Plant Oil Extraction System with Temperature Control

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Solution Overview

Problem

Current plant oil extraction methods are complex and costly, requiring solvent mixing and high temperatures, making them unsuitable for non-industrial settings like cosmetics laboratories or consumer use, and there is a need for a simpler, more efficient process that maintains the solvent at a cooler temperature for optimal extraction.

Innovation Solution

A plant oil extraction system comprising an extraction vessel, a separator vessel, and an expansion filter, using hydrocarbon solvents with a computer-based temperature control assembly to regulate the solvent temperature between 25-degrees Fahrenheit and 30-degrees Fahrenheit, optimizing oil extraction efficiency and solvent recovery.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If high temperatures are used in extraction, then oil extraction efficiency is improved, but energy consumption increases and solvent denaturation occurs

Engineering Contradiction:
Improveoil extraction efficiencyVSAvoidenergy consumption
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The patent changes the temperature parameter from high temperature to lower temperature range (25-30°F for solvent, extraction temperature maintained below solvent boiling point), achieving optimal extraction efficiency while reducing energy consumption and preventing solvent denaturation

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent utilizes phase transition of hydrocarbon solvent from liquid to gas state during extraction, then condenses it back to liquid for recovery and recycling, enabling efficient extraction at lower temperatures with complete solvent recovery

Inventive Principle:
Principle #36Phase transitions

2Productivity

If complex solvent mixing processes are used, then extraction efficiency is improved, but operational complexity increases

Engineering Contradiction:
Improveextraction efficiencyVSAvoidoperational complexity
Core Design Contradiction:
ProductivityVSEase of operation

Solution Approach 1:

The patent extracts and eliminates the complex solvent mixing step from the traditional extraction process, using a single hydrocarbon solvent that naturally achieves optimal extraction efficiency without requiring mixing with other solvents

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The hydrocarbon solvent performs multiple functions automatically: it extracts oil from plant material, then through phase transition and condensation, purifies itself and is recovered for recycling, eliminating the need for complex external processing

Inventive Principle:
Principle #25Self-service

3Productivity

If traditional extraction methods are used, then oil extraction is achieved, but solvent recovery and recycling are insufficient

Engineering Contradiction:
Improveoil extractionVSAvoidsolvent recovery
Core Design Contradiction:
ProductivityVSLoss of substance

Solution Approach 1:

The patent employs phase transition of the hydrocarbon solvent from liquid to gas during extraction, then condenses the gas back to liquid in a condenser, achieving complete solvent recovery and enabling continuous recycling with minimal loss

Inventive Principle:
Principle #36Phase transitions

Solution Approach 2:

Instead of discarding the solvent after extraction, the patent recovers it through condensation of vapor and implements a recycling system that returns the condensed solvent to the extraction vessel for continuous use

Inventive Principle:
Principle #34Discarding and recovering

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 system enables efficient and cost-effective plant oil extraction in non-industrial settings by maintaining a cooler solvent temperature, enhancing oil recovery and reducing energy consumption while minimizing solvent exposure and operational complexity.

Implementation Method 1

A cooling device is operationally connected to the extraction vessel and the computer-based temperature control assembly, allowing cooling of the liquid solvent admitted into the extractor vessel to a temperature between 25-degrees Fahrenheit and 30-degrees Fahrenheit

Methodology Applied
Scientific EffectCooling: Cooling

Implementation Method 2

A separator thermal jacket envelopes the separator vessel and receives heating medium therein, which causes vaporization of the solvent during the plant oil separation process

Methodology Applied
Scientific EffectVaporization: Evaporation

Implementation Method 3

A solvent expansion filter is mounted downstream of the separator vessel, filtering the solvent before it is re-circulated in the system. An upright stand supports the extraction vessel, the separator vessel, and the expansion filter vessel

Methodology Applied
Scientific EffectHeating: Heating

Data Source

PatentUS9687754B2Apparatus for extracting oil from oil-bearing plants
Publication Date: 2017.06.27 PINNACLE STAINLESS LLC
  • US9687754B2 patent drawing
  • US9687754B2 patent drawing
  • US9687754B2 patent drawing

AI summary

A system for extracting oil from oil-bearing plant parts has an extraction vessel supported by an upright stand, a separator vessel mounted below the extraction vessel, and an expansion filter vessel mounted downstream from the separator vessel. A source of hydrocarbon solvent supplies liquid gas to the top of the extraction vessel, while a recycling pump connected to the separator vessel facilitates transport of the solvent through the plant material in the extraction vessel. The solvent is recovered and re-circulated, while extracted oil is removed from the separator. A computer-based temperature control assembly having a cooling device and a jacketed injection coil regulates temperature of the solvent delivered to the extraction assembly. A thermal jacket is mounted on each of the separator vessel and the expansion filter vessel, with the thermal jackets supplying heat and cold to the interior of the separator vessel and the expansion filter vessel and helping evaporate and condense the solvent.