Melamine Offgas Scrubbing with Cooled Urea Melt Recirculation
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Solution Overview
Problem
The existing high-pressure melamine synthesis processes face issues with melamine cyanurate precipitation and corrosion in urea melt coolers due to the use of a double-stage scrubbing process, leading to operational inefficiencies and high investment costs.
Innovation Solution
A single-stage scrubbing process using urea melt to purify melamine offgas, with recirculated urea melt cooled to a temperature above 165°C and mixed with fresh urea melt, prevents melamine cyanurate precipitation and reduces corrosion, maintaining process efficiency.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Manufacturing precision
If a double-stage scrubbing process is used to purify melamine offgas, then the purification efficiency is improved, but melamine cyanurate precipitation and corrosion in urea melt coolers occur
Solution Approach 1:
The patent changes the temperature parameter of the recirculated urea melt by cooling it to a controlled temperature range before reintroduction. This parameter change prevents melamine cyanurate precipitation while maintaining purification efficiency, resolving the contradiction between purification performance and operational reliability.
2Manufacturing precision
If a double-stage scrubbing process is used to purify melamine offgas, then the purification efficiency is improved, but investment costs increase
Solution Approach 1:
The patent merges the purification stages into a single-stage scrubbing process where recirculated cooled urea melt is reintroduced. This consolidation maintains purification efficiency while reducing the number of equipment units and overall investment costs.
3Loss of energy
If recirculated urea melt is cooled to recover heat, then energy efficiency is improved, but melamine cyanurate precipitation occurs
Solution Approach 1:
The patent optimizes the cooling temperature parameter of the recirculated urea melt, maintaining it within a specific range that allows heat recovery while preventing melamine cyanurate precipitation. This controlled parameter change resolves the contradiction between energy efficiency and harmful precipitation.
4Loss of energy
If the urea melt cooler operates at high efficiency, then heat recovery is improved, but corrosion risk increases
Solution Approach 1:
The patent controls the temperature parameter of the recirculated urea melt to optimize the operating conditions of the urea melt cooler. By maintaining the temperature within a specific range, the system achieves efficient heat recovery while reducing corrosion risk through optimized thermal conditions.
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 single-stage process effectively purifies melamine offgas, reduces corrosion risks, and lowers equipment maintenance, while maintaining energy efficiency and reducing the risk of plant shutdowns.
Implementation Method 1
The contact between the offgas and the falling urea melt generates melamine precursors such as ammeline and cyanuric acid
Implementation Method 2
The contact between the offgas and the falling urea melt generates melamine precursors
Implementation Method 3
The recirculated portion of urea melt is cooled in a urea melt cooler prior to reintroduction into the first stage. Cooling the urea melt recovers the heat released by the scrubbing process
Implementation Method 4
Cooling the urea melt recovers the heat released by the scrubbing process, particularly by the absorption of the offgas in the urea melt
Implementation Method 5
said recirculated urea melt being cooled in a shell and tube heat exchanger
Data Source
AI summary
A process for the synthesis of melamine including the purification of the offgas released by the synthesis of melamine by means of a single purification stage (6); in the purification stage (6), the offgas (3) is washed with fresh urea melt and with a recirculated urea melt (8) containing ammonia and melamine precursors (5); said recirculated urea melt is withdrawn from bottom of the single purification stage (6) and cooled in a shell and tube heat exchanger (11), optionally after mixing with the fresh urea melt (15), to a temperature of at least 165° C. preferably in the range 165° C. to 245° C. prior to reintroduction in the purification stage.

