Process for the production of highly permeable calcined diatomites with low cristobalite content and resultant calcined diatomaceous filtration agents

• US 5,179,062 A
• Filed: 06/07/1991
• Issued: 01/12/1993
• Est. Priority Date: 06/20/1990
• Status: Expired due to Term

• Current Assignee: CEC Bank SA
• Original Assignee: CEC Bank SA
• Inventors: Dufour, Pascal
• Primary Examiner(s): MCFARLANE, ANTHONY R
• Application Number:
  US07/712,069
• Time in Patent Office: 585 Days
• Field of Search: 502/412, 55/523, 423/326
• US Class Current: 502/412
• CPC Class Codes: B01J 20/14 Diatomaceous earth

Abstract

A process for the production of calcined diatomaceous filtration agents having a cristobalite content lower than 1% and a 50-μm screen retention rate lower than 5% by rapid calcination of diatomites, comprising injecting the diatomite into a high-temperature gaseous stream and during its residence in the gaseous stream maintaining the diatomite between about 1250° and 850° C. for a period of time between several tens of milliseconds and several seconds, and calcined diatomaceous filtration agents having a permeability between 0.06 and 0.4 darcy and a cristobalite content lower than 1%.

Claims

1. A process for the production of calcined diatomaceous filtration agents having a cristobalite content lower than 1% and a 50-μ

m screen retention rate lower than 5% by rapid calcination of diatomites, comprising injecting the diatomite into a high-temperature gaseous stream and during its residence in the gaseous stream maintaining the diatomite between about 1250° and

850°

C. for a period of time between several tens of milliseconds and several seconds.

2. The process of claim 1 wherein said high-temperature gaseous stream injected with said diatomite also supports a material in levitation.

3. The process of claim 2 wherein said high-temperature gaseous stream is in a furnace in which said gaseous stream has an ascending helicoidal path and in which said levitating material is not transported in an ascending helicoidal path by said gas stream and remains in levitation in an annular zone.

4. The process of claim 3, wherein said diatomite is injected into said gaseous stream below said annular zone of said levitating material.

5. The process of claim 4 wherein the residence time of the diatomite in the part of said gaseous stream supporting said material in levitation is between several tens of milliseconds and several seconds.

6. The process of any one of claims 2 to 5, wherein said levitating material is composed of refractory spheres.

7. The process of any one of claims 1 to 5, wherein there is no subsequent grinding of said filtration agents to obtain a 50-μ

m screen retention rate lower than 5%.

8. The process of any one of claims 1 to 5, wherein said diatomites injected into said gaseous stream have a level of impurities higher than 0.05%, which impurities consist of alkali metal or alkaline-earth metal salts or oxides, of aluminum and iron.

9. The process of any one of claims 1 to 5, wherein the gas in said gaseous stream is air or flue gas containing oxygen.

10. A calcined diatomaceous filtration agent having a permeability between 0.06 and 0.4 darcy and a cristobalite content lower than 1%.