Gyrolite Calcium Silicate Powder Production via Spray Drying

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Conventional gyrolite-type calcium silicate powders have small particle sizes and poor handleability due to their finely divided form, leading to issues with flowability and high powder scattering during filling, and attempts to increase particle size through granulation compromise oil absorption and strength.

Innovation Solution

A method involving the use of gypsum and a calcium compound in an aqueous solvent, followed by hydrothermal synthesis and spray-drying to produce gyrolite-type calcium silicate powder with large particle size, high oil absorption, and enhanced particle strength without the need for granulation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If conventional gyrolite-type calcium silicate powder is produced by hydrothermal treatment, then high oil absorption is achieved, but particle size remains small and handleability deteriorates

Engineering Contradiction:
Improveoil absorptionVSAvoidhandleability
Core Design Contradiction:
Quantity of substanceVSEase of operation

Solution Approach 1:

The patent applies preliminary action by conducting hydrothermal treatment before spray-drying to pre-form the gyrolite crystal structure with high oil absorption capacity. This preliminary crystallization ensures that the oil absorption properties are established before the particle size enlargement process, resolving the contradiction between maintaining high oil absorption and achieving large particle size for better handleability

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent employs parameter changes by controlling the spray-drying conditions (inlet temperature, outlet temperature, feed rate) to transform the hydrothermally treated slurry into large-particle powder. By optimizing these parameters, the process achieves particle size enlargement while preserving the gyrolite crystal structure's oil absorption capacity, thus resolving the contradiction between particle size and oil absorption

Inventive Principle:
Principle #35Parameter changes

2Ease of operation

If granulation is performed to increase particle size, then handleability improves, but particle strength decreases and disintegration occurs

Engineering Contradiction:
ImprovehandleabilityVSAvoidparticle strength
Core Design Contradiction:
Ease of operationVSStrength

Solution Approach 1:

The patent replaces the mechanical granulation process with a spray-drying process that uses fluid dynamics and rapid evaporation to form particles. This substitution eliminates the mechanical compression and tumbling that cause particle densification and strength loss, while still achieving large particle size and improved handleability through controlled droplet formation and drying

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

Solution Approach 2:

The patent utilizes phase transitions in the spray-drying process, where the slurry undergoes rapid evaporation of water from liquid to vapor phase, forming solid particles. This phase transition approach creates particles with porous structures that maintain strength while achieving large size, resolving the contradiction between particle size and particle strength

Inventive Principle:
Principle #36Phase transitions

3Quantity of substance

If granulated material is produced with priority on oil absorption, then high oil absorption is achieved, but particle strength is insufficient and granules disintegrate

Engineering Contradiction:
Improveoil absorptionVSAvoidparticle strength
Core Design Contradiction:
Quantity of substanceVSStrength

Solution Approach 1:

The patent applies preliminary action by completing the hydrothermal treatment to form gyrolite crystals with high oil absorption capacity before the spray-drying step. This ensures that the oil absorption properties are fully developed in the crystal structure before particle size enlargement, preventing disintegration while maintaining high oil absorption

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent creates a composite structure where the gyrolite crystal framework provides both high oil absorption capacity and structural strength. The spray-drying process preserves this composite structure by forming particles that maintain the internal gyrolite morphology, thus achieving both high oil absorption and sufficient particle strength

Inventive Principle:
Principle #40Composite materials

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 resulting powder exhibits excellent handleability, flowability, and maintains particle size with high oil absorption and strength, suitable for various applications including drug additives and cosmetics, reducing dusting and improving overall performance.

Implementation Method 1

subjecting an aqueous slurry containing the reaction product to a hydrothermal synthesis reaction to obtain gyrolite-type calcium silicate

Methodology Applied
Scientific EffectHydrothermal synthesis:

Implementation Method 2

spray-drying a dispersion liquid containing the gyrolite-type calcium silicate to obtain a gyrolite-type calcium silicate powder

Methodology Applied
Scientific EffectSpray-drying:

Data Source

PatentEP3067316B1Powdered gyrolite-type calcium silicate having high oil absorbency and large particle diameter, and production method therefor
Publication Date: 2024.11.06 TOMITA PHARMACEUTICAL CO LTD
  • EP3067316B1 patent drawingFigure 1~3
  • EP3067316B1 patent drawingFigure 4~6
  • EP3067316B1 patent drawing

AI summary

Provided is powdered gyrolite-type calcium silicate that has a relatively large particle size, yet is endowed with both a high oil absorption and a high particle strength. The powdered gyrolite-type calcium silicate has (1) an oil absorption of at least 2.8 mL/g, (2) an average particle diameter of at least 40 µm, and (3) in treatment where the gyrolite-type calcium silicate is charged into a laser diffraction-type particle size analyzer within the range of a diffraction volume of from 0.1 to 0.6 and circulated at a flow rate of 32.5 mL/s for 5 minutes, a percent change in average particle diameter following treatment with respect to average particle diameter before treatment of 15% or less.