Upstream Catalytic NO Oxidation for Cryogenic Gas Purification

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Solution Overview

Problem

Current methods for purifying gas streams containing nitrogen monoxide (NO) and nitrogen oxides (NOx) are inefficient in converting NO to a more oxidized form (NOx) upstream, leading to incomplete NOx removal and potential corrosion issues due to acid generation in downstream processes, especially under varying conditions like compression.

Innovation Solution

A device comprising a catalytic bed, preferably sulfur-doped activated carbon or alumina, located upstream of a cryogenic separation unit, converts at least 60% of NO to NOx, with a conversion rate of 80-100%, effectively addressing the incomplete NOx removal and acid generation issues by advancing the NO to NOx conversion before the reduction unit.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If conventional purification methods (low-pressure washing, water washing, cryogenic separation) are used without upstream NO conversion, then the process is simpler and investment cost is lower, but NOx removal efficiency is insufficient and acid corrosion problems occur downstream

Engineering Contradiction:
ImproveNOx removal efficiencyVSAvoidprocess complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The patent applies preliminary action by installing a catalytic converter upstream of the purification unit to convert NO to NO2 before the gas enters the washing or cryogenic separation stage. This preliminary oxidation step ensures that nitrogen oxides are in a form that can be more effectively removed by downstream purification processes, thereby improving overall NOx removal efficiency without significantly complicating the process.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The catalytic converter acts as an intermediary device between the gas stream and the purification unit. It mediates the chemical transformation of NO to NO2, creating a more favorable condition for subsequent purification. This intermediary step resolves the contradiction by enabling efficient NOx removal while maintaining a relatively simple overall process structure.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Object-affected harmful factors

If NO is not converted upstream, then the process operates at lower cost, but acid condensates are generated during compression and refrigeration causing corrosion

Engineering Contradiction:
Improvecorrosion resistanceVSAvoidinvestment cost
Core Design Contradiction:
Object-affected harmful factorsVSEase of manufacture

Solution Approach 1:

The catalytic converter performs preliminary oxidation of NO to NO2 before compression and refrigeration stages. This preliminary action prevents the formation of acid condensates during downstream processing by ensuring nitrogen oxides are in a less reactive form, thereby protecting equipment from corrosion while incurring only moderate additional investment in the catalytic unit.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent applies preliminary anti-action by converting NO to NO2 upstream to prevent the harmful effect of acid condensate formation downstream. The catalytic oxidation creates a condition that counteracts the potential corrosion problem before it can occur during compression and refrigeration, thus protecting the system without requiring expensive corrosion-resistant materials throughout.

Inventive Principle:
Principle #9Preliminary anti-action

3Reliability

If SNCR process is used for NOx removal, then no catalyst is required and investment cost is lower, but operating temperature must be very high (850-1050°C) and efficiency is limited to 40-65%

Engineering Contradiction:
ImproveNOx removal efficiencyVSAvoidoperating temperature
Core Design Contradiction:
ReliabilityVSTemperature

Solution Approach 1:

The patent replaces the thermal-based SNCR process with a catalytic conversion approach. Instead of relying on high-temperature thermal reactions to remove NOx, the system uses a catalytic converter to facilitate NO oxidation at lower temperatures, followed by conventional purification. This substitution eliminates the need for extreme operating temperatures while achieving superior NOx removal efficiency.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

Solution Approach 2:

The patent changes the operating parameters from high-temperature thermal processing (SNCR at 850-1050°C) to low-temperature catalytic processing (ambient to moderate temperatures). By changing the fundamental parameter of operating temperature and the mechanism of action from thermal to catalytic, the system achieves both lower energy consumption and higher removal efficiency.

Inventive Principle:
Principle #35Parameter changes

4Reliability

If SCR process is used for NOx removal, then removal efficiency exceeds 90%, but operating temperature increases with SO2 content (170-540°C) and investment cost is high

Engineering Contradiction:
ImproveNOx removal efficiencyVSAvoidinvestment cost
Core Design Contradiction:
ReliabilityVSEase of manufacture

Solution Approach 1:

The patent segments the NOx removal process into two distinct stages: (1) catalytic oxidation of NO to NO2 in a dedicated converter, and (2) removal of the converted NOx species through conventional washing or cryogenic separation. This segmentation allows each stage to be optimized independently, achieving high overall efficiency while using cost-effective, conventional technologies for the removal stage rather than requiring expensive SCR systems.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The catalytic converter serves as an intermediary that transforms NO into a more removable form (NO2), enabling the use of simpler, lower-cost purification technologies. This intermediary transformation resolves the contradiction by making conventional, cost-effective purification methods sufficient to achieve high NOx removal efficiency, eliminating the need for expensive SCR systems.

Inventive Principle:
Principle #24Intermediary (Mediator)

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 significantly enhances the purification efficiency of gas streams by achieving high NO to NOx conversion rates, reducing downstream acid formation and corrosion risks, and also captures mercury, resulting in a more comprehensive and efficient NOx abatement process.

Implementation Method 1

conversion of NO to NOx in a catalytic bed at a temperature between 50 and 140°C

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

conversion of nitrogen monoxide NO to nitrogen oxides NOx

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 3

cryogenic separation, by distilling combustion fumes rich in CO2 comprising nitrogen oxides (NOx) where the nitrogen oxides whose oxidation is greater than that of NO are separated from the fumes

Methodology Applied
Scientific EffectCryogenic separation: Cryogenics

Implementation Method 4

distilling combustion fumes rich in CO2 comprising nitrogen oxides

Methodology Applied
Scientific EffectDistillation: Distillation

Implementation Method 5

catalytic bed being a sulfur-doped activated carbon bed

Methodology Applied
Scientific EffectAdsorption: Adsorption

Implementation Method 6

captures mercury

Methodology Applied
Scientific EffectAbsorption: Absorption (physical)

Data Source

PatentEP2435163B1Purifying a gas containing nitrogen oxides
Publication Date: 2018.10.10 LAIR LIQUIDE SA POUR LETUDE & LEXPLOITATION DES PROCEDES GEORGES CLAUDE

AI summary

The invention relates to a method for removing nitrogen monoxide (NO) and nitrogen oxides (NOx with x>1) from a gas stream, implementing a device including a catalytic bed for converting a portion at least a part of the NO into NOx with x>1, and a unit for reducing the NOx with x>1, and in which the gas stream is placed into contact with the catalytic bed before entering the unit for reducing the NOx with x>1.