Apparatus and Process For Calcining Feed Material

Patent metadata

Field	Value
Publication number	US-2024190762-A1
Application number	US-202218079203-A
Country	US
Kind code	A1
Filing date	Dec 12, 2022
Priority date	Dec 12, 2022
Publication date	Jun 13, 2024
Grant date	—

Abstract

A process for calcining a feed material can include passing a solid particulate material through a burner or adjacent a burner for being pass through a flame formed by the burner to facilitate calcination of the material. The material can be emitted from the flame of the burner within a calciner for passing through a body of the calciner to an outlet for further calcination of the material so the material has a pre-selected residence time as it is passed through the flame and calciner to an outlet. The residence time can be 20 seconds to 30 seconds, 1-3 minutes, less than 5 minutes in some embodiments. Some embodiments can facilitate calcination of a CaCO 3 material so the calcined solid material output from a calciner is comprised of Ca(OH) 2 (e.g. is mostly Ca(OH) 2 , is over 90 weight percent Ca(OH) 2 , etc.).

First claim

What is claimed is:

1 . A process for calcining a feed material comprising:
feeding solid particulate material to a flame formed in a calciner so the solid particulate material passes through the flame as the solid particulate material moves through the calciner to an outlet of the calciner.

2 . The process of claim 1 , wherein the solid particulate material has a residence time for calcination of between 5 minutes and 5 seconds, between 3 minutes and 5 seconds, between 10 seconds and 30 seconds, or between 5 seconds and 1 minute.

3 . The process of claim 1 , wherein the feeding of the solid particulate material to the flame comprises:
passing the solid particulate material into a burner for feeding into the calciner via the burner; and/or passing the solid particulate material into the calciner adjacent to the flame so that the solid particulate material passes through the flame.

4 . The process of claim 1 , comprising:
feeding a fuel and at least one flow of oxidant to the burner for formation of the flame in the calciner.

5 . The process of claim 4 , wherein the flame facilitates calcination of the solid particulate material at a pre-selected calcination temperature range of between 815° C. and 2,205° C., between 815° C. and 1,370° C., between 815° C. and 1,650° C., between 925° C. and 1,650° C. or between 925° C. and 1,370° C.

6 . The process of claim 1 , wherein the calcined material comprises between 70 weight percent (wt %) Ca(OH) 2 and 100 wt % Ca(OH) 2 , between 80 wt % Ca(OH) 2 and 100 wt % Ca(OH) 2 , or between 90 wt % Ca(OH) 2 and 100 wt % Ca(OH) 2 .

7 . The process of claim 1 , wherein the feed material is comprised of at least 70 weight percent carbonate material and no more than 30 weigh percent impurities.

8 . The process of claim 1 , wherein the feed material has average particle size of 50 micrometers to 2,000 micrometers and a maximum particle size that is not greater than 5,000 micrometers.

9 . The process of claim 1 , comprising:
filtering a flow output from the outlet of the calciner to separate the solid particulate material from combustion gas formed from formation of the flame, the solid particulate material separated from the combustion gas being calcined material.

10 . The process of claim 1 , comprising:
passing the solid particulate material through at least one dryer prior to the feeding the solid particulate material to the flame within the calciner; and passing the combustion gas to the dryer to dry the solid particulate material within the dyer prior to the combustion gas being passed to a carbon capture system to capture carbon dioxide from the combustion gas.

11 . The process of claim 1 , comprising:
filtering a flow output from the outlet of the calciner to separate the solid particulate material from combustion gas formed from formation of the flame, the solid particulate material separated from the combustion gas being calcined material; and cooling the flow output from the outlet of the calciner prior to the filtering.

12 . The process of claim 11 , wherein a cooling medium for the cooling of the flow output from the outlet of the calciner prior to the filtering comprises carbon dioxide.

13 . An apparatus for calcining a feed material comprising:
a calciner; at least one burner positioned adjacent to an inlet portion of the calciner such that solid feed material fed into the calciner is passable through at least one flame formed in the calciner via the burner for calcination of the solid feed material, the calciner and the at least one burner arranged and positioned so that the solid feed material is passable through the at least one flame to an outlet of the calciner for calcination of the solid feed material.

14 . The apparatus of claim 13 , comprising:
at least one filter device connectable to the outlet of the calciner to receive the solid feed material and combustion gas from the outlet of the calciner to filter solid particulates of the solid feed material from the combustion gas.

15 . The apparatus of claim 13 , wherein the at least one burner and the calciner are arranged and configured so that the solid feed material has a residence time for calcination of between 5 minutes and 5 seconds, between 3 minutes and 5 seconds, between 10 seconds and 30 seconds, or between 5 seconds and 1 minute.

16 . The apparatus of claim 13 , wherein the at least one burner is connectable to a source of fuel, at least one source of an oxidizer, and at least one source of the solid feed material such that at least a portion of the solid feed material is feedable to the burner for being fed into the flame.

17 . The apparatus of claim 13 , wherein the calciner is connectable to at least one source of the solid feed material so that at least a portion of the solid feed material is feedable into the calciner for being passed into the flame for partial calcination in the flame in a first phase of calcination prior to being passed out of the flame and towards the outlet of the calciner for further calcination in a second phase of calcination.

18 . The apparatus of claim 13 , wherein the at least one burner and the calciner are arranged and configured so that the flame facilitates calcination of the solid feed material at a pre-selected calcination temperature range of between 815° C. and 2,205° C., between 815° C. and 1,370° C., between 815° C. and 1,650° C., between 925° C. and 1,650° C. or between 925° C. and 1,370° C.

19 . The apparatus of claim 13 , comprising:
a carbon capture system positioned downstream of the outlet of the calciner to capture carbon dioxide from the combustion gas output from the outlet of the calciner.

20 . A calcination system comprising:
a calciner having an outlet in communication with a chamber; at least one burner connected to the calciner to form at least one flame within the chamber for calcination at a pre-selected calcination temperature range of between 815° C. and 2,205° C.; at least one filter device connected to the outlet of the calciner to receive calcined material entrained within combustion gas from the calciner to separate the calcined material from the combustion gas; and a carbon capture system connected to the at least one filter device to receive the combustion gas for removal of moisture from the combustion gas and capturing of carbon dioxide from the combustion gas; and wherein a source of solid particulate feed material is connectable to the at least one burner and/or the calciner to feed the solid particulate feed material into the at least one flame for a first phase of calcination of the solid particulate feed material, the calciner sized and configured so that the solid particulate feed material passes from the flame to the outlet within the chamber of the calciner for a second phase of calcination of the feed material so that a pre-selected residence time of the solid particulate feed material for calcination to form the calcined material is greater than 5 seconds and is less than or equal to 5 minutes.

Assignees

• Air Prod & Chem

Inventors

• Mocsari Jeffrey Carl
• Makwana Anandkumar

Classifications

• F27M2003/03

  Calcining · CPC title

• F27B15/16

  Arrangements of cooling devices · CPC title

• F27B15/12

  Arrangements of dust collectors · CPC title

• F23D14/22

  with separate air and gas feed ducts, e.g. with ducts running parallel or crossing each other · 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