PHA Filtration via pH and Density Control

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Solution Overview

Problem

Existing PHA production methods face challenges with low filtrate permeability and high leakage ratios during filtration, which inefficiencies require significant energy for water evaporation and result in impurities remaining in the final product.

Innovation Solution

A novel PHA production method that controls the pH of the aqueous PHA suspension, air permeability of the filter medium, amount of PHA surface adhesion protein, and liquid density to achieve specific filtrate permeability and leakage ratios, enabling efficient filtration.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional filtration methods are used for PHA production, then the filtration process can be completed, but the filtrate permeability is low and the leakage ratio is high

Engineering Contradiction:
Improvefiltrate permeabilityVSAvoidleakage ratio
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent applies parameter changes by precisely controlling the pH of the aqueous PHA suspension (2.5-5.5), the air permeability of the filter medium (0.01-5.0 cc/cm2/sec), the amount of PHA surface adhesion protein (not more than 2,000 ppm), and the liquid density (0.50-1.08 g/mL). These parameter optimizations enable the filtration process to achieve both high filtrate permeability (at least 200 L/m2/hr) and low leakage ratio (no more than 5%), resolving the technical contradiction between productivity and manufacturing precision.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If filtration is performed with poor efficiency, then the filtration process can be completed, but significant energy is required for water evaporation

Engineering Contradiction:
Improvefiltration efficiencyVSAvoidenergy consumption for water evaporation
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

By optimizing the parameters (pH, air permeability, protein content, liquid density) to achieve efficient filtration with high filtrate permeability and low leakage ratio, the patent reduces the amount of water that needs to be evaporated to achieve the desired PHA purity. This directly decreases the energy consumption for water evaporation while maintaining high filtration efficiency.

Inventive Principle:
Principle #35Parameter changes

3Productivity

If conventional filtration is used, then the filtration process can be completed, but impurities remain in the final product

Engineering Contradiction:
Improvefiltration completionVSAvoidproduct purity
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent controls the pH (2.5-5.5), air permeability (0.01-5.0 cc/cm2/sec), PHA surface adhesion protein content (not more than 2,000 ppm), and liquid density (0.50-1.08 g/mL) to achieve optimal filtration conditions. These parameter optimizations enable the filtration process to effectively separate PHA from impurities, achieving both filtration completion and high product purity (leakage ratio of no more than 5%).

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

The method achieves efficient filtration with a filtrate permeability of at least 200 L/m2/hr and a leakage ratio of no more than 5%, reducing energy consumption and improving the purity of the PHA product.

Implementation Method 1

a filtration step of subjecting, to dead-end filtration, an aqueous PHA suspension

Methodology Applied
Scientific EffectFiltration: Filter (physical)

Data Source

PatentUS20250051518A1Method for producing polyhydroxyalkanoate and use of same
Publication Date: 2025.02.13 KANEKA CORP
  • US20250051518A1 patent drawing

AI summary

An object is to provide a PHA production method which enables efficient filtration. The above problem is solved by providing a PHA production method including a filtration step of subjecting, to dead-end filtration, an aqueous PHA suspension having a pH of 2.5 to 5.5 with use of a filter medium having an air permeability of 0.01 cc/cm2/sec to 5.0 cc/cm2/sec, the aqueous PHA suspension containing PHA surface adhesion protein in an amount of not more than 2,000 ppm, the aqueous PHA suspension having a liquid density of 0.50 g/mL to 1.08 g/mL in the filtration step.