Network Mixer with Oblique Channels for Convective Mixing

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Solution Overview

Problem

Current mixing devices in industrial processes, especially those involving chemical reactions, face inefficiencies in mixing and control due to reliance on simplifying assumptions and limited flexibility, with existing technologies struggling to effectively manage convective mechanisms and the addition of multiple fluids during reactions.

Innovation Solution

A network mixer design featuring individualized chambers and obliquely connected channels, allowing for convective and diffusive mixing mechanisms, with versatile injection and ejection points, enabling efficient control of reaction conversion and selectivity, and temperature management through a high specific area for heat transfer.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If monolithic structures are used for mixing, then structural simplicity and ease of manufacture are improved, but mixing efficiency and flexibility are worsened

Engineering Contradiction:
Improveease of manufactureVSAvoidmixing efficiency
Core Design Contradiction:
Ease of manufactureVSProductivity

Solution Approach 1:

The mixing device is divided into multiple modular units, each containing channels and chambers that can be independently configured. This segmentation allows for improved mixing efficiency through multiple flow paths while maintaining ease of manufacture through modular construction

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention transitions from traditional two-dimensional mixing approaches to a three-dimensional network structure with channels and chambers arranged in multiple spatial dimensions, enabling convective mixing mechanisms that significantly improve mixing efficiency while keeping the structure manufacturable

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

2Ease of operation

If complex mixing structures with static flow barriers are used, then mixing control is improved, but device complexity and cost are worsened

Engineering Contradiction:
Improvemixing controlVSAvoiddevice complexity
Core Design Contradiction:
Ease of operationVSDevice complexity

Solution Approach 1:

Different regions of the mixing device have specialized functions - channels are optimized for flow distribution, chambers for mixing and reaction control. This local optimization achieves superior mixing control without requiring complex overall structure

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The mixing device is designed to perform multiple functions simultaneously - mixing, reaction control, temperature management, and fluid distribution - through a unified structure, reducing overall device complexity while improving operational control

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

3Productivity

If microreactors and microfluidic systems are used, then mixing efficiency is improved, but manufacturing complexity and cost are worsened

Engineering Contradiction:
Improvemixing efficiencyVSAvoidmanufacturing complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The device incorporates adjustable flow distribution and variable residence time characteristics through its channel and chamber geometry, enabling dynamic control of mixing and reaction conditions without requiring complex manufacturing processes

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The mixing mechanism is replicated across multiple identical or similar units arranged in parallel, allowing for simplified manufacturing of individual modules while achieving high mixing efficiency through the collective action of multiple units

Inventive Principle:
Principle #26Copying

4Ease of operation

If traditional mixing devices are used, then operational simplicity is maintained, but mixing speed and homogeneity are worsened

Engineering Contradiction:
Improveoperational simplicityVSAvoidmixing speed
Core Design Contradiction:
Ease of operationVSSpeed

Solution Approach 1:

The mixing device operates continuously with fluids flowing through the channels and chambers in a steady-state process, eliminating the need for intermittent mixing actions and maintaining simple operation while achieving rapid mixing through continuous convective action

Inventive Principle:
Principle #20Continuity of useful 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

The network mixer achieves efficient mixing and reaction control, reducing costs and environmental impact by promoting convective mechanisms, allowing flexible fluid addition, and enhancing reaction selectivity and temperature control, thereby improving process efficiency and safety.

Implementation Method 1

allowing for convective and diffusive mixing mechanisms

Methodology Applied
Scientific EffectConvection: Convection

Implementation Method 2

allowing for convective and diffusive mixing mechanisms

Methodology Applied
Scientific EffectDiffusion: Diffusion

Implementation Method 3

enhancing reaction selectivity and temperature control through a high specific area for heat transfer

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Data Source

PatentUS8434933B2Network mixer and related mixing process
Publication Date: 2013.05.07 BRITO LOPES JOSE CARLOS
  • US8434933B2 patent drawing
  • US8434933B2 patent drawing
  • US8434933B2 patent drawing

AI summary

A static continuous flow mixer, with or without reaction, is provided with basic cells, which are individually provided with an individualized chamber (1). The basic cells are also provided with at least two connecting channels (2), at least two of them being oblique relatively to the resulting direction (x) of the flow in the mixer, and with at least two additional apertures (0) for connection with the exterior. The cells interconnect successively in the space, forming a network. The mixer promotes convective processes. The dimensions (Dj, li, di, φ), the geometry of the chambers (spherical or cylindrical) and of the channels (cylindrical or prismatic) may vary, as well as their quantity.