Method for operating cement plant

Patent metadata

Field	Value
Publication number	US-10131576-B2
Application number	US-201414916465-A
Country	US
Kind code	B2
Filing date	Jun 30, 2014
Priority date	Sep 30, 2013
Publication date	Nov 20, 2018
Grant date	Nov 20, 2018

Abstract

There is provided a method for operating a cement plant capable of simultaneously optimizing both combustion in a calciner and a heat consumption rate. The method for operating a cement plant includes: feeding first fuel to a calciner; feeding second fuel for maintaining the inside at a burning temperature to a cement kiln along with combustion primary air, and introducing air for cooling cement clinker to a cooler; and feeding a part of the air as secondary air to the cement kiln, feeding as tertiary air to the calciner, and discharging the rest of the air from the cooler, wherein relation between a first oxygen concentration at an exhaust gas outlet of the calciner and a heat consumption rate determined by the first fuel and the second fuel, and relation between a second oxygen concentration at an exhaust gas outlet of the preheater and the heat consumption rate are beforehand obtained, and amounts of the secondary air and the tertiary air are adjusted such that both the first oxygen concentration and the second oxygen concentration fall within a range including values of the oxygen concentrations at which the heat consumption rate becomes at its minimum.

First claim

The invention claimed is:

1. A method for operating a cement plant which includes a preheater that preheats a raw material, a calciner that calcines at least part of the raw material picked out of the preheater, a cement kiln that burns the raw material passed through the preheater and the calciner into cement clinker, and a cooler that cools the cement clinker discharged from the cement kiln, the method comprising:
feeding first fuel in an amount required for calcining the introduced raw material to the calciner;
feeding to the cement kiln, along with combustion primary air, second fuel in an amount required for maintaining an inside of the cement kiln at a burning temperature, and introducing air in a certain amount for cooling the cement clinker to the cooler; and
feeding a part of the air as secondary air for assisting combustion of the second fuel to the cement kiln, feeding another part of the air as tertiary air for combustion of the first fuel to the calciner, and discharging the rest of the air from the cooler, wherein
relation between a first oxygen concentration at an exhaust gas outlet of the calciner and a heat consumption rate determined by the first fuel and the second fuel, and relation between a second oxygen concentration at an exhaust gas outlet of the preheater and the heat consumption rate are beforehand calculated and obtained, the first oxygen concentration at the exhaust gas outlet of the calciner being measured before the second oxygen concentration at the exhaust gas outlet of the preheater, and
flow rates of the tertiary air and exhaust from the cooler are adjusted such that both the first oxygen concentration and the second oxygen concentration fall within a range including values of the oxygen concentrations at which the heat consumption rate becomes at its minimum, whereby both the combustion at the calciner and the heat consumption rate are simultaneously optimized.

2. The method for operating the cement plant according to claim 1 , wherein the first fuel is fed to the calciner at a certain feed amount, and the second fuel is adjusted at a feed amount required for maintaining it at the burning temperature and fed to the cement kiln.

3. The method according to claim 1 , wherein the oxygen concentration in the exhaust gas at the calciner outlet is adjusted to be approximately 2% to 4%, and the oxygen concentration in the preheater exhaust gas is adjusted to be approximately 0.5% to 2%.

4. The method according to claim 1 , wherein the oxygen concentration measurement in the exhaust gas outlet of the calciner is taken before the exhaust gas of the calciner is mixed with the exhaust gas of the cement kiln.

Assignees

• Mitsubishi Materials Corp

Inventors

• Komatsu Takuya
• Takayama Yoshinori

Classifications

• F23N2223/40

  Simulation · CPC title

• C04B7/006

  Cement-clinker used in the unground state in mortar - or concrete compositions · CPC title

• F27D99/0033

  using burners · CPC title

• C04B7/434 Primary

  Preheating with addition of fuel, e.g. calcining · CPC title

• C04B7/4407

  Treatment or selection of the fuel therefor, e.g. use of hazardous waste as secondary fuel (fuels in general C10L); Use of particular energy sources, e.g. waste hot gases from other processes · CPC title