FGD Gypsum and Ash Conversion to Value-Added Materials

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Solution Overview

Problem

Current methods fail to effectively convert entire coal combustion products (CCP) inventories into value-added, marketable products with minimal waste, specifically focusing on the treatment of flue gas desulfurization (FGD) gypsum and ash.

Innovation Solution

The process involves reacting FGD gypsum with ammonium carbonate to produce ammonium sulfate and calcium carbonate, and a leach process followed by precipitation to extract metal hydroxides, which can be converted to oxides or carbonates, utilizing a series of reactors and pH adjustments for selective separation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Object-affected harmful factors

If FGD gypsum and ash are stored in piles and ponds, then they present environmental issues, but converting them to value-added products requires complex chemical processing

Engineering Contradiction:
Improveenvironmental issuesVSAvoidchemical processing complexity
Core Design Contradiction:
Object-affected harmful factorsVSDevice complexity

Solution Approach 1:

The patent divides the complex waste treatment process into distinct modular stages: (1) FGD gypsum conversion to ammonium sulfate and calcium carbonate, (2) ash leaching to extract metals, (3) selective precipitation of metal hydroxides at different pH levels, and (4) filtration and product recovery. Each stage handles specific components independently, making the overall complex process more manageable and scalable while eliminating environmental hazards.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent utilizes pH adjustment as a key parameter change to achieve selective separation. By controlling pH at different stages (acidic conditions for leaching, then progressively neutralizing to precipitate different metal hydroxides), the process transforms waste streams into valuable products. This parameter-based control simplifies the complexity by providing clear operational criteria for each processing stage.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If current methods convert only specific parts of CCPs, then certain products are produced, but significant portions remain as non-marketable waste

Engineering Contradiction:
Improveproduct conversion efficiencyVSAvoidnon-marketable waste
Core Design Contradiction:
ProductivityVSLoss of substance

Solution Approach 1:

The patent creates a universal treatment system that handles multiple waste streams (FGD gypsum and ash) simultaneously through integrated processing. The FGD gypsum conversion produces both ammonium sulfate (fertilizer) and calcium carbonate (filler), while ash processing recovers metals and produces construction materials. This multi-functional approach ensures near-complete conversion of all CCP components into marketable products, eliminating non-marketable waste.

Inventive Principle:
Principle #6Universality (Multi-functionality)

Solution Approach 2:

The patent transforms harmful waste materials into beneficial products: FGD gypsum becomes fertilizer and filler, ash becomes metal sources and construction materials, and sulfur compounds become valuable chemicals. This conversion paradigm turns the entire waste inventory into economic assets, achieving both environmental protection and resource recovery.

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

3Quantity of substance

If selective precipitation is used to extract metals from ash, then valuable metals are recovered, but multiple processing steps are required

Engineering Contradiction:
Improvemetal recoveryVSAvoidprocessing steps
Core Design Contradiction:
Quantity of substanceVSDevice complexity

Solution Approach 1:

The patent employs systematic pH adjustment as the primary mechanism for selective metal precipitation. By controlling pH levels sequentially (starting from acidic leachate and progressively neutralizing), different metal hydroxides precipitate at characteristic pH ranges, enabling selective recovery of valuable metals. This parameter-based approach consolidates multiple separation operations into a unified, controllable process flow.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent implements continuous processing where leachate flows through a series of precipitation tanks with progressively increasing pH, allowing continuous metal recovery without discrete batch operations. The process maintains continuous flow and separation actions, improving efficiency while managing complexity through standardized continuous processing units.

Inventive Principle:
Principle #20Continuity of useful action

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

This approach generates high-value products like ammonium sulfate and calcium carbonate from FGD gypsum, and valuable metals from ash, achieving near-zero waste and environmental benefits by recycling reagents and minimizing waste streams.

Implementation Method 1

reacting FGD gypsum with ammonium carbonate to produce ammonium sulfate and calcium carbonate

Methodology Applied
Scientific EffectChemical reaction: Chemical Bonding

Implementation Method 2

a leach process followed by precipitation to extract metal hydroxides

Methodology Applied
Scientific EffectLeaching: Liquid-Liquid Extraction

Implementation Method 3

precipitation to selectively precipitate components at predetermined pHs resulting in metal hydroxides

Methodology Applied
Scientific EffectPrecipitation: Precipitation

Data Source

PatentUS20210347648A1Systems and methods to treat flue gas desulfurization and metal-bearing waste streams to recover value-added materials
Publication Date: 2021.11.11 DAVY POWERSPORTS INC
  • US20210347648A1 patent drawing
  • US20210347648A1 patent drawing
  • US20210347648A1 patent drawing

AI summary

Disclosed herein are systems and methods from processing flue gas desulfurization (FGD) gypsum feedstock and ash feedstocks, either separately or together. FGD gypsum conversion comprises reacting FGD gypsum (e.g. calcium sulfate) feedstock, in either batch or continuous mode, with ammonium carbonate reagent to produce commercial products wherein the commercial products comprise ammonium sulfate and calcium carbonate. Ash conversion comprises a leach process followed by a precipitation process to selectively precipitate components at predetermined pHs resulting in metal hydroxides which may be optionally converted to oxides or carbonates. The processes may be controlled by use of one or more processors.