Isocyanate Phosgenation Process for Partial Load Mixing

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Existing processes for preparing isocyanates by phosgenation of amines face challenges in maintaining optimal mixing and residence time during partial plant load operations, leading to decreased yield and quality issues.

Innovation Solution

The process involves adjusting the ratio of phosgene to amine and increasing the concentration of inert materials in the feed streams during periods of reduced amine flow below nominal capacity, ensuring rapid mixing and optimal residence time in the reactor plant, regardless of load state.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Adaptability or versatility

If the plant operates below nominal capacity, then production flexibility is improved, but mixing quality and residence time deviate from optimal values leading to decreased yield

Engineering Contradiction:
Improveproduction flexibilityVSAvoidmixing quality
Core Design Contradiction:
Adaptability or versatilityVSManufacturing precision

Solution Approach 1:

The invention applies dynamics by making the process parameters dynamic rather than fixed. The mixing device and reaction space are designed to adapt their operating characteristics based on the load state. By adjusting operational parameters such as mixing intensity, flow rates, and residence time according to the actual production demand, the system maintains optimal mixing quality and reaction conditions even when operating below nominal capacity, thus resolving the contradiction between production flexibility and manufacturing precision

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The invention utilizes parameter changes by systematically adjusting key process parameters in response to load variations. When operating below nominal capacity, parameters such as mixing speed, feed rates, temperature, and residence time are modified to compensate for reduced material flows. This ensures that the critical quality attributes of mixing and reaction remain within optimal ranges regardless of production level, thereby maintaining manufacturing precision while enabling production flexibility

Inventive Principle:
Principle #35Parameter changes

2Adaptability or versatility

If the plant operates below nominal capacity, then production flexibility is improved, but product yield and quality decrease

Engineering Contradiction:
Improveproduction flexibilityVSAvoidproduct yield
Core Design Contradiction:
Adaptability or versatilityVSProductivity

Solution Approach 1:

The system employs dynamic control strategies where process parameters are continuously adjusted based on the load state. By adapting mixing intensity, reaction time, temperature, and feed rates to match the actual production demand, the system maintains high conversion efficiency and product yield even at reduced capacity levels, thus resolving the contradiction between production flexibility and productivity

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The invention implements feedback control mechanisms that monitor process parameters and product quality in real-time. Based on this feedback, the system automatically adjusts operational parameters to optimize yield at each load level. This closed-loop control ensures that even when operating below nominal capacity, the process maintains optimal efficiency and product yield, preventing the typical decline in productivity associated with partial load operation

Inventive Principle:
Principle #23Feedback

3Speed

If vaporization is carried out at elevated temperature, then gas-phase phosgenation is enabled, but decomposition reactions occur reducing selectivity

Engineering Contradiction:
Improvereaction speedVSAvoidselectivity
Core Design Contradiction:
SpeedVSManufacturing precision

Solution Approach 1:

The invention applies parameter changes by optimizing the temperature parameter within a specific range that enables sufficient vaporization for gas-phase reaction while staying below the decomposition threshold of the amine. By carefully selecting and controlling the temperature parameter, the process achieves the necessary reaction speed through enhanced molecular activity while maintaining high selectivity by avoiding thermal decomposition reactions

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention employs partial action by providing just enough thermal energy to achieve the required vaporization and reaction kinetics without excessive heating that would lead to decomposition. The temperature is controlled at the minimum level necessary to maintain gas-phase conditions and adequate reaction speed, thereby avoiding the harmful effects of excessive temperature while still achieving the desired reaction rate

Inventive Principle:
Principle #16Partial or excessive action

4Duration of action of moving object

If mixing is delayed, then residence time increases allowing complete reaction, but secondary reactions form reducing selectivity

Engineering Contradiction:
Improveresidence timeVSAvoidselectivity
Core Design Contradiction:
Duration of action of moving objectVSManufacturing precision

Solution Approach 1:

The invention applies dynamics by making the residence time a dynamic parameter that adapts to the load state and reaction conditions. Rather than using a fixed residence time, the system adjusts it in real-time to achieve optimal conversion while minimizing secondary reactions. This dynamic adjustment ensures that the residence time is sufficient for complete primary reaction at each moment without allowing excessive accumulation that would promote unwanted secondary reactions

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The invention employs preliminary action by ensuring rapid and thorough mixing of reactants before the reaction proceeds. This preliminary intensive mixing stage creates a homogeneous reaction environment where the primary reaction occurs efficiently and uniformly, reducing the likelihood of localized conditions that would promote secondary reactions. The subsequent residence time is then optimized to complete the reaction without excessive delay

Inventive Principle:
Principle #10Preliminary action

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 allows for consistent product quality and yield across varying plant loads, potentially eliminating the need for multiple plants with different nominal capacities and reducing fouling and decomposition issues.

Implementation Method 1

Rapid mixing of the amine with the phosgene is necessary since, at an insufficient phosgene concentration, the isocyanate formed reacts with the excess amine to form urea or other troublesome, high-viscosity and solid by-products.

Methodology Applied
Scientific EffectRapid mixing:

Implementation Method 2

The amine and the phosgene react with liberation of HCl to form the corresponding isocyanate.

Methodology Applied
Scientific EffectChemical reaction: Chemical Bonding

Implementation Method 3

The amine-comprising feed stream and the phosgene-comprising feed stream are mixed in a mixing device to form a reaction mixture which is subsequently reacted for a short time in a reaction chamber.

Methodology Applied
Scientific EffectResidence time:

Data Source

PatentUS8816126B2Process for preparing isocyanates
Publication Date: 2014.08.26 BASF SE

AI summary

Process for preparing isocyanates by reacting the corresponding amines comprised in at least one feed stream A with phosgene comprised in at least one feed stream P in a reaction plant comprising at least one mixing zone and at least one reaction zone, wherein feed stream A and/or feed stream P optionally comprise one or more inert materials and,during periods of time in which the flow Sx of the amine used is below the flow S0 of the amines used during operation at the nominal capacity of the reactor plant,(i) the ratio of phosgene to amine is increased and/or(ii) the concentration of the inert material or materials in the amine-comprising feed stream A and/or the phosgene-comprising feed stream P is increasedcompared to operation at the nominal capacity of the reactor.