Selective Diolefin Hydrogenation in Cracked Naphtha Streams

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Solution Overview

Problem

Diolefins in cracked naphtha and LPG streams from processes like FCC and delayed coking pose challenges due to fouling and catalyst poisoning, requiring an efficient method to remove these contaminants to prevent undesirable conditions in downstream petrochemical applications.

Innovation Solution

A process involving the selective hydrogenation of diolefins in cracked streams before debutanization, using a diolefin hydrogenation reactor in conjunction with fractionation and stripping columns, to produce diolefin-depleted streams that reduce fouling and catalyst poisoning, thereby improving the quality of naphtha and LPG for further processing.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If diolefins are removed from cracked streams using conventional downstream treatment, then fouling and catalyst poisoning are prevented, but process complexity and operational steps increase

Engineering Contradiction:
Improveprevention of fouling and catalyst poisoningVSAvoidprocess configuration
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The patent applies preliminary action by performing diolefin hydrogenation upstream in the debutanizer overhead stream before the stream is separated into naphtha and LPG products. This prevents fouling and catalyst poisoning in downstream applications while avoiding the need for additional downstream treatment steps, thereby reducing overall process complexity

Inventive Principle:
Principle #10Preliminary action

2Reliability

If diolefins are hydrogenated in the liquid cracked stream, then fouling is prevented, but additional hydrogen consumption and processing steps are required

Engineering Contradiction:
Improvestability of cracked streamVSAvoidhydrogen consumption
Core Design Contradiction:
ReliabilityVSUse of energy by moving object

Solution Approach 1:

The patent extracts the diolefin hydrogenation step from the conventional downstream treatment sequence and relocates it to the debutanizer overhead stream. By targeting specifically the diolefin-containing overhead fraction rather than treating the entire cracked stream, hydrogen consumption is reduced while still preventing fouling and catalyst poisoning in the final naphtha and LPG products

Inventive Principle:
Principle #2Taking out (Extraction)

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 effectively eliminates the need for additional hydrotreatment, prevents polymerization fouling, and ensures the diolefin-depleted streams can be stored without gum formation, enhancing the stability and usability of cracked naphtha and LPG in downstream applications.

Implementation Method 1

selectively hydrogenating diolefins in the liquid, cracked stream to provide a diolefin depleted, liquid cracked stream

Methodology Applied
Scientific EffectHydrogenation: Hydrogenation

Implementation Method 2

The cracked stream is fractionated to provide a liquid, cracked stream

Methodology Applied
Scientific EffectFractionation: Fractionation

Implementation Method 3

The cracked stream is subsequently stripped to remove dry gas from the liquid, cracked stream

Methodology Applied
Scientific EffectStripping:

Implementation Method 4

The stripped, liquid cracked stream is debutanized to provide a naphtha stream and an LPG stream

Methodology Applied
Scientific EffectDistillation: Distillation

Data Source

PatentUS10519388B2Process and apparatus for selectively hydrogenating diolefins
Publication Date: 2019.12.31 UOP LLC
  • US10519388B2 patent drawing
  • US10519388B2 patent drawing

AI summary

The present invention discloses a process and apparatus for selectively hydrogenating diolefins in a cracked stream. The method combines a conversion unit and a recovery section. The recovery section includes the diolefin hydrogenation reactor that is used to selectively hydrogenate the diolefins in the cracked naphtha. The diolefin depleted naphtha may be debutanized to separate the stabilized naphtha and liquefied petroleum gas streams.