Oxycombustion Process for Vanadium Fuel

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Existing combustion processes for low-ranking hydrocarbon fuels containing vanadium and alkaline metals face challenges in achieving high-temperature operation without producing aggressive flue gases that corrode equipment and reduce energy recovery efficiency, as they result in high fly ash, incombustible residues, and toxic compounds.

Innovation Solution

An oxycombustion process using magnesium oxide and silico-aluminate additives in a refractory combustor operating at 1250-1450°C with oxygen and steam, transforming vanadium into non-aggressive orthovanadates and pyrovanadates, and removing alkaline metals as metavanadates, under pressurized conditions to minimize fly ash and corrosive species.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Temperature

If conventional combustion processes are used for low-ranking hydrocarbon fuels containing vanadium, then high-temperature operation can be achieved, but aggressive flue gases are produced that corrode equipment and reduce energy recovery efficiency

Engineering Contradiction:
Improvecombustion temperatureVSAvoidequipment corrosion
Core Design Contradiction:
TemperatureVSObject-affected harmful factors

Solution Approach 1:

Magnesium oxide acts as an intermediary substance that reacts with vanadium compounds in the flue gas to form magnesium orthovanadate, a non-corrosive compound. This mediator captures the harmful vanadium species before they can attack equipment surfaces, thereby protecting the system while maintaining high combustion temperatures

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The harmful vanadium compounds that cause corrosion are transformed into beneficial magnesium orthovanadate deposits on refractory surfaces. This conversion turns a harmful substance into a harmless or even protective layer, eliminating the corrosion problem while maintaining the combustion process

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

2Temperature

If conventional combustion processes are used for low-ranking hydrocarbon fuels containing vanadium, then high-temperature operation can be achieved, but high fly ash and incombustible residues are produced

Engineering Contradiction:
Improvecombustion temperatureVSAvoidfly ash content
Core Design Contradiction:
TemperatureVSLoss of substance

Solution Approach 1:

The combustion process parameters are changed by introducing magnesium oxide and operating under specific temperature and pressure conditions. These parameter changes alter the chemical reactions occurring during combustion, transforming the nature of residues from problematic fly ash to manageable solid deposits with different physical and chemical properties

Inventive Principle:
Principle #35Parameter changes

3Productivity

If conventional combustion processes are used for low-ranking hydrocarbon fuels containing vanadium, then energy production can be maintained, but frequent cleaning of equipment is required

Engineering Contradiction:
Improveenergy productionVSAvoidoperation duration without cleaning
Core Design Contradiction:
ProductivityVSDuration of action of moving object

Solution Approach 1:

The vanadium compounds that would normally cause corrosive damage and require frequent cleaning are converted into stable magnesium orthovanadate deposits on refractory surfaces. These deposits are non-corrosive and do not degrade equipment performance, thereby extending operation duration without cleaning while maintaining energy production

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

Solution Approach 2:

The refractory surfaces act as disposable or sacrificial elements that capture vanadium deposits. Instead of protecting expensive metal equipment from corrosion, the refractory material accepts the deposits, serving as a protective barrier that can be maintained more easily than critical equipment surfaces

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

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

The process achieves flue gases with low fly ash, negligible incombustible residues, and reduced vanadium and alkaline metal compounds, preventing equipment corrosion and maintaining energy recovery efficiency for extended plant operation without the need for frequent cleaning.

Implementation Method 1

transforming vanadium into non-aggressive orthovanadates and pyrovanadates

Methodology Applied
Scientific EffectChemical reaction: Chemical Bonding

Implementation Method 2

combustors working at temperatures in the range 1250°-1450°C

Methodology Applied
Scientific EffectCombustion: Combustion

Implementation Method 3

the hydrocarbon fraction being fed in admixture with water or steam

Methodology Applied
Scientific EffectMixing: Diffusion

Data Source

PatentEP2877560B1Combustion process for fuel containing vanadium compounds
Publication Date: 2018.03.14 ITEA SPA
  • EP2877560B1 patent drawing
  • EP2877560B1 patent drawing
  • EP2877560B1 patent drawing

AI summary

Oxycombustion process for producing energy wherein low ranking gaseous, liquid, solid, optionally solid melting hydrocarbon fractions are used as fuels, having a vanadium content in amounts by weight from 50 to 5,000 ppm or higher, and alkaline metals Ma in amounts from 20 to 10,000 ppm, wherein magnesium is added as oxide, or as a magnesium compound forming MgO in the combustion process, or mixtures thereof and a silico-aluminate wherein the molar ratio SiO2:Al2O3 ranges from 2:1 to 6:1; the combustor being refractored, isotherm or quasi-isotherm, flameless, working at temperatures in the range 1,250°-1,450°C and under pressurized conditions, wherein the oxidant being used in admixture with water or steam, the ratio by moles oxidant: (water/steam) being comprised between about 1:0.4 and about :3, or the oxidant is used in admixture with flue gases recycled from the flue gases outletting the energy recovery equipments, wherein the water/steam amount is higher than 30% by volume, optionally by adding water to the recycled flue gases, the molar ratio oxidant: (water/steam) in flue gases being comprised from about 1:0.4 to about 1:3; the hydrocarbon fraction being fed in admixture with water or steam, the amount of water/steam being at least 30% by weight with respect to the hydrocarbon fraction.