Oxy-calcination process

Patent metadata

Field	Value
Publication number	US-2020216357-A1
Application number	US-202016825735-A
Country	US
Kind code	A1
Filing date	Mar 20, 2020
Priority date	Dec 1, 2014
Publication date	Jul 9, 2020
Grant date	—

Abstract

Method and installation for calcining cement raw meal in a calciner whereby fuel and a calciner oxidant having an oxygen content of at least 30% vol are introduced into the calciner so as to generate either an oxidant-lean zone or a fuel-lean zone in the calciner located between the lowermost fuel inlet level and the lowermost oxidant inlet level of the calciner, between 50% and 100% by weight of the raw meal being supplied to the calciner upstream of and/or within the oxidant-lean, respectively the fuel-lean zone.

First claim

What is claimed is:

1 . A calcination installation for calcining cement raw meal, the installation comprising a calciner having a total calciner height and extending between a bottom end and a top end in a longitudinal direction, the calciner comprising:
a lowermost oxidant inlet level at which one or more first oxidant inlets are located, and optionally one or more second oxidant inlet levels located above the lowermost oxidant inlet level in the longitudinal direction and at which one or more second oxidant inlets are located, said first oxidant inlets and, if present, said second oxidant inlets being connected to a source of calciner oxidant having an oxygen content of at least 30% vol;
a lowermost fuel inlet level at which one or more first fuel inlets are located;
a flue gas outlet located at the top end of the calciner;
a flue-gas recycle inlet located at the bottom end of the calciner; and
one or more raw meal inlets, wherein:
the lowermost oxidant inlet level is located above the lowermost fuel inlet level at an oxygen-lean zone distance Do>0 from said lowermost oxidant inlet in the longitudinal direction, at least one raw meal inlet being located below or at the lowermost oxidant inlet level in the longitudinal direction, or
the lowermost fuel inlet level is located above the lowermost oxidant inlet level at a fuel-lean zone distance Df>0 from the lowermost oxidant inlet level in the longitudinal direction, at least one raw meal inlet being located below or at the lowermost fuel inlet level in the longitudinal direction.

2 . The calcination installation of claim 1 , whereby the an oxygen-lean zone distance Do, respectively the fuel-lean zone distance Df is between 1/10 and 4/10 of the total calciner height.

3 . The calcination installation of claim 1 , further comprising a raw meal preheater connected to the flue gas outlet and to the one or more raw meal inlets of the calciner.

4 . The calcination installation of claim 3 , further comprising a flue gas purification installation connected to the flue gas outlet of the calciner, said flue gas purification installation being adapted for removing components other than CO 2 from flue gas evacuated from the calciner via the flue gas outlet.

5 . A cement clinker production unit comprising a calcination installation of claim 1 and a clinkerisation kiln, the clinkerization kiln being connected to the calcination installation so that meal calcined in the calciner is transferred to the clinkerization kiln.

Assignees

• Air Liquide
• Lair Liquide Sa Pour Letude Et L?Exploitation Des Procedes Georges Claude

Inventors

• Panier Faustine
• Paubel Xavier
• Renna Carlo
• Gimenez Michel
• Paxton Colin
• Wassard Henrik
• Drivsholm Morten
• Tsiava Remi

Classifications

• Y02P40/18

  Carbon capture and storage [CCS] · CPC title

• F27D17/10

  Arrangements for using waste heat · CPC title

• C01B32/50

  Carbon dioxide · CPC title

• F27B7/20

  Details, accessories or equipment specially adapted for rotary-drum furnaces · CPC title

• C04B2/10

  Preheating, burning calcining or cooling (decarbonation during burning of cement raw materials C04B7/43; {obtaining CaO or MgO otherwise than by thermal decomposition of the corresponding carbonates C01F11/02, C01F5/02}) · CPC title