Hydrocarbon Separation Unit with Reflux for Impurity Removal

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Solution Overview

Problem

Existing processes for producing hydrocarbons, such as jet fuel, from renewable and fossil sources face challenges in reducing impurities like H2S, H2O, NH3, and CO2, which can contaminate noble metal catalysts used in the dewaxing step, particularly when using feedstocks from renewable sources.

Innovation Solution

A process involving a hydroprocessing step followed by a separation unit with reflux, where the overhead hydrocarbon liquid stream is used as reflux to the separation unit, significantly reducing impurities like H2S and H2O before the dewaxing step, and a single hydrogen recycle loop is used to integrate and simplify the process.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If the overhead hydrocarbon liquid stream is sent directly to the dewaxing step, then the process is simple and continuous, but the noble metal catalysts are contaminated and impaired by impurities such as H2S, H2O, NH3, CO and CO2

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

Solution Approach 1:

The invention applies preliminary action by introducing a separation unit before the dewaxing step to remove impurities (H2S, H2O, NH3, CO, CO2) from the hydrocarbon liquid stream. This preliminary separation prevents catalyst contamination before the catalytic reaction occurs, thereby protecting catalyst performance without requiring complex modifications to the dewaxing unit itself.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The separation unit acts as an intermediary between the hydroprocessing step and the dewaxing step. It mediates the transition by selectively removing harmful impurities while allowing hydrocarbons to pass through, thus protecting the noble metal catalysts from direct contact with contaminants without disrupting the overall process flow.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Reliability

If a separation unit with reflux is introduced to remove impurities, then catalyst protection is improved, but the device complexity and energy consumption increase

Engineering Contradiction:
Improvecatalyst protectionVSAvoidenergy consumption
Core Design Contradiction:
ReliabilityVSUse of energy by stationary object

Solution Approach 1:

The separation unit utilizes phase transitions (condensation and vaporization) to achieve impurity removal. The reflux mechanism relies on condensing vapor phases and returning liquid to the separation unit, leveraging natural phase change thermodynamics to enhance separation efficiency while minimizing additional energy input requirements compared to purely thermal separation methods.

Inventive Principle:
Principle #36Phase transitions

3Manufacturing precision

If multiple separation steps are used to reduce impurities, then manufacturing precision is improved, but productivity decreases due to additional processing time

Engineering Contradiction:
Improveimpurity reductionVSAvoidproduction rate
Core Design Contradiction:
Manufacturing precisionVSProductivity

Solution Approach 1:

The invention segments the impurity removal function into a dedicated separation unit with specific reflux mechanisms, rather than attempting to achieve separation through multiple sequential distillation columns or repeated processing steps. This segmentation allows for optimized single-stage separation that maintains high impurity removal efficiency while minimizing residence time and processing delays.

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 approach results in a substantial reduction of impurities by one order of magnitude, effectively protecting the noble metal catalysts and ensuring the production of high-quality hydrocarbon products like jet fuel and diesel by minimizing contamination.

Implementation Method 1

the overhead stream is partly condensed and the resulting hydrocarbon liquid fraction

Methodology Applied
Scientific EffectCondensation: Condensation

Implementation Method 2

passing the feedstock through one or more catalytic hydrotreating units under the addition of hydrogen

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 3

HDO to obtain a hydrotreated stream

Methodology Applied
Scientific EffectHydrodeoxygenation:

Implementation Method 4

hydrodenitrification (HDN)

Methodology Applied
Scientific EffectHydrodenitrification:

Implementation Method 5

in which hydroisomerization and possibly a side reaction of hydrocracking occurs

Methodology Applied
Scientific EffectHydroisomerization:

Data Source

PatentUS20230357652A1Removing impurities in a process for producing hydrocarbon products
Publication Date: 2023.11.09 HALDOR TOPSOE AS
  • US20230357652A1 patent drawing
  • US20230357652A1 patent drawing

AI summary

Process for producing a hydrocarbon product, said process comprising: i) passing a feedstock originating from a renewable source and/or from a fossil source through a hydroprocessing step for producing a main hydrotreated stream; said hydroprocessing step comprising: passing the feedstock through one or more catalytic hydrotreating units under the addition of hydrogen for producing a first hydrotreated stream; passing the first hydrotreated stream to a first separation step comprising the use of a separation unit for particularly removing the impurities H2S, CO, CO2 and H2O; withdrawing from said first separation step an overhead stream and separating an overhead hydrocarbon liquid stream thereof which is passed as a reflux stream to said first separation unit; withdrawing from said first separation step a bottom stream and passing at least a portion of said bottom stream to a dewaxing step comprising the use of one or more catalytic hydrotreating units under the addition of hydrogen for producing said main hydrotreated stream; and ii) passing the main hydrotreated stream to a second separation step for producing said hydrocarbon product.