Isothermal and Adiabatic Absorption for Phosgene Recovery

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Solution Overview

Problem

Current processes for producing isocyanates result in high concentrations of phosgene in the hydrogen chloride stream, leading to material losses and safety concerns, with existing separation methods being energetically unfavorable and inefficient.

Innovation Solution

A two-stage absorption process involving isothermal and adiabatic absorption steps, where phosgene is partially condensed and then absorbed in a solvent, followed by further adiabatic absorption to achieve low phosgene concentrations in the hydrogen chloride stream, minimizing material losses and enhancing safety.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Loss of substance

If conventional separation methods are used to remove phosgene from the hydrogen chloride stream, then phosgene recovery is achieved, but energy consumption increases and process complexity increases

Engineering Contradiction:
Improvephosgene lossVSAvoidenergy consumption
Core Design Contradiction:
Loss of substanceVSUse of energy by stationary object

Solution Approach 1:

The invention changes the temperature parameter of the absorption process by implementing a two-stage system with isothermal absorption at lower temperatures followed by adiabatic absorption at higher temperatures. This parameter variation optimizes phosgene absorption efficiency while reducing energy consumption compared to conventional single-stage methods

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The separation process is divided into two distinct stages: isothermal absorption and adiabatic absorption. Each stage operates under different thermal conditions to maximize phosgene recovery efficiency while minimizing overall energy requirements and process complexity

Inventive Principle:
Principle #1Segmentation

2Loss of substance

If conventional separation methods are used to remove phosgene from the hydrogen chloride stream, then phosgene recovery is achieved, but device complexity increases

Engineering Contradiction:
Improvephosgene lossVSAvoidprocess complexity
Core Design Contradiction:
Loss of substanceVSDevice complexity

Solution Approach 1:

The separation process is divided into two distinct stages: isothermal absorption and adiabatic absorption. Each stage operates under different thermal conditions to maximize phosgene recovery efficiency while minimizing overall energy requirements and process complexity

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The absorption system serves multiple functions: it removes phosgene from the hydrogen chloride stream, recovers phosgene for reuse, and does so through a integrated two-stage process that combines isothermal and adiabatic operations in a unified configuration

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

3Loss of substance

If high concentrations of phosgene are present in the hydrogen chloride stream, then material loss is reduced, but safety hazards increase

Engineering Contradiction:
Improvephosgene lossVSAvoidsafety hazards
Core Design Contradiction:
Loss of substanceVSObject-affected harmful factors

Solution Approach 1:

The invention changes the temperature parameter of the absorption process by implementing a two-stage system with isothermal absorption at lower temperatures followed by adiabatic absorption at higher temperatures. This parameter variation optimizes phosgene absorption efficiency while reducing energy consumption compared to conventional single-stage methods

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The process converts the potentially harmful presence of phosgene in the hydrogen chloride stream into a beneficial recovery opportunity. By using the two-stage absorption system, phosgene that would otherwise be wasted or pose safety risks is efficiently captured and reused in the phosgene synthesis process

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

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 effectively reduces phosgene content in the hydrogen chloride stream to less than 0.5 wt%, minimizing raw material loss and improving process safety, while also optimizing energy usage and reducing the number of equipment components, thereby enhancing the economic viability of the process.

Implementation Method 1

the vapor mixture formed when phosgene and amine are reacted is subjected to at least one isothermal absorption treatment and at least one adiabatic absorption treatment

Methodology Applied
Scientific EffectCondensation: Condensation

Implementation Method 2

the vapor mixture formed when phosgene and amine are reacted is subjected to at least one isothermal absorption treatment

Methodology Applied
Scientific EffectAbsorption (physical): Absorption (physical)

Implementation Method 3

the vapor mixture formed when phosgene and amine are reacted is subjected to at least one isothermal absorption treatment and at least one adiabatic absorption treatment

Methodology Applied
Scientific EffectAbsorption (physical): Absorption (physical)

Data Source

PatentEP1849767B1Process for the production of isocyanates
Publication Date: 2009.10.28 BAYER MATERIALSCIENCE LLC
  • EP1849767B1 patent drawingFigure 1
  • EP1849767B1 patent drawingFigure 2
  • EP1849767B1 patent drawingFigure 3

AI summary

Isocyanates are produced by a) reacting at least one amine with phosgene, optionally in the presence of a solvent to produce the corresponding isocyanate and a stream containing hydrogen chloride, phosgene and optionally solvent, low-boiling compounds and inert substances is obtained, b) separating the stream containing hydrogen chloride, phosgene and optionally solvent, low-boiling compounds and inert substances in an at least two-stage sequence of absorption steps that includes (1) at least one isothermal absorption step and (2) at least one adiabatic absorption step, to obtain (i) a hydrogen chloride stream containing phosgene in concentrations of at most 0.5 wt.% (based on the weight of the hydrogen chloride stream) and (ii) a liquid phosgene stream, and c) recycling the liquid phosgene stream (ii) to the reaction of amine with phosgene.