Taylor Reactor Quantum Dot Manufacturing

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Current methods for mass-producing quantum dots face challenges in uniformly controlling particle size and achieving high crystallinity, leading to issues with color purity and stability, particularly during scale-up and exposure to moisture and oxygen.

Innovation Solution

An automatic quantum dot manufacturing apparatus and method that fluidly connects Taylor reactors for core synthesis, shell synthesis, and washing, allowing for continuous or semi-continuous production of colloidal or powdered quantum dots by controlling temperature and using a Taylor vortex for uniform mixing and precise temperature control.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Temperature

If batch reaction system (hot injection method) is used for quantum dot synthesis, then high temperature reaction can be achieved, but uniform control of reaction temperature and time becomes difficult leading to poor manufacturing precision

Engineering Contradiction:
Improvereaction temperatureVSAvoiduniformity of quantum dot diameter
Core Design Contradiction:
TemperatureVSManufacturing precision

Solution Approach 1:

The patent divides the quantum dot synthesis process into multiple sequential microreactors (first microreactor for core formation, second microreactor for shell formation, third microreactor for washing). Each microreactor operates at controlled temperature and processes a specific stage, enabling precise temperature control for each step while maintaining overall manufacturing precision. This segmentation resolves the contradiction by allowing high temperature reactions in controlled environments rather than a single batch system.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent employs a microfluidic system where precursors are delivered through capillaries using hydraulic flow control. The microreactors utilize fluid dynamics to maintain laminar flow and precise mixing, enabling accurate temperature and residence time control. This hydraulic approach replaces the manual batch injection method, providing automated precision in temperature and time control while maintaining high reaction temperatures.

Inventive Principle:
Principle #29Pneumatics and hydraulics

2Productivity

If scale-up is performed in hot injection method, then production capacity increases, but temperature control range increases and reaction time control becomes difficult

Engineering Contradiction:
Improveproduction capacityVSAvoidcontrol of reaction time
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent segments the synthesis process across multiple microreactors connected in series. Each microreactor handles a specific function (core formation, shell formation, washing) with controlled residence time. This segmentation allows the system to scale up production capacity by increasing flow rates through the series-connected reactors while maintaining precise reaction time control in each individual reactor, resolving the contradiction between productivity and time control precision.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent implements a continuous flow system where precursors continuously flow through the microreactors without batch interruptions. The microfluidic channels maintain continuous mixing and reaction, eliminating the start-stop nature of batch processing. This continuity enables sustained high production capacity while maintaining consistent reaction times through controlled flow rates, resolving the contradiction between productivity and time control.

Inventive Principle:
Principle #20Continuity of useful action

3Device complexity

If batch-type hot injection method is used, then simple apparatus can be used, but stirring intensity becomes weak at large scale leading to poor mixing uniformity

Engineering Contradiction:
Improvereactor system simplicityVSAvoiduniformity of particle formation
Core Design Contradiction:
Device complexityVSStability of the object's composition

Solution Approach 1:

The patent replaces mechanical stirring with hydraulic mixing in microfluidic channels. The microreactors utilize laminar flow and diffusion-driven mixing, where precursors mix uniformly as they flow through narrow channels. This hydraulic mixing approach eliminates the need for mechanical stirrers, maintaining device simplicity while achieving superior mixing uniformity through controlled fluid dynamics, resolving the contradiction between apparatus simplicity and composition stability.

Inventive Principle:
Principle #29Pneumatics and hydraulics

Solution Approach 2:

The patent transitions from three-dimensional bulk mixing in batch reactors to two-dimensional surface-dominated mixing in microfluidic channels. The narrow channel dimensions create a high surface-area-to-volume ratio, enhancing diffusion and mixing efficiency. This dimensional change allows simple channel structures without moving parts to achieve uniform mixing, resolving the contradiction between device simplicity and mixing uniformity.

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

4Productivity

If conventional manufacturing methods are used, then quantum dots can be produced, but color purity decreases due to increased FWHM

Engineering Contradiction:
Improvemanufacturing capabilityVSAvoidcolor purity
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent segments the synthesis into distinct microreactors for core formation and shell formation, with each step optimized for specific size control. The sequential processing in series-connected microreactors narrows the particle size distribution, directly reducing FWHM and improving color purity. This segmentation enables mass production capability while maintaining narrow size distributions, resolving the contradiction between productivity and color purity.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent systematically controls and optimizes multiple parameters including precursor concentration, flow rates, temperature, and residence time in each microreactor stage. By precisely adjusting these parameters, the system achieves narrow particle size distributions and high crystallinity, reducing FWHM while maintaining production capacity. This parameter optimization resolves the contradiction between manufacturing capability and color purity.

Inventive Principle:
Principle #35Parameter changes

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

Enables the automatic and continuous production of quantum dots with uniform particle size and high crystallinity, improving color purity and stability, while reducing production time and costs by using a single reactor system for multiple steps.

Implementation Method 1

a first Taylor reactor fluidly connected to a core precursor supply source; a second Taylor reactor fluidly connected to a shell precursor supply source and the first Taylor reactor

Methodology Applied
Scientific EffectTaylor vortex: Vortex Ring

Data Source

PatentUS20230278002A1Automatic quantum dot manufacturing apparatus and automatic quantum dot manufacturing method
Publication Date: 2023.09.07 LAMINAR
  • US20230278002A1 patent drawing
  • US20230278002A1 patent drawing

AI summary

The present invention relates to an automatic quantum dot manufacturing apparatus, which can automatically and/or continuously or semi-continuously manufacture quantum dots from a precursor by fluidly connecting a Taylor reactor for core synthesis, a Taylor reactor for shell synthesis, and a Taylor reactor for quantum dot washing to each other, and an automatic quantum dot manufacturing method using the same, in which the apparatus includes: a first Taylor reactor fluidly connected to a core precursor supply source; a second Taylor reactor fluidly connected to a shell precursor supply source and the first Taylor reactor; and a third Taylor reactor fluidly connected to a washing liquid supply source and the second Taylor reactor.