Spherical Reactor Inlet Distributor for Uniform Vapor Flow

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Solution Overview

Problem

Reactor inlet designs often result in uneven distribution of vaporous reactants due to higher velocities around bends, leading to hot spots and underutilization of catalyst, which reduces productivity and causes premature catalyst aging.

Innovation Solution

A reactor inlet system with an equalizer section that minimizes obstruction and balances vapor velocities using flange and ring plates, and a distributor section with radial nozzles to ensure uniform vapor distribution across the reactor vessel, reducing pressure drop and enhancing catalyst utilization.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If baffles and vanes are used to create back pressure on the inlet stream, then reactant distribution across the reactor is improved, but pressure drop increases significantly

Engineering Contradiction:
Improvereactant distribution uniformityVSAvoidpressure drop
Core Design Contradiction:
Manufacturing precisionVSStress or pressure

Solution Approach 1:

The inlet distributor is segmented into multiple radial nozzles arranged circumferentially, each delivering reactants to different radial zones of the catalyst bed. This segmentation allows uniform distribution without requiring high back pressure, as each nozzle independently controls flow to its designated zone.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Different radial nozzles are designed with different flow characteristics tailored to local requirements - outer nozzles compensate for lower velocity regions while inner nozzles handle higher velocity regions. This local customization achieves uniform distribution without uniform high pressure drop across the entire inlet.

Inventive Principle:
Principle #3Local quality

2Manufacturing precision

If an inert support bed with thick layer is provided to create tortuous paths, then mixing and back pressure are improved, but reactor volume increases significantly

Engineering Contradiction:
Improvereactant distribution uniformityVSAvoidreactor volume
Core Design Contradiction:
Manufacturing precisionVSVolume of stationary object

Solution Approach 1:

The inert support bed is reduced to a thin layer that performs preliminary distribution function, while the main distribution task is handled by the specially designed radial nozzle system at the inlet. This preliminary action approach eliminates the need for a thick support bed, reducing reactor volume while maintaining distribution quality.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The radial nozzle system acts as an intermediary device between the inlet stream and the catalyst bed, performing the distribution function that would otherwise require a thick inert support bed. This intermediary mechanism achieves uniform distribution with minimal support bed thickness.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Productivity

If higher velocities are allowed to follow the outside of the bend, then flow rate is maintained, but reactant concentration becomes uneven across the reactor

Engineering Contradiction:
Improveflow rateVSAvoidreactant distribution uniformity
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The radial nozzle system provides locally optimized flow distribution - outer nozzles deliver reactants to regions that would otherwise receive excess flow from bend-induced high velocities, while inner nozzles adjust to regions that would receive less flow. This local quality adjustment maintains overall flow rate while achieving uniform distribution.

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The radial nozzle arrangement and flow characteristics are deliberately asymmetric to compensate for the asymmetric velocity profile created by the bend. The nozzle design accounts for the non-uniform velocity distribution, creating a corrected asymmetric pattern that results in uniform overall distribution while maintaining high flow rates.

Inventive Principle:
Principle #4Asymmetry

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

The system achieves a balanced vapor distribution across the reactor, optimizing catalyst usage, increasing productivity, and extending catalyst run time while maintaining low pressure drop.

Implementation Method 1

the equalizer section of the reactor inlet system dampens asymmetrically distributed velocities of vapor entering the reactor inlet to provide the distributor section with a generally symmetrically balanced velocity profile

Methodology Applied
Scientific EffectFluid flow distribution:

Implementation Method 2

the distributor section distributes the flow of vapor outwardly and downwardly from the outlet end of the inlet system such that vapor flow is generally uniform across the reactor vessel

Methodology Applied
Scientific EffectFluid flow distribution:

Data Source

PatentUS10005054B2Combination equalizer and inlet distributor for spherical reactor
Publication Date: 2018.06.26 PHILLIPS 66 CO
  • US10005054B2 patent drawing
  • US10005054B2 patent drawing
  • US10005054B2 patent drawing

AI summary

The invention relates to equalizing and distributing reactants more evenly across the interior space of a reactor vessel utilizing a combination equalizer and distributor at the inlet end that initially impedes with uneven flow rates of vapor and then directs the flow of vapor through a series of circumferential nozzles. The nozzles are physical spaced such that the first nozzle provides the reactants into the vessel to spread radially and broadly outwardly into the vessel and each successive circumferential nozzle to deliver reactants in a less broadly distribution or dispersion where the interior space is filled with reactants without broadly diverse velocities that may create hot spots within the catalyst bed.