and an outlet for a mixture of atomization gas and liquid, wherein the nozzle has an opening for discharge of atomization gas which opening is in fluid communication with the first passage at a position upstream of the mixing chamber and wherein a shield is fixed to the first passage surrounding the nozzle.

Claims

1. A spray nozzle manifold comprising a first co-axial passage for supply of an atomisation gas, a second co-axial passage present in said first passage for supply of a liquid, more than one laterally spay nozzle for atomisation and spraying liquid in a direction away from the longitudinal axis of the manifold attached to the first passage, said laterally spaced nozzles run along one side of the first passage and a number of laterally spaced openings are present in the wall of the first passage at its opposite end, said nozzles having an inlet for liquid fluidly connected to said second passage, an inlet for atomisation gas fluidly connected to the first passage, a mixing chamber wherein atomisation gas and liquid mix and an outlet for a mixture of atomisation gas and liquid, wherein the nozzle has an opening for discharge of atomisation gas which said opening is in fluid communication with the first passage at a position upstream of the mixing chamber and wherein a shield is fixed to the first passage surrounding the nozzle.

2. A spray nozzle manifold according to claim 1, wherein the first and second passage are fluidly connected to conduits to supply atomisation gas and liquid respectively at one end of said passages and wherein at the other end of said passages a nozzle is present which has a spray direction, which is tilted with respect to the spray direction of the other nozzles.

3. A spray nozzle manifold according to claim 1, wherein the nozzle comprises a vertical and central supply passage for a liquid fluidly connected with the second co-axial passage, as present in a passage body, said passage body having outward and radial discharge openings at its lower end, said radial discharge openings exiting in the mixing chamber, said mixing chamber comprising an annular space fluidly connected to the first co-axial passage for atomisation gas and fluidly connected to a single outlet passage at the lower end of the nozzle, said outlet passage being defined by the inner wall of a nozzle body and wherein said outlet passage terminates at its lower end in a diverging outlet opening for a mixture of liquid and atomisation gas.

4. A spray nozzle manifold according to claim 1, wherein a blaster is present to continuously or intermittently or in any combination blast away any deposits, which may form on the upper side of a spray nozzle manifold.

5. An arrangement of spray nozzle manifolds, said spray nozzle manifolds comprise a first co-axial passage for supply of an atomisation gas, a second co-axial passage present in said first passage for supply of a liquid, more than one laterally spaced nozzle for atomisation and spraying liquid in a direction away from the longitudinal axis of the manifold attached to the first passage, said laterally spaced nozzles run along one side of the first passage and a number of laterally spaced openings are present in the wall of the first passage at its opposite end, said nozzles having an inlet for liquid fluidly connected to said second passage, an inlet for atomisation gas fluidly connected to the first passage, a mixing chamber wherein the nozzle has an opening for discharge of atomisation gas which said opening is in fluid communication with the first passage at a position upstream of the mixing chamber and wherein a shield is fixed to the first passage surrounding the nozzle,

wherein the majority of the nozzles are directed in substantially the same direction, wherein the manifolds are radially positioned in one horizontal circular plane and wherein conduits supplying atomisation gas and liquid to the manifold are present along its circumference and wherein the ends of the manifold at the center of the circle are spaced away from each other.

6. An arrangement according to claim 5, wherein the first and second passage of the spray nozzle manifolds are fluidly connected to conduits to supply atomisation gas and liquid respectively at one end of said passages and wherein at the other end of said passages a nozzle is present which has a spray direction, which is tilted with respect to the spray direction of the other nozzles.

7. An arrangement according to claim 5, wherein the nozzle comprises a vertical and central supply passage for a liquid fluidly connected with the second co-axial passage, as present in a passage body, said passage body having outward and radial discharge openings at its lower end, said radial discharge openings exiting in the mixing chamber, said mixing chamber comprising an annular space fluidly connected to the first co-axial passage for atomisation gas and fluidly connected to a single outlet passage at the lower end of the nozzle, said outlet passage being defined by the inner wall of a nozzle body and wherein said outlet passage terminates at its lower end in a diverging outlet opening for a mixture of liquid and atomisation gas.

8. An arrangement according to claim 5, wherein blasters are present to continuously or intermittently or in any combination blast away any deposits, which may form on the upper side of a spray nozzle manifold.

9. A process to quench a flow of hot gas by injecting a spray of liquid droplets present in an atomisation gas into the flow of hot gas using an arrangement according to claim 5, wherein the hot gas is passed in a direction perpendicular to the circular plane and wherein the spray is injected in the same direction as the flow direction of the hot gas.

10. A process according to claim 9, wherein the hot gas is an ash containing gaseous mixture of carbon monoxide and hydrogen having a pressure of between 2 and 10 MPa and an initial temperature of between 500 and 900°

C., the liquid comprises water and wherein the temperature of the gas after the quenching step is between 200 and 600°

C. and wherein an atomising gas as supplied in the first co-axial passage has a pressure of between 0.5 and 2 MPa above the pressure of the gaseous mixture of carbon monoxide and hydrogen.

11. A process according to claim 10, wherein the initial temperature is between 600 and 800°

C. and wherein the temperature of the gas after the quenching step is between 300 and 500°

C.