Integrated Formaldehyde Production via Methanol Oxidation Vent Gas Recycling

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Solution Overview

Problem

The existing processes for producing formaldehyde are inefficient due to the need for a dedicated formaldehyde production facility, which incurs high capital and operating costs, and the small-scale demand for formaldehyde to stabilize urea, leading to suboptimal energy and feedstock usage.

Innovation Solution

A process integrating formaldehyde production with methanol and ammonia co-production, where methanol is oxidized with air to produce a formaldehyde-containing stream, which is then separated and recycled for synthesis gas generation, carbon dioxide removal, methanol synthesis, or urea synthesis, eliminating the need for a separate formaldehyde production unit and vent gas treatment.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If a dedicated formaldehyde production facility is established, then formaldehyde can be produced to stabilize urea, but capital and operating costs increase significantly

Engineering Contradiction:
Improveformaldehyde supply for urea stabilizationVSAvoidcapital and operating costs
Core Design Contradiction:
ReliabilityVSEase of manufacture

Solution Approach 1:

The patent combines formaldehyde production with an existing methanol production facility by integrating a formaldehyde synthesis unit into the methanol plant. The methanol oxidation unit produces formaldehyde as a primary product, leveraging existing infrastructure (reactors, distillation columns, vent gas treatment units) to avoid the need for a completely separate dedicated facility, thereby reducing capital and operating costs while ensuring reliable formaldehyde supply for urea stabilization.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The methanol production facility is designed to perform multiple functions: producing methanol as the primary product and formaldehyde as a secondary product. The same production unit can switch between or simultaneously produce both chemicals by adjusting operating conditions, making the facility universal and reducing the need for dedicated single-purpose plants, thus lowering overall costs while maintaining product reliability.

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

2Reliability

If formaldehyde is produced at a separate dedicated facility and transported to the ammonia/urea production facility, then formaldehyde supply is ensured, but energy and feedstock efficiency decreases

Engineering Contradiction:
Improveformaldehyde supply to urea facilityVSAvoidenergy and feedstock efficiency
Core Design Contradiction:
ReliabilityVSLoss of energy

Solution Approach 1:

The patent merges the formaldehyde production facility with the methanol production facility at the same location, eliminating the need for transportation between separate facilities. The integrated plant produces both methanol and formaldehyde on-site, reducing energy consumption associated with transport and storage, while ensuring continuous and reliable formaldehyde supply for urea stabilization through direct integration with the urea production unit.

Inventive Principle:
Principle #5Merging (Combining)

3Reliability

If a dedicated formaldehyde production facility is built, then formaldehyde can be produced, but the scale is suboptimal for small demand

Engineering Contradiction:
Improveformaldehyde production capabilityVSAvoidproduction efficiency
Core Design Contradiction:
ReliabilityVSProductivity

Solution Approach 1:

The methanol production facility is designed with multi-functionality to produce both methanol and formaldehyde. By adjusting the oxidation conditions and feedstock ratios, the same facility can optimize production between the two products based on demand, achieving optimal scale and efficiency for formaldehyde production without requiring a separate dedicated plant that would operate at suboptimal capacity for small-scale urea stabilization needs.

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

4Ease of manufacture

If formaldehyde production is integrated with methanol and ammonia co-production, then capital and operating costs are reduced, but process complexity increases

Engineering Contradiction:
Improvecapital and operating costsVSAvoidprocess integration complexity
Core Design Contradiction:
Ease of manufactureVSDevice complexity

Solution Approach 1:

The patent integrates formaldehyde production into the existing methanol production process by adding oxidation units that convert methanol to formaldehyde using the same feedstock and infrastructure. The integration utilizes existing distillation columns and vent gas treatment units, merging multiple functions into a unified process flow that reduces overall plant complexity compared to maintaining separate dedicated facilities, while achieving cost reductions through shared infrastructure.

Inventive Principle:
Principle #5Merging (Combining)

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 integrated process reduces capital and operating costs by recycling vent gases, improving ammonia productivity, and enabling more efficient use of energy and feedstocks, while simplifying the formaldehyde production unit and eliminating the need for expensive emissions control systems.

Implementation Method 1

subjecting methanol to oxidation with air in a formaldehyde production unit thereby producing a formaldehyde-containing stream

Methodology Applied
Scientific EffectOxidation: Oxidation

Data Source

PatentUS10457634B2Process for the production of formaldehyde
Publication Date: 2019.10.29 JOHNSON MATTHEY DAVY TECHNOLOGIES LTD
  • US10457634B2 patent drawing
  • US10457634B2 patent drawing

AI summary

A process is described for the production of formaldehyde, comprising (a) subjecting methanol to oxidation with air in a formaldehyde production unit thereby producing a formaldehyde-containing stream; (b) separating said formaldehyde-containing stream into a formaldehyde product stream and a formaldehyde vent gas stream; wherein the vent gas stream, optionally after treatment in a vent gas treatment unit, is passed to one or more stages of: (i) synthesis gas generation, (ii) carbon dioxide removal, (iii) methanol synthesis or (iv) urea synthesis.