Fluid Mixing and Splitting Apparatus with Pressure Feedback Control

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Solution Overview

Problem

Chemical processes like olefin polymerization in gas-phase fluidized-bed reactors face challenges with uniform distribution of reactants, leading to issues like electrostatic charges, hot spots, and fouling due to local inhomogeneities in reactant feeding, requiring a method for controlled mixing and splitting of fluid streams to maintain accurate flow ratios and adapt to pressure fluctuations.

Innovation Solution

A process involving continuous mixing of fluid streams through separated conduits, forming a homogeneous mixture, measuring pressure, and splitting it into partial streams with flow control devices adjusted by pressure feedback to maintain consistent flow rates, allowing flexible adjustment of component ratios and robustness against reactor difficulties.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Stability of the object's composition

If multiple feeding points are used to improve uniform distribution of reactants, then homogeneity of reactant distribution is improved, but device complexity and difficulty of control increase

Engineering Contradiction:
Improveuniform distribution of reactantsVSAvoidnumber of feeding points
Core Design Contradiction:
Stability of the object's compositionVSDevice complexity

Solution Approach 1:

The single feed stream is segmented into multiple partial streams that are distributed to different feeding points in the reactor. This allows the system to maintain uniform reactant distribution across multiple locations while managing complexity through a centralized mixing unit that handles the segmentation logic.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Pressure sensors are installed in the feeding lines to provide real-time feedback on flow conditions. This feedback is used by control valves to automatically adjust and equalize the flow rates to each feeding point, maintaining uniform distribution without requiring complex manual control of multiple feeding points.

Inventive Principle:
Principle #23Feedback

2Manufacturing precision

If flow control devices are installed at multiple feeding points to maintain accurate flow ratios, then manufacturing precision of flow distribution is improved, but device complexity increases

Engineering Contradiction:
Improveflow ratio accuracyVSAvoidnumber of control devices
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

Multiple control functions are merged into a single centralized control system that receives pressure feedback from multiple sensing points and coordinates the control valves accordingly. This reduces the number of independent control devices needed while maintaining precise flow ratio accuracy through collaborative control.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

Pressure feedback from the feeding lines is used to dynamically adjust control valve positions, ensuring accurate flow ratios are maintained despite variations in reactor pressure or line conditions. The feedback loop continuously equalizes flow distribution without requiring complex predictive control algorithms.

Inventive Principle:
Principle #23Feedback

3Device complexity

If mixing is performed before splitting to reduce number of feeding points, then device complexity is reduced, but reliability decreases due to potential plugging in feeding lines

Engineering Contradiction:
Improvenumber of feeding pointsVSAvoidresistance to conduit plugging
Core Design Contradiction:
Device complexityVSReliability

Solution Approach 1:

The mixing of reactant streams is performed in advance in a dedicated mixing unit before distribution to multiple feeding points. This preliminary mixing ensures homogeneous composition throughout the feed, reducing the risk of localized plugging or fouling in the distribution lines while maintaining a manageable number of feeding points.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

Pressure monitoring in the feeding lines provides early warning of potential plugging conditions. The feedback control system can detect pressure drops or increases that indicate incipient fouling and adjust flow rates accordingly, preventing complete blockages and maintaining system reliability.

Inventive Principle:
Principle #23Feedback

4Reliability

If pressure measurement and feedback control are implemented to adapt to pressure fluctuations, then reliability is improved, but device complexity increases

Engineering Contradiction:
Improveadaptability to pressure changesVSAvoidcontrol system complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

Pressure sensors in the feeding lines provide real-time feedback on reactor pressure conditions and line pressure drops. This feedback is fed to control valves that automatically adjust their opening positions to maintain constant flow rates despite pressure fluctuations, improving reliability through adaptive control.

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The control system uses the pressure feedback to self-regulate flow distribution without external intervention. The control valves automatically compensate for pressure changes based on the feedback signal, making the system self-correcting and reducing the need for complex external control algorithms or manual adjustments.

Inventive Principle:
Principle #25Self-service

Data Source

PatentUS9000114B2Process and apparatus for mixing and splitting fluid streams
Publication Date: 2015.04.07 BASELL POLYOLEFINE GMBH
  • US9000114B2 patent drawing
  • US9000114B2 patent drawing

AI summary

A process for continuously mixing at least two fluid streams and splitting the stream of the mixture into at least two partial streams, comprising a) providing streams of the at least two fluids via separated conduits; b) combining the streams of the fluids and forming a homogeneous mixture; c) measuring the pressure in the conduit conveying the mixture of the fluids; d) splitting the stream of the mixture of the fluids into at least two partial streams and feeding each of the partial streams to a conduit equipped with a flow control device controlled by a controller; and e) adjusting the flow rates of the partial streams of the mixture of the fluids by feeding the pressure information measured in step c) as process variable to the controllers controlling the flow control devices, a process for feeding a mixture of at least two fluids via at least two feeding points, an apparatuses for carrying out such processes and a process for polymerizing olefins.