Catalyst Slurry Valve Control for Stable Reactor Flow Distribution

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Solution Overview

Problem

Gas-phase polymerization processes face challenges with thermal fluctuations and catalyst particle overheating, leading to polymer agglomeration, equipment plugging, and sub-optimal process control due to the use of control valves with solid catalyst particles, which result in reactor shutdowns and product quality issues.

Innovation Solution

A method involving at least three injection nozzles and corresponding lines with independent slurry flow valves to regulate the flow rate and temperature of modified catalyst slurry, ensuring balanced distribution and activation of catalyst compounds in a gas-phase polymerization reactor.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of operation

If control valves are used to regulate catalyst flow, then process control is achieved, but valve erosion and plugging occur due to solid catalyst particles

Engineering Contradiction:
Improveprocess controlVSAvoidvalve durability
Core Design Contradiction:
Ease of operationVSReliability

Solution Approach 1:

The harmful solid catalyst particles are separated from the fluid stream before reaching the control valve. A catalyst solution is introduced downstream of the valve to modify catalyst properties, extracting the solids removal function from the valve system and preventing erosion and plugging while maintaining control capability.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

Catalyst properties are modified in advance by introducing a catalyst solution before the catalyst enters the reactor. This preliminary modification adjusts catalyst activity and flow characteristics upstream, enabling better control valve performance and preventing downstream issues with particle accumulation and erosion.

Inventive Principle:
Principle #10Preliminary action

2Productivity

If catalyst particles are heated during polymerization, then reaction rate increases, but thermal swings cause polymer agglomeration and sheeting

Engineering Contradiction:
Improvereaction rateVSAvoidpolymer agglomeration
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The physical and chemical parameters of the catalyst are modified by introducing a catalyst solution that changes catalyst composition, activity, and thermal properties. This parameter adjustment allows the catalyst to operate at higher temperatures without causing polymer agglomeration, maintaining high reaction rates while preventing thermal runaway and sheeting.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

A catalyst solution acts as an intermediary substance that modifies catalyst properties and mediates the heat transfer process. This intermediary controls the thermal environment of the catalyst particles, enabling sustained high reaction rates while preventing excessive temperature swings that would cause polymer agglomeration and sheeting.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Adaptability or versatility

If multiple catalyst lines are used for flexibility, then process adaptability improves, but flow distribution control becomes difficult

Engineering Contradiction:
Improveprocess flexibilityVSAvoidflow distribution control
Core Design Contradiction:
Adaptability or versatilityVSManufacturing precision

Solution Approach 1:

Each catalyst line receives a locally optimized catalyst solution composition and flow rate tailored to that specific line's requirements. This local quality adjustment ensures uniform catalyst distribution across all lines despite varying flow conditions, maintaining precise flow distribution control while preserving the flexibility benefits of multiple lines.

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

Catalyst solution is introduced in controlled partial amounts to each line based on individual flow requirements. This partial action approach allows independent optimization of each line's catalyst concentration and flow rate, achieving precise flow distribution control while maintaining the adaptability of the multi-line system.

Inventive Principle:
Principle #16Partial or excessive 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 stabilizes catalyst temperature and flow rates, reducing thermal swings and equipment fouling, thereby enhancing process control and maintaining consistent polymer quality without reactor shutdowns.

Implementation Method 1

independently regulating each of: a) a first flow rate of modified catalyst slurry of the first line by at least partially opening or closing a first slurry flow valve in contact with the first line

Methodology Applied
Scientific EffectFluid flow regulation:

Implementation Method 2

independently heating each of: a) the first modified catalyst slurry of the first line using a first heating block, b) the second modified catalyst slurry of the second line using a second heating block, or c) the third modified catalyst slurry of the third line using a third heating block

Methodology Applied
Scientific EffectThermal heating: Heating

Implementation Method 3

thermal swings during gas-phase polymerization can alter the viscosity of fluids, resulting in flow rate alterations, equipment (e.g., injection nozzle) plugging

Methodology Applied
Scientific EffectThermal viscosity reduction:

Data Source

PatentUS20260034528A1Methods for Regulating Reactor Catalyst Flow Distribution During Olefin Polymerization
Publication Date: 2026.02.05 EXXONMOBIL TECHNOLOGY & ENGINEERING CO
  • US20260034528A1 patent drawing
  • US20260034528A1 patent drawing
  • US20260034528A1 patent drawing

AI summary

Slurry flow valves may be used to control flow in a gas-phase polymerization reactor. For example, a system may include at least three injection nozzles fluidly connected to a gas-phase polymerization reactor, wherein the at least three injection nozzles are configured to carry' a modified catalyst slurry; at least three lines connected to the at least three injection nozzles, wherein the at least-three lines comprise a first line connected to a first injection nozzle, a second line connected to a second injection nozzle, and a third line connected to a third injection nozzle; and at least three slurry? flow valves in contact with the at least three lines, wherein the at least three slurry flow valves comprise a first slurry flow valve, a second slurry flow valve, and a third slurry' flow valve. Preferably, the valves can each be independently controlled to regulate flow therethrough.