Two-Stage Reactor for Water-Free Hydrocarbon Production

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Solution Overview

Problem

Current methods fail to efficiently separate water from ethanol in aqueous solutions before reacting over microporous zeolite catalysts, leading to dealumination and reduced catalyst stability in the production of liquid hydrocarbons, and there is no effective method for converting low-energy dense aqueous biomass chemicals to water-free hydrocarbons.

Innovation Solution

A two-stage reactor system using a solid acid catalyst composed of microporous aluminosilicates mixed with silicon carbide binder, where the first reactor converts ethanol to ethylene gas and water, and the second reactor, with water removal via a condenser, produces water-free liquid hydrocarbons, preventing catalyst deactivation and enhancing yield.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If water is not removed from aqueous ethanol before reacting over microporous zeolite catalyst, then the conversion process can proceed continuously, but the catalyst undergoes dealumination and deactivation

Engineering Contradiction:
Improvecontinuous conversionVSAvoidcatalyst stability
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent divides the conversion process into two separate reactors: the first reactor performs dehydration of ethanol to ethylene, while the second reactor performs oligomerization of ethylene to liquid hydrocarbons. This segmentation allows water to be managed in the first reactor without affecting the catalyst in the second reactor, enabling continuous operation while preventing catalyst deactivation.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent extracts water from the reaction stream by condensing it between the first and second reactors. This removal of water prevents it from reaching the microporous zeolite catalyst in the second reactor, thereby preventing dealumination and maintaining catalyst stability while allowing continuous processing of aqueous feedstock.

Inventive Principle:
Principle #2Taking out (Extraction)

2Reliability

If pre-concentration of ethanol is performed before reaction, then catalyst performance is maintained, but the process complexity and energy consumption increase

Engineering Contradiction:
Improvecatalyst performanceVSAvoidprocess complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

By segmenting the process into two reactors with water removal between them, the patent eliminates the need for pre-concentration steps. The first reactor handles the aqueous feedstock and separates water, while the second reactor receives dry ethylene gas, maintaining catalyst performance without requiring complex pre-treatment equipment.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The first reactor performs self-service by converting aqueous ethanol to ethylene gas and water, with the water automatically condensing and separating. This self-drying function eliminates the need for external pre-concentration equipment, reducing process complexity while maintaining catalyst performance in the second reactor.

Inventive Principle:
Principle #25Self-service

3Object-affected harmful factors

If aqueous biomass chemicals are converted directly to hydrocarbons, then the environmental impact is reduced, but water removal becomes a major challenge

Engineering Contradiction:
Improveenvironmental impactVSAvoidwater removal challenge
Core Design Contradiction:
Object-affected harmful factorsVSDevice complexity

Solution Approach 1:

The patent segments the conversion process to handle water management in the first reactor through condensation and separation, then feeds the dried ethylene gas to the second reactor. This segmentation provides a straightforward water removal solution that enables direct conversion of aqueous biomass chemicals to hydrocarbons with minimal environmental impact.

Inventive Principle:
Principle #1Segmentation

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 process effectively converts low-energy dense aqueous oxygenates to high-yield water-free liquid hydrocarbons, increasing the longevity of the catalyst and eliminating the need for pre-concentrating ethanol, thus improving the efficiency and sustainability of liquid hydrocarbon production.

Implementation Method 1

removing the water with a condenser between the first reactor and second reactor

Methodology Applied
Scientific EffectCondensation: Condensation

Implementation Method 2

converting a feedstock of an aqueous solution of an oxygen containing organic compound to ethylene gas and water

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 3

converting ethanol to ethylene gas and water

Methodology Applied
Scientific EffectDehydration:

Implementation Method 4

converting the ethylene gas to one or more liquid hydrocarbons

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS10913902B2Production of high energy-dense liquid hydrocarbon from low energy-dense aqueous solutions of oxygen containing organic compound(s)
Publication Date: 2021.02.09 UNITED STATES OF AMERICA THE AS REPRESENTED BY THE SEC OF THE ARMY
  • US10913902B2 patent drawing
  • US10913902B2 patent drawing
  • US10913902B2 patent drawing

AI summary

Methods to convert an oxygen containing organic compound(s) to one or more water-free liquid hydrocarbons products. They make use of a catalytic process in a two-stage reactor system having a first reactor and a second reactor in series. Process design is described for effective conversion of aqueous low energy-dense aqueous solutions containing oxygen containing organic compound(s) to liquid hydrocarbons; the process design preferably employs the solid acid catalysts comprised of microporous aluminosilicates denoted as zeolites mixed with silicon carbide binder in series of two reactor system with capability of complete water removal.