Propylene Production via Dehydrogenation Effluent and Offgas Merging

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Solution Overview

Problem

Current processes for producing propylene from paraffins, such as propane, face challenges in increasing production rates while minimizing additional equipment and costs to meet growing demand for polypropylene.

Innovation Solution

A process that combines an effluent stream from a paraffin dehydrogenation reactor with an offgas stream containing propane to form a combined effluent stream, which is then separated into a propylene product stream and a propane-rich recycle stream, with the latter being reintroduced into the reactor to enhance propylene production, along with a butane isomerization process to generate additional propane for conversion.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional propylene production processes are used, then propylene is produced from paraffin dehydrogenation, but production rates are limited and additional equipment is required to increase output

Engineering Contradiction:
Improvepropylene production rateVSAvoidadditional equipment required
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent combines the dehydrogenation reactor effluent stream with an isomerization unit offgas stream that contains propane. By merging these two streams, the process utilizes existing equipment from both units to increase propylene production without requiring separate additional conversion equipment. The combined stream is then separated to recover propylene and recycle propane, creating an integrated system that maximizes output from available infrastructure.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The patent recovers propane from the isomerization unit offgas stream that would otherwise be discarded or underutilized. This recovered propane is combined with the dehydrogenation effluent and recycled back to the reactor, effectively converting a waste or low-value stream into a valuable feedstock that increases propylene production without requiring additional fresh feed input.

Inventive Principle:
Principle #34Discarding and recovering

2Quantity of substance

If more propane feed is added to increase propylene output, then production increases, but additional processing capacity and equipment are required

Engineering Contradiction:
Improvepropane conversion quantityVSAvoidprocess complexity and cost
Core Design Contradiction:
Quantity of substanceVSEase of manufacture

Solution Approach 1:

The patent makes the isomerization unit offgas stream serve a dual function: its primary function remains supporting the isomerization process, and its secondary function becomes a source of additional propane feedstock for the dehydrogenation reactor. This multi-functional use of existing process streams increases propane conversion quantity without requiring dedicated additional feed handling or processing equipment.

Inventive Principle:
Principle #6Universality (Multi-functionality)

Solution Approach 2:

The process uses its own internal offgas stream from the isomerization unit to supplement the dehydrogenation feed requirement. By recycling and reutilizing material already present within the process system, the plant serves its own feed needs without requiring external additional feedstock input or associated processing infrastructure.

Inventive Principle:
Principle #25Self-service

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 increases propylene production by providing more propane for conversion within the dehydrogenation reactor, thereby enhancing output without requiring significant additional equipment or costs, thus addressing the demand for polypropylene production efficiently.

Implementation Method 1

catalytic dehydrogenation of paraffins such as propane

Methodology Applied
Scientific EffectCatalytic dehydrogenation: Catalysis

Implementation Method 2

n-butane to iso-butane in a butane isomerization process

Methodology Applied
Scientific EffectIsomerization: Catalysis

Data Source

PatentUS9051230B2Processes for producing propylene from paraffins
Publication Date: 2015.06.09 UOP LLC
  • US9051230B2 patent drawing
  • US9051230B2 patent drawing
  • US9051230B2 patent drawing

AI summary

Embodiments of processes for producing propylene from paraffins are provided. The process comprises the steps of combining an effluent that comprises propylene and propane from a paraffin dehydrogenation reactor with an offgas stream that comprises propane to form a combined effluent stream. The combined effluent stream is separated into a propylene product stream and a propane-rich recycle stream. The propane-rich recycle stream is introduced to the paraffin dehydrogenation reactor operating at dehydrogenation conditions to convert propane in the propane-rich recycle stream to propylene.