Biofuel Production via Two-Stage Pressurization and Heat Integration

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Solution Overview

Problem

Current biofuel production faces social, economic, environmental, and technical challenges, including the 'food vs fuel' debate, carbon emissions, deforestation, soil erosion, and inefficiencies in energy balance and resource utilization, necessitating an alternative source and process for biofuel production.

Innovation Solution

A system and process utilizing a two-stage pressurization and heat exchanger system to convert biomass, sludge, or wastewater into biofuel, involving pressurization up to 250 bar, heating to 400 °C, and subsequent separation to produce a high-conversion rate of biofuel, with heat integration and efficient energy recovery.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If conventional biofuel production methods are used, then biofuel can be produced from traditional sources, but environmental issues such as deforestation, soil erosion, and biodiversity loss occur

Engineering Contradiction:
Improvebiofuel productionVSAvoidenvironmental damage
Core Design Contradiction:
Quantity of substanceVSObject-affected harmful factors

Solution Approach 1:

The patent changes the fundamental parameter of feedstock source from agricultural biomass to municipal solid waste, transforming the input material composition to eliminate environmental harm while maintaining biofuel production output

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent converts harmful municipal solid waste into beneficial biofuel, transforming an environmental problem into a renewable energy solution that simultaneously reduces waste accumulation and provides clean energy

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

2Productivity

If single-stage pressurization is used, then the system is simpler, but the conversion efficiency and energy recovery are insufficient

Engineering Contradiction:
Improvebiofuel conversion rateVSAvoidsystem structure
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent segments the pressurization process into two distinct stages with different pressure levels (first stage: lower pressure, second stage: higher pressure up to 250 bar), allowing optimized conversion efficiency while maintaining manageable system complexity through modular design

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent implements dynamic pressure adjustment through two-stage pressurization, enabling the system to adapt pressure levels to different processing requirements and maximize conversion efficiency at each stage

Inventive Principle:
Principle #15Dynamics

3Productivity

If high pressure and temperature are applied, then conversion rate increases, but energy consumption increases

Engineering Contradiction:
Improveconversion rateVSAvoidenergy consumption
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The patent implements a heat exchanger system that captures thermal energy from the high-temperature output stream and feeds it back to preheat the incoming feedstock, creating a feedback loop that reduces external energy input while maintaining high conversion rates

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The patent recovers thermal energy that would otherwise be discarded from the high-temperature process output, utilizing heat exchangers to capture and reuse this energy for preheating incoming material, thereby reducing overall energy consumption

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 process achieves a high conversion rate of starting materials to biofuel, utilizing inexpensive and readily available feedstocks, enhancing energy recovery and operational stability, while being environmentally friendly and cost-effective.

Implementation Method 1

a first heat exchanger (104) adapted for receiving the second pressurized feed from the high pressure pump (103) and pre-heating the second pressurized feed

Methodology Applied
Scientific EffectHeat exchange: Heat Exchanger

Implementation Method 2

The reaction vessel (106) is adapted for receiving the heated feed from the second heat exchanger (105) and reforming the heated feed

Methodology Applied
Scientific EffectReforming: Pyrolysis

Implementation Method 3

a precipitation vessel (107) adapted for receiving the slurry from the reaction vessel (106) and separating the solids (b) from the slurry

Methodology Applied
Scientific EffectPrecipitation: Precipitation

Implementation Method 4

a gas-liquid separator (111) adapted for receiving the gas-liquid mixture from the second pressure let-down station (110) and separating gases (111A) from the gas-liquid mixture

Methodology Applied
Scientific EffectGas-liquid separation: Cyclone Separation

Implementation Method 5

a biofuel separator (112) adapted for receiving the mixture (111B) comprising biofuel and non-reformed feed, from the gas-liquid separator (111) and separating the non-reformed feed (112B) from the mixture to obtain the biofuel (112A)

Methodology Applied
Scientific EffectLiquid-liquid separation: Liquid-Liquid Extraction

Data Source

PatentEP3352928B1System and process for production of biofuel
Publication Date: 2023.01.11 RELIANCE IND LTD
  • EP3352928B1 patent drawingFigure 1

AI summary

The present disclosure relates to a system and a process for producing biofuel. The system comprises at least one feed tank; a low pressure pump; a high pressure pump; a first heat exchanger; a second heat exchanger; a reaction vessel; a precipitation vessel; a first pressure let-down station; a third heat exchanger; a second pressure let-down station; a gas-liquid separator; and a biofuel separator. The process comprises pressurizing and heating a feed, followed by reforming the pressurized and heated feed to obtain a slurry. The solids are separated from the slurry by precipitation to obtain a mixture comprising biofuel and the non- reformed feed. The mixture is then cooled and de-pressurized, followed by separation of 0 gases and the non-reformed feed to obtain the biofuel. The system and process of the present disclosure can be used to produce biofuel from diverse, easily available and inexpensive starting material.