Process for producing modified fly ash

Patent metadata

Field	Value
Publication number	US-10899663-B2
Application number	US-201816494521-A
Country	US
Kind code	B2
Filing date	Mar 19, 2018
Priority date	Mar 30, 2017
Publication date	Jan 26, 2021
Grant date	Jan 26, 2021

Abstract

A process for producing a modified fly ash comprising the steps of providing, as a raw material, the raw fly ash discharged from a pulverized coal combustion boiler; classifying the raw fly ash into a crude powder and a fine powder; removing the unburned carbon contained in the crude powder by heating the crude powder at a temperature in a range of 500 to 1000° C.; and mixing together the crude powder from which the unburned carbon has been removed and the fine powder to obtain a modified fly ash.

First claim

The invention claimed is:

1. A process for producing modified fly ash, comprising:
providing, as a raw material, a raw fly ash discharged from a pulverized coal combustion boiler;
classifying said raw fly ash into a crude powder and a fine powder;
removing an unburned carbon contained in said crude powder by heating said crude powder at a temperature in a range of 500 to 1000° C.; and
mixing together said crude powder from which the unburned carbon has been removed and said fine powder to obtain a modified fly ash;
and further comprising a step of measuring an amount of the unburned carbon contained in said raw fly ash prior to the step of classification,
wherein classification conditions are set in said step of classification depending upon an amount of the unburned carbon measured to be contained in said raw fly ash,
wherein the raw fly ash containing the unburned carbon in large amounts is classified in said step of classification by using a sieve having a small perforation size, and the raw fly ash containing the unburned carbon in small amounts is classified in said step of classification by using the sieve having a large perforation size, and
wherein in executing the classification in said step of classification, the raw fly ash is classified in said step of classification while setting the perforation size of the sieve that is used as described below depending on the amount of the unburned carbon that is measured

Content of the unburned carbon
Sieve perforation size

Less than 4% by mass
90 to 150
μm

Not less than 4% by mass
45 to 90
μm

but less than 8% by mass

Not less than 8% by mass
20 to 45
μm.

2. The process for producing the modified fly ash according to claim 1 , wherein a reference threshold content of the unburned carbon contained in the finally obtained modified fly ash is set to lie in a range of 1 to 4% by mass;
in said step of mixing, the ratio of mixing said fine powder and said crude powder is adjusted so that the amount of the unburned carbon contained in said modified fly ash obtained by mixing together said fine powder and said crude powder from which the unburned carbon has been removed, lies in a range of said reference threshold content ±0.5% by mass.

3. The process for producing the modified fly ash according to claim 1 , wherein,
a threshold value of not less than 6% by mass is set for the amount of the unburned carbon contained in said raw fly ash, and a reference threshold amount of the unburned carbon contained in said finally obtained modified fly ash is set to lie in a range of 1 to 4% by mass;
the raw fly ash containing the unburned carbon in an amount less than said threshold value is classified in said step of classification, said fine powder obtained in said step of classification is stored in a first silo, the crude powder obtained in said step of classification is introduced into the step of removing the unburned carbon and is stored in a second silo after the unburned carbon has been removed therefrom;
the raw fly ash containing the unburned carbon in an amount not less than said threshold value is not introduced into said step of classification but is introduced into said step of removing the unburned carbon to remove the unburned carbon therefrom, and the obtained fly ash from the unburned carbon has been removed is stored in the second silo like said crude powder; and
the fine powder stored in said first silo and the fly ash stored in said second silo and from which the unburned carbon has been removed are mixed together in said step of mixing so that the amount of the unburned carbon contained in said modified fly ash lies in a range of said reference threshold content ±0.5% by mass.

4. The production process according to claim 3 , further, including the step of measuring the amount of the unburned carbon contained in the fine powder stored in said first silo.

Assignees

• Tokuyama Corp

Inventors

• Omura Kohei
• Seki Takuya
• Kato Hiroyoshi

Classifications

• B09B3/40 Primary

  involving thermal treatment, e.g. evaporation (processes using mineral binders involving a melting or softening step B09B3/29; involving radiation B09B3/50) · CPC title

• C04B7/44 Primary

  Burning; Melting · CPC title

• Y02W30/91

  Use of waste materials as fillers for mortars or concrete · CPC title

• B09B2101/30

  Incineration ashes · CPC title

• C04B18/08

  Flue dust {, i.e. fly ash} · CPC title