Usage of fly ash from flue gas desulfurization to make compositions for building

Information

  • Patent Grant
  • 10640421
  • Patent Number
    10,640,421
  • Date Filed
    Thursday, August 3, 2017
    7 years ago
  • Date Issued
    Tuesday, May 5, 2020
    4 years ago
Abstract
Composition for building materials comprises of fly ash from flue gas desulfurization. The fly ash (β CaSO4 anhydrite), obtained from circulating fluidized bed flue gas desulfurization, is mixed with binder reactants at a ratio of 9:1. It's mainly used for non-structural cement mortar, bricks for paving walkways, brick wall decors, fire-resistant walls for interior partitions, plasterboards and so on. The binder reactants compose of 70% CaSO4.½H2O, 10% Na2SO4, 10% CaO, 5% NaOH, 0˜5% cement and 0˜5% starch. When the binder reactants are mixed with fly ash and water (30% to 40% of the above total weight), the hydration process of CaSO4 anhydrite is accelerated.
Description
CROSS-REFERENCE TO RELATED APPLICATIONS

This application claims the benefit of Taiwan Invention Patent Application No. TW 105124724 filed Aug. 4, 2016, which is hereby incorporated by reference.


BACKGROUND OF THE INVENTION
(1) Field of Invention

This invention relates to a reuse of abandoned fly ash, specifically focusing on fly ash from flue gas desulfurization to make compositions for building materials.


(2) Description of Related Art

Formosa Plastics Corporation (FPC) Sixth Naphtha Cracker Complex uses Circulating Fluidized Bed (CFB) Boiler from ALSTOM. Petroleum coke and limestone are mixed with a ratio of 2:1 and sent inside the boiler, undergoing high temperature oxidative combustion to generate steam and drive turbines. Hundreds of tons of by-product fly ash, composed of pulverized β CaSO4 anhydrite, granular β CaSO4 anhydrite and hydrated CaSO4, are produced daily and have not been effectively dealt with. Since the fly ash is produced at temperatures above 850° C.˜900° C., it contains primarily the form β CaSO4 anhydrite and doesn't easily undergo hydration with water under standard atmospheric pressure and temperature. As this property influences the usability of fly ash, the inventors continues to research and develop products that meet environmentally friendly standards.




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BRIEF SUMMARY OF THE INVENTION

The goal of this invention is to use fly ash from flue gas desulfurization, along with binder reactants and known quantity of water, to make compositions for building materials that have a comparable strength to that cement.


To accomplish this goal, this invention involves mixing fly ash (β CaSO4), obtained from circulating fluidized bed flue gas desulfurization with binder reactants at a ratio of 9:1. It's mainly used for non-structural cement mortar, bricks for paving walkways, brick wall decors, fire-resistant walls for interior partitions, plasterboards and so on. The binder reactants compose of 70% CaSO4.½H2O, 10% Na2SO4, 10% CaO, 5% NaOH, 0˜5% cement and 0˜5% starch. When the binder reactants are mixed with fly ash and water (30% to 40% of the above total weight), the hydration process of CaSO4 anhydrite is accelerated.







DETAILED DESCRIPTION OF THE INVENTION

[Simple Illustration]


To help the review committee better understand the technology, means and effects by which set goals are accomplished, the following case is shown in sequence and illustrated in details to provide deeper perception of the goals, features and advantages of this invention.


[The Way of Implement]


This invention involves mixing fly ash (β CaSO4 anhydrite), obtained from circulating fluidized bed flue gas desulfurization, with binder reactants at a ratio of 9:1. It's mainly used for non-structural cement mortar, bricks for paving walkways, brick wall decors, fire-resistant walls for interior partitions, plasterboards and so on. The binder reactants compose of 70% CaSO4.½H2O, 10% Na2SO4, 10% CaO, 5% NaOH, 0˜5% cement and 0˜5% starch. When the binder reactants are mixed with fly ash and water (30% to 40% of the above total weight), the hydration process of CaSO4 anhydrite is accelerated.




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The products are showed in the following:














Category
Raw Material
Strength (SGS)







Non-structural Cement
CaSO4 anhydrite 43%
2500~3000 Lb/in2


Mortar
granular CaSO4 57%



Bricks for Walkways
CaSO4 anhydrite 43%
2500~3000 Lb/in2



granular CaSO4 57%



Wall decor and plasterboard
CaSO4 anhydrite 100%
1500~1700 Lb/in2


Fire-resistant walls for
CaSO4 anhydrite 43%
1000 Lb/in2


interior partitions and
Hydrated CaSO4 57%



plasterboards











The above products satisfy the demands and standards of normal building materials. Only 10% binder reactant by weight of the above by-products is needed to produce building materials that meet standard construction strength requirement.


From the above procedures, it can be seen that the binder reactant of this invention can accelerate the hydration reaction of the fly ash, which provides a great variety of applications, in contrast to prior art.


The invention has been described in detail with particular reference to certain preferred embodiments thereof and it is intended that the specification and examples be exemplary only. It should be appreciated that variations and modifications can be effected within the spirit and scope of the invention.

Claims
  • 1. The binder reactant for reusing a calcium sulfate compound, comprising: about 70% CaSO4.½H2O, about 10% Na2SO4, about 10% CaO, about 5% NaOH, about 0-5% cement, and about 0-5% starch, wherein said binder reactant is mixed with said calcium sulfate compound for reusing said calcium sulfate compound.
  • 2. The binder reactant of claim 1, wherein the calcium sulfate compound is characterized by a fly ash, wherein said fly ash, obtained from circulating fluidized bed flue gas desulfurization, contains substantially β CaSO4 anhydrite, and wherein said fly ash is mixed with said binder reactant at a ratio about 9:1, thereby a mixture is formed.
  • 3. The binder reactant of claim 2, wherein said mixture is mixed with water with weighted percentage essential between 30% and 40%, whereby a hydration process is accelerated.
Priority Claims (1)
Number Date Country Kind
105124724 A Aug 2016 TW national
US Referenced Citations (4)
Number Name Date Kind
5488991 Cowan Feb 1996 A
7247284 Seck Jul 2007 B1
20110083556 Duesel, Jr. Apr 2011 A1
20140272376 Aldabaibeh Sep 2014 A1
Foreign Referenced Citations (7)
Number Date Country
101475326 Jul 2009 CN
102432073 May 2012 CN
105117080 Dec 2015 CN
106145725 Nov 2016 CN
108117080 Jun 2018 CN
62254824 Nov 1987 JP
63296827 Dec 1988 JP
Related Publications (1)
Number Date Country
20180037499 A1 Feb 2018 US