# US 4,395,223 A · Multi-stage combustion method for inhibiting formation of nitrogen oxides

> Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt

- Number: US 4,395,223 A
- Document ID: US4395223A
- Status: Granted
- Kind: A
- Application number: 06/221,825
- Filed: 1980-12-31
- Granted: 1983-07-26
- Earliest claimed: 1978-06-09
- Assignees: Hitachi Shipbuilding & Engineering Co., Ltd.
- Inventors: Noboru Okigami; Hiroshi Hayasaka; Yoshitoshi Sekiguchi; Harushige Tamura
- Web page: https://patentgrep.com/patent/US4395223A

## CPC

- F23C 6/047: {with fuel supply in stages}
- F23C 2201/30: Staged fuel supply
- F23C: METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN {A CARRIER GAS OR} AIR (burners F23D)

## Abstract

A method comprising injecting a primary fuel and air into a furnace to burn the fuel and form a first-stage combustion zone, the fuel being diluted with surrounding combustion gas and the air being supplied at a rate in excess of the stoichiometric rate required for the combustion of the fuel, and injecting a secondary fuel into the furnace around or downstream of the first-stage zone at a range approximately equal to the stoichiometric rate required for the consumption of the excess oxygen resulting from the combustion in the first-stage zone the fuel being diluted with surrounding combustion gas and to form a second-stage combustion zone around or downstream of the first-stage zone.

## Claims

### Claim 1

A multi-stage combustion method for inhibiting the formation of nitrogen oxides comprising injecting a primary fuel and primary air into a furnace to burn the fuel and form a first-stage combustion zone, the air being supplied at a rate in excess of the stoichiometric rate required for the combustion of the fuel, injecting only a secondary fuel in the absence of air into the furnace in the vicinity of the first-stage combustion zone at a rate in excess of the stoichiometric rate required for the consumption of the excess oxygen resulting from the combustion in the first-stage zone to form a second-stage combustion in the vicinity of the first-stage zone, the secondary fuel being supplied at the ratio of secondary fuel supply to total fuel supply of 0.2 to 0.5, the heat produced therein being absorbed by heat absorbing means provided in the wall of the furnace, and supplying secondary air downstream of the second-stage zone, at a rate not less than the stoichiometric rate required for the oxidation of the unburned components resulting from the combustion in the second-stage zone to oxidize the unburned components and form a third-stage combustion zone downstream from the second-stage zone.

### Claim 2 (depends on 1)

A method as defined in claim 1 wherein the secondary fuel is injected around the first-stage zone.

### Claim 3 (depends on 1)

A method as defined in claim 1 wherein the secondary fuel is injected toward a location downstream of the combustion gas of the first-stage zone.

### Claim 4 (depends on 1)

A method as defined in claim 1 wherein the secondary air is supplied when the ratio of air actually provided to air stoichiometrically required for combustion in the second-stage combustion zone is not higher than 1.15.

### Claim 5 (depends on 1)

A method as defined in claim 1 wherein the unburned components are oxidized at a temperature of 800.degree. to 1,000.degree. C.

### Claim 6 (depends on 1)

A method as defined in claim 1 wherein the primary air is supplied at a rate equal to the stoichiometric rate required for the combustion of the whole amount of fuel supplied to the furnace.