Cascade Distillation Condenser Layout for Stable Isotope Separation

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Solution Overview

Problem

Conventional cascade distillation processes for isotope enrichment face challenges in efficiently feeding and condensing gases between distillation columns, leading to unstable flow and reduced separation efficiency due to pressure differences and the use of liquid pumps, which increase liquid hold-up and heat leakage.

Innovation Solution

A distillation apparatus with separate feed-gas condensers and top-gas condensers connected through dedicated lines ensures stable gas flow and condensation, allowing all generated liquid to be refluxed directly to the next column, reducing pressure fluctuations and enhancing separation efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Speed

If pressure differences are used to return gases between distillation columns, then gas flow is achieved, but the separation factor becomes smaller and distillation efficiency decreases

Engineering Contradiction:
Improvegas flow rateVSAvoidseparation factor
Core Design Contradiction:
SpeedVSManufacturing precision

Solution Approach 1:

The gas return path is segmented into two independent systems: (1) feed gas from former column to feed-gas condenser, and (2) top gas from distillation column to top-gas condenser. This segmentation eliminates the mixing problem and allows independent optimization of each gas stream's pressure and flow characteristics, resolving the contradiction between achieving gas flow and maintaining separation factor.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Feed-gas condensers and top-gas condensers serve as intermediary devices that receive gases from distillation columns, condense them separately, and return the condensed liquids. These intermediaries eliminate direct gas-phase pressure differential dependencies, allowing each condenser to operate independently and maintain optimal separation factors while ensuring proper gas flow through condensation and liquid return mechanisms.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If liquid pumps are used to flow liquid between distillation columns, then material transfer is achieved, but liquid hold-up increases and startup time is extended

Engineering Contradiction:
Improvematerial transfer rateVSAvoidstartup time
Core Design Contradiction:
ProductivityVSLoss of time

Solution Approach 1:

Liquid pumps are completely extracted (removed) from the system. Instead of using mechanical pumps to transfer liquid, the invention relies on natural liquid flow driven by pressure differences and gravity. The feed-gas condenser liquid and top-gas condenser liquid are returned to distillation columns through liquid return lines without mechanical pumping, eliminating liquid hold-up in pumps and reducing startup time while maintaining continuous material transfer.

Inventive Principle:
Principle #2Taking out (Extraction)

3Productivity

If liquid pumps are used in cryogenic distillation, then liquid transfer is achieved, but heat inleak increases

Engineering Contradiction:
Improveliquid transfer capabilityVSAvoidheat inleak
Core Design Contradiction:
ProductivityVSLoss of energy

Solution Approach 1:

Liquid pumps are extracted from the cryogenic liquid transfer system. The invention uses passive liquid return mechanisms where condensed liquids flow back to distillation columns through liquid return lines driven by pressure and gravity differences. This eliminates mechanical pumping of cryogenic liquids, removing the associated heat inleak from pump mechanisms while maintaining effective liquid transfer capability.

Inventive Principle:
Principle #2Taking out (Extraction)

4Device complexity

If feed gas is mixed with top gas before condensation, then condensation occurs, but feed gas flow becomes unstable due to top gas flow dynamics

Engineering Contradiction:
Improvecondensation processVSAvoidfeed gas flow stability
Core Design Contradiction:
Device complexityVSStability of the object's composition

Solution Approach 1:

The condensation process is segmented into two independent pathways: feed gas condensation in feed-gas condensers and top gas condensation in top-gas condensers. This segmentation prevents mixing of feed gas and top gas streams, allowing feed gas flow to remain stable and unaffected by top gas flow dynamics. Each condenser handles its specific gas stream independently, maintaining flow stability while achieving condensation.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Feed-gas condensers act as intermediary devices that receive feed gas separately from top-gas condensers. This intermediary arrangement prevents direct mixing between feed gas and top gas streams, isolating the feed gas flow from the dynamic effects of top gas flow. The intermediary condensation process ensures stable feed gas flow while maintaining the necessary condensation function.

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

This configuration ensures stable feeding of the feed gas into the distillation columns, increasing the separation factor and improving the efficiency of isotope enrichment by minimizing liquid hold-up and heat leakage, while reducing the need for pressurizing devices.

Implementation Method 1

feed-gas condensers which condense feed gases from respective former distillation columns and feed the condensed feed gases to respective latter distillation columns

Methodology Applied
Scientific EffectCondensation: Condensation

Implementation Method 2

top-gas condensers provided on the tops of the respective distillation columns

Methodology Applied
Scientific EffectCondensation: Condensation

Data Source

PatentUS9194623B2Distillation device
Publication Date: 2015.11.24 NIPPON SANSO CORP
  • US9194623B2 patent drawing
  • US9194623B2 patent drawing
  • US9194623B2 patent drawing

AI summary

A distillation apparatus includes: a distillation column group in which a plurality of distillation columns, which are respectively equipped with a reboiler, is connected in the form of a distillation cascade; feed-gas condensers which liquefy feed gases from respective former distillation columns and feed said liquefied feed gases to respective latter distillation columns; gas-feeding lines which connect the respective former distillation columns and the respective feed-gas condensers; and liquid-feeding lines which connect the respective feed-gas condensers and the respective latter distillation columns.