Addition of organophosphonates for size control of wet calcium-based FGD byproduct solids under forced oxidation conditions

• US 5,246,677 A
• Filed: 05/07/1991
• Issued: 09/21/1993
• Est. Priority Date: 05/07/1991
• Status: Expired due to Fees

• Current Assignee: Electronics and Telecommunications Research Institute
• Original Assignee: Electric Power Research Institute
• Inventors: Meserole, Frank B., Moser, Robert E., Maller, Gordon
• Primary Examiner(s): HELLER, GREGORY
• Application Number:
  US07/696,768
• Time in Patent Office: 868 Days
• Field of Search: 423/242 A, 423/243, 423/555, 423/242 R, 423/242.2, 423/242.7, 423/242.3, 423/243.08, 423/243.09
• US Class Current: 423/243.08
• CPC Class Codes: B01D 53/501 by treating the gases with a solution or a suspension of an alkali or earth-alkali or ammonium compound
• CPC Class Codes: B01D 53/73 After-treatment of removed components
• CPC Class Codes: C01F 11/464 Sulfates of Ca from gases containing sulfur oxides
• CPC Class Codes: C01P 2004/10 extending in one dimension, e.g. needle-like
• CPC Class Codes: C01P 2004/61 Micrometer sized, i.e. from 1-100 micrometer

Abstract

A process for producing large, regularly-shaped crystalline gypsum solids in a wet calcium-based flue gas desulfurization system is provided. A chemical crystal modifier, preferably an organophosphonate, is added to the gypsum-containing solids slurry produced by the FGD process under forced oxidation conditions at an addition level which promotes the formation of large, regular gypsum crystals that are easily dewatered. The dewatered gypsum is useful in producing gypsum-based building products and the like.

Claims

1. A method for modifying calcium sulfate crystals produced as byproduct solids in a wet calcium-based flue gas desulfurization process conducted under forced oxidation conditions favoring the production of calcium sulfate over calcium sulfite solids to produce substantially regularly shaped calcium sulfate crystals greater than 200 microns in size, consisting essentially of contacting a sulfur oxide-containing gas with calcium to produce calcium sulfate solids;

adding 5-200 ppm of a crystal growth habit modifier selected from the group consisting of polyphosphates, organic phosphates and organophosphonates to said calcium sulfate solids; and

recovering substantially regularly shaped calcium sulfate crystals greater than 200 microns in size.

2. The method for modifying calcium sulfate flue gas desulfurization byproduct solids crystals described in claim 1, wherein said crystal growth habit modifier is an organophosphonate, and less than 100 ppm of said organophosphonate is added to said calcium sulfate byproduct solids.

3. The method for modifying calcium sulfate flue gas desulfurization byproduct solids crystals described in claim 2, wherein said organophosphonate is selected from the group consisting of aminotri(methylene phosphonic acid), hydroxyethylidene-1, 1-diphosphonic acid, hexamethylenediamine tetra(methylene phosphonic acid) and diethylenetriamine penta(methylene phosphonic acid).

4. The method for modifying calcium sulfate byproduct solids crystals described in claim 1, wherein 5-20 ppm of a polyphosphate or an organophosphonate is added to said byproduct solids.

5. The method for modifying calcium sulfate flue gas desulfurization byproduct solids crystals described in claim 3, wherein 20 ppm aminotri(methylene phosphonic acid) is added to said calcium sulfate byproduct solids.

6. A method for modifying gypsum crystals produced as byproduct solids in a flue gas desulfurization process conducted under conditions producing the substantially complete oxidation of calcium sulfite to calcium sulfate to form substantially regularly shaped gypsum crystals greater than 200 microns in size, consisting essentially of contacting a sulfur oxide-containing gas with calcium to produce gypsum solids;

adding 5-100 ppm of an organophosphonate selected from the group consisting of aminotri (methylene phosphonic acid), hydroxyethylidene-1, 1-diphosphonic acid, hexamethylenediamine tetra(methylene phosphonic acid), and diethylenetriamine penta (methylene phosphonic acid) to said gypsum solids; and

recovering substantially regularly shaped gypsum solids greater than 200 microns in size.

7. The method for modifying gypsum crystals described in claim 6, wherein 20 ppm of aminotri (methylene phosphonic acid) is added to said gypsum solids.

8. The method for modifying gypsum crystals described in claim 6, wherein 5-10 ppm of said organophosphonate is added to said gypsum solids.

9. The method for modifying gypsum crystals described in claim 6, wherein said regularly-shaped crystals are about 400 to 500 microns in size and exhibit a columnar and agglomerate crystal habit.

10. The method for modifying gypsum crystals described in claim 6, wherein the flue gas desulfurization process includes a particle grinding step to replenish removed crystals and to provide more precise control of crystal size.