Flash Cooling Pretreated Biomass Slurry

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

The challenge in the production of second-generation biofuels from lignocellulosic biomass lies in efficiently cooling high consistency slurries post-pretreatment, as conventional methods require large, expensive equipment and excessive water usage, leading to increased energy costs and operational complexities.

Innovation Solution

A method involving the mixing of pretreated biomass with a cooling liquid to reduce viscosity, followed by solid-liquid separation, where the liquid stream is recycled and used to cool the biomass, thereby reducing the need for large equipment and water, and facilitating the use of standard pumps and piping.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Temperature

If conventional cooling methods are used for high consistency slurries, then cooling effectiveness is improved, but equipment size and cost increase significantly

Engineering Contradiction:
Improvecooling effectivenessVSAvoidequipment size
Core Design Contradiction:
TemperatureVSVolume of stationary object

Solution Approach 1:

The patent introduces a two-stage cooling approach where flash cooling acts as an intermediary step between pretreatment and final cooling. The slurry first undergoes rapid flash cooling to reduce temperature significantly, then proceeds to a second cooling stage. This intermediary flash cooling step enables the overall system to achieve effective cooling without requiring a single oversized heat exchanger.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Temperature

If conventional cooling methods are used for high consistency slurries, then cooling effectiveness is improved, but water usage increases excessively

Engineering Contradiction:
Improvecooling effectivenessVSAvoidwater usage
Core Design Contradiction:
TemperatureVSQuantity of substance

Solution Approach 1:

The patent utilizes flash cooling where high consistency slurry undergoes rapid phase change and temperature reduction. The slurry is flashed from pressurized conditions to atmospheric or reduced pressure, causing immediate cooling through adiabatic expansion and partial vaporization. This phase transition-based cooling achieves significant temperature reduction with minimal water addition, as the cooling energy comes from the slurry's own pressure energy rather than large volumes of cooling water.

Inventive Principle:
Principle #36Phase transitions

3Temperature

If high consistency slurry is cooled using conventional methods, then cooling is achieved, but energy consumption increases

Engineering Contradiction:
Improvecooling achievementVSAvoidenergy consumption
Core Design Contradiction:
TemperatureVSLoss of energy

Solution Approach 1:

The patent converts the high pressure energy present in the pretreated slurry into useful cooling energy through flash cooling. The pressurized slurry from the pretreatment reactor is directly flashed to lower pressure without intermediate pressure reduction steps, transforming the pressure energy into thermal energy reduction. This approach turns what would otherwise be wasted pressure energy into the driving force for cooling, significantly reducing external energy input requirements.

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

4Productivity

If high consistency slurry is processed, then pretreatment effectiveness is improved, but pumping and handling become more difficult

Engineering Contradiction:
Improvepretreatment effectivenessVSAvoidpumping and handling
Core Design Contradiction:
ProductivityVSEase of operation

Solution Approach 1:

The patent performs flash cooling as a preliminary action immediately after pretreatment and before the slurry enters pumping and handling systems. By reducing the temperature and adjusting the consistency of the slurry through flash cooling first, the subsequent pumping and handling operations become significantly easier. The slurry becomes less viscous and more pumpable after the flash cooling step, eliminating the need for specialized high-consistency pumping equipment.

Inventive Principle:
Principle #10Preliminary action

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

This approach allows for efficient cooling of high consistency slurries, reducing energy consumption and operational costs, while enabling the use of standard equipment and minimizing water usage, thus enhancing the overall efficiency of the biofuel production process.

Implementation Method 1

mixing the discharged pretreated biomass with a cooling liquid to form a slurry

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Implementation Method 2

pumping the slurry to a solid-liquid separator, said solid-liquid separator for providing a first stream comprising a liquid component of the slurry and a second other stream comprising a solid component of the slurry

Methodology Applied
Scientific EffectCentrifugal separation: Centrifugal Separation

Data Source

PatentUS10889795B2System and method for cooling pretreated biomass
Publication Date: 2021.01.12 IOGEN ENERGY CORP
  • US10889795B2 patent drawing
  • US10889795B2 patent drawing
  • US10889795B2 patent drawing

AI summary

Discharging pretreated biomass from a pretreatment reactor and mixing the discharged pretreated biomass with a cooling liquid in a vessel provides a cooled slurry having a consistency that is less than about 12 wt %. Since the consistency is relatively low, the cooled slurry may be pumped to a higher elevation using standard pumping equipment. At the higher elevation, the cooled slurry may be separated into a first stream comprising a liquid component of the slurry and a second other stream comprising a solid component of the slurry (e.g., having a consistency between about 15 wt % and 40 about wt %). The solid component may be fed to an inlet of a hydrolysis reactor, while the liquid component may be fed to a cooling system that provides a cooled stream. The cooled stream may then be cycled back to the vessel.