Low-Iron Hydrous Phospholipids From Soybean Oil Sediments

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Solution Overview

Problem

Existing methods for processing soybean oil sediments into phospholipids face challenges such as low acetone-insoluble content, inability to remove iron ions, and difficulties in industrial-scale production, leading to environmental pollution and food safety hazards.

Innovation Solution

A hydration method involving soaking soybean oil sediments in water, followed by centrifugal sedimentation and static stratification, to produce low-iron hydrous phospholipids with high acetone-insoluble content and minimal metal salts, which are then processed into low-iron powdered phospholipids without solvents.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If conventional hydration method is used to prepare concentrated phospholipids, then production cost is reduced, but acetone-insoluble content is too low (60-65 g/100 g) and iron ions cannot be removed

Engineering Contradiction:
Improveacetone-insoluble contentVSAvoidiron ion content
Core Design Contradiction:
Quantity of substanceVSObject-affected harmful factors

Solution Approach 1:

The patent extracts and removes phospholipid metal salts (particularly iron ions) from the hydration system through centrifugal separation. The metal salts precipitate during hydration and are separated by centrifugation, achieving removal of harmful iron ions while maintaining high acetone-insoluble content of 93-97 g/100 g

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent optimizes hydration parameters including water-to-sediment ratio (2:1 to 4:1), hydration temperature (60-95°C), and hydration time (2-6 hours) to control the hydration process. These parameter changes enable simultaneous achievement of high phospholipid extraction, metal salt precipitation, and high acetone-insoluble content

Inventive Principle:
Principle #35Parameter changes

2Quantity of substance

If solvent extraction method is used to prepare powder phospholipids, then acetone-insoluble content is high (95-98 g/100 g), but production cost increases and environmental pollution occurs

Engineering Contradiction:
Improveacetone-insoluble contentVSAvoidproduction cost
Core Design Contradiction:
Quantity of substanceVSEase of manufacture

Solution Approach 1:

The patent replaces the chemical solvent extraction method with a physical hydration-centrifugation system. Water is used as the hydrating agent instead of organic solvents, and centrifugal force replaces chemical extraction. This substitution achieves comparable acetone-insoluble content (93-97 g/100 g) without the environmental pollution and high costs associated with solvent methods

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

Solution Approach 2:

The patent changes the fundamental parameter of the extraction system from organic solvent to water-based hydration. By controlling hydration temperature, water ratio, and time, the method achieves high phospholipid purity and acetone-insoluble content through physical-chemical hydration rather than chemical extraction

Inventive Principle:
Principle #35Parameter changes

3Device complexity

If conventional hydration method is used, then production process is simple, but iron ions remain in the product and acetone-insoluble content is insufficient

Engineering Contradiction:
Improveprocess complexityVSAvoidacetone-insoluble content
Core Design Contradiction:
Device complexityVSQuantity of substance

Solution Approach 1:

The patent merges the hydration process with metal salt precipitation and centrifugal separation into an integrated system. The hydration step simultaneously extracts phospholipids and precipitates metal salts, which are then separated by centrifugation in the same continuous process flow, achieving high acetone-insoluble content without significantly increasing process complexity

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The patent implements a continuous process where hydration, precipitation, and centrifugal separation occur in sequence without interruption. The hydration mixture is directly centrifuged after the hydration period, and the supernatant is processed continuously, maintaining high acetone-insoluble content through uninterrupted separation of phospholipids from metal salts

Inventive Principle:
Principle #20Continuity of useful action

4Ease of manufacture

If conventional hydration method is used, then production cost is low, but the method is difficult to popularize due to food safety hazards from iron ions

Engineering Contradiction:
Improveproduction costVSAvoidfood safety
Core Design Contradiction:
Ease of manufactureVSReliability

Solution Approach 1:

The patent extracts and removes phospholipid metal salts through centrifugal separation after hydration. The metal salts precipitate during the hydration process and are separated by centrifugation, achieving removal of harmful iron ions to less than 18 mg/kg while maintaining low production cost and high food safety

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent converts the harmful effect of metal ions into a beneficial separation process. The metal ions that would normally contaminate the product are utilized as precipitation agents during hydration, forming separable phospholipid metal salts that can be removed by centrifugation, thus transforming a food safety hazard into an effective separation mechanism

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

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 high acetone-insoluble content (92.5-95.5 g/100 g) and low iron content (≤18 mg/kg), suitable for industrial production, eliminating environmental pollution and food safety risks while reducing production costs.

Implementation Method 1

The main components of the low-iron water-containing phospholipid are phospholipids, oil and water; wherein the water content is 70-80 g/100 g

Methodology Applied
Scientific EffectAbsorption (physical): Absorption (physical)

Implementation Method 2

centrifugal sedimentation and static stratification, to produce low-iron hydrous phospholipids

Methodology Applied
Scientific EffectCentrifugal separation: Centrifugal Separation

Implementation Method 3

centrifugal sedimentation and static stratification

Methodology Applied
Scientific EffectSedimentation: Sedimentation

Data Source

PatentUS12473311B2Low iron hydrous phospholipid and method for separating low-iron hydrous phospholipids from soybean oil sediments
Publication Date: 2025.11.18 SHANGHAI BOBEYMAN TECH CO LTD
  • US12473311B2 patent drawing
  • US12473311B2 patent drawing
  • US12473311B2 patent drawing

AI summary

The invention belongs to the technical field of phospholipid processing, in particular to a low-iron hydrous phospholipid and a method for separating low-iron hydrous phospholipids from soybean oil sediments. The main components of low-iron water-containing phospholipids are phospholipids, oil and water; its water content is 70-80 g/100 g; on a dry basis, the content of acetone-insoluble matter is 92.5-95.5 g/100 g; in terms of acetone-insoluble matter, the iron content is less than or equal to 18 mg/kg. The low-iron water-containing phospholipid of the present invention is prepared from soybean oil by a hydration method, and is used to solve the defects of low acetone-insoluble content of the water-containing phospholipid, inability to remove iron ions and the industry's long-term dependence on the solvent method to prepare the powdered phospholipid; At the same time, the method solves the technical problem that “the preparation of powder phospholipid by hydration method cannot realize industrial production”.