Multi-Channel Adsorption Tower for Longer Paths and In-Situ Regeneration

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Solution Overview

Problem

Existing adsorption towers face issues such as nonuniform adsorbent distribution, short adsorption path, frequent adsorbent replacement, high heat loss, and inefficient utilization of adsorbent due to simple stacking and harsh operating conditions.

Innovation Solution

A multi-channel adsorption tower design with tray and partition assemblies, ceramic balls, and graded alumina adsorbent particles, combined with low-temperature liquid flushing and nitrogen purge for desorption regeneration, to extend adsorption path and improve adsorption efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Length of moving object

If simple stacking of adsorbent is used in traditional adsorption tower, then device structure is simple, but adsorption path is excessively short and space utilization rate is low

Engineering Contradiction:
Improveadsorption pathVSAvoidtower structure
Core Design Contradiction:
Length of moving objectVSDevice complexity

Solution Approach 1:

The adsorption tower is divided into multiple channels (first channel, second channel, third channel) with tray assemblies and partition assemblies creating distinct flow paths. This segmentation extends the adsorption path from a simple vertical stack to a multi-dimensional flow pattern through the adsorbent beds, allowing material to traverse longer paths while maintaining structural organization.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The introduction of radial partitions and tray assemblies transforms the adsorption path from a one-dimensional vertical flow to a multi-dimensional path that includes radial and axial components. Material flows through multiple levels and channels, effectively increasing the adsorption path length without proportionally increasing tower height.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

2Quantity of substance

If nonuniform adsorbent distribution is used in traditional adsorption tower, then filling process is simple, but adsorbent utilization is insufficient and wear is easy

Engineering Contradiction:
Improveadsorbent utilizationVSAvoidfilling process
Core Design Contradiction:
Quantity of substanceVSEase of operation

Solution Approach 1:

The partition assemblies create localized zones with controlled adsorbent distribution. Each channel and tray section can be independently filled and optimized for specific flow rates and contact patterns. This ensures uniform adsorbent distribution in each local zone, improving overall utilization and reducing wear hotspots while maintaining relatively simple filling procedures through modular assembly.

Inventive Principle:
Principle #3Local quality

3Productivity

If adsorption tower and desorption tower are separated, then regeneration process is simple, but adsorption is interrupted and processing capacity is low

Engineering Contradiction:
Improveprocessing capacityVSAvoidtower system
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The first channel and second channel are merged into a single integrated adsorption tower structure, allowing one channel to perform adsorption while the other simultaneously performs desorption. This merging eliminates the need for separate towers while maintaining continuous operation, as regeneration in one channel does not interrupt adsorption in the other channel.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The multi-channel design enables continuous useful action by allowing adsorption and desorption to occur simultaneously in different channels. While the first channel is adsorbing, the second channel can be regenerated, and vice versa. This eliminates downtime and maintains continuous processing capacity without requiring separate towers.

Inventive Principle:
Principle #20Continuity of useful action

4Loss of energy

If thermal regeneration process is used for adsorbent, then regeneration efficiency is high, but heat loss is large and operating conditions are harsh

Engineering Contradiction:
Improveheat lossVSAvoidregeneration effect
Core Design Contradiction:
Loss of energyVSReliability

Solution Approach 1:

A fluid intermediary (such as a desorption agent or process stream) is introduced to facilitate the desorption process. This intermediary carries the adsorbed contaminants away from the adsorbent at lower temperatures, replacing the need for high-temperature thermal regeneration. The intermediary acts as a mediator that enables effective regeneration while minimizing energy loss and avoiding harsh thermal conditions.

Inventive Principle:
Principle #24Intermediary (Mediator)

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

Enhances adsorption path contact time, improves adsorbent utilization, reduces heat loss, and enables simultaneous adsorption and desorption, increasing processing capacity and adsorbent recycling rate.

Implementation Method 1

Adsorption desulfurization is a technology in which an adsorbent is used in an adsorption tower to selectively adsorb sulfur-containing substances from a material

Methodology Applied
Scientific EffectAdsorption: Adsorption

Implementation Method 2

a certain amount of liquid medium enters the adsorption tower to flush the adsorbent

Methodology Applied
Scientific EffectLiquid flushing:

Implementation Method 3

nitrogen enters the adsorption tower to purge the adsorbent

Methodology Applied
Scientific EffectNitrogen purge:

Data Source

PatentUS20260070012A1Multi-channel adsorption tower and desorption regeneration process
Publication Date: 2026.03.12 EAST CHINA UNIV OF SCI & TECH
  • US20260070012A1 patent drawing
  • US20260070012A1 patent drawing
  • US20260070012A1 patent drawing

AI summary

The present disclosure provides a multi-channel adsorption tower including a tower body, an upper head, a lower head, tray assemblies, partition assemblies, a support plate, ceramic balls and an adsorbent. The interior of the adsorption tower is divided from bottom to top into a feed chamber, a first-stage adsorption chamber, a second-stage adsorption chamber, a third-stage adsorption chamber and a discharge chamber in sequence by the tray assemblies. Each adsorption chamber is equally divided into four material compartments by the partition assemblies. The adsorption chambers are filled with the adsorbent, and unloading ports are provided at the outside of each adsorption chamber. A feed port is provided at the bottom of the lower head, and a discharge port is provided at the top of the upper head. The feed chamber and the discharge chamber contain ceramic balls. The arrangement provides two material paths in the adsorption tower.