Anhydrous Ammonia Vapor Separator Filter Segmentation

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Solution Overview

Problem

Existing anhydrous ammonia fertilizer systems face challenges in achieving uniform ammonia application due to difficulties in controlling mixed liquid and vapor streams, leading to incorrect flow sensor data and vapor locking, and are prone to filter plugging and liquid entrainment, which affects operational efficiency and reliability.

Innovation Solution

The system incorporates a larger filter basket in a two-tower configuration, where the first tower filters solid impurities and pre-separates the ammonia stream, and the second tower ensures minimal vapor and liquid intermixing, reducing turbulence and extending filter cleaning intervals, allowing for more efficient vapor exhaust and improved flow control.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If a commercial basket filter is used in the vapor separator, then the separator can filter solid impurities, but the filter plugs occasionally requiring frequent cleaning interruptions

Engineering Contradiction:
Improvefilter operation continuityVSAvoidfilter cleaning frequency
Core Design Contradiction:
ReliabilityVSLoss of time

Solution Approach 1:

The filter system is segmented into multiple sections with different filtration characteristics. The filter basket is divided into an outer screen section and an inner screen section, allowing different particle sizes to be captured in different zones. This segmentation prevents rapid clogging by distributing the filtration load across multiple zones with varying pore sizes.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The filter basket is extended in the vertical dimension with a length of 18 inches compared to conventional shorter filters. This increased vertical dimension provides greater filtration surface area and volume, allowing the filter to hold more accumulated trash before requiring cleaning, thus extending operational intervals.

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

2Duration of action of moving object

If the filter basket length is increased to 18 inches, then the filter can operate longer between cleanings, but the device complexity increases

Engineering Contradiction:
Improvefilter operation intervalVSAvoidfilter basket structure
Core Design Contradiction:
Duration of action of moving objectVSDevice complexity

Solution Approach 1:

The extended filter basket is segmented into functional zones with different screen configurations. The outer and inner screens are positioned at different heights and have different pore sizes, creating a zoned filtration system that maximizes capacity while maintaining manageable structural complexity through modular design.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The extended filter basket structure serves multiple functions simultaneously: it filters solid impurities, provides vapor-liquid separation surface area, and acts as a trash collection volume. This multi-functionality justifies the increased length by consolidating multiple requirements into a single component.

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

3Stress or pressure

If liquid ammonia flows through valves and fittings, then pressure loss occurs causing vaporization, but this creates mixed liquid-vapor stream that complicates flow control

Engineering Contradiction:
Improvepressure drop through systemVSAvoidliquid-vapor phase composition
Core Design Contradiction:
Stress or pressureVSStability of the object's composition

Solution Approach 1:

The flow stream is segmented into separate liquid and vapor pathways through the vapor separator. The separator uses a baffle system that directs liquid ammonia through the bottom of the separator while vapor is directed through the top, preventing mixing and allowing each phase to be controlled independently through subsequent valves and fittings.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The vapor separator acts as an intermediary device between the pressure-loss-prone valve system and the application system. It receives the mixed liquid-vapor stream from the valves, separates the phases, and delivers controlled liquid to the application system, mediating the conflict between pressure drop and phase stability.

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 solution enhances the separation of liquid and vapor ammonia, reducing filter plugging and entrainment, enabling more reliable and efficient ammonia application with longer filter operation intervals and improved flow control, thus ensuring uniform fertilizer distribution.

Implementation Method 1

The filter in the tower has greater length, approximately 18 inches than the previously used commercial basket filter... filtration of rust and other trash

Methodology Applied
Scientific EffectFiltration: Filter (physical)

Implementation Method 2

The first tower also pre separates the incoming ammonia stream into separate liquid and gaseous streams... separates the ammonia vapor from liquid ammonia in a tower

Methodology Applied
Scientific EffectPhase separation: Phase Change

Implementation Method 3

Because of the lowered pressure some liquid ammonia vaporizes to cool the liquid to the saturation temperature associated with that lower pressure

Methodology Applied
Scientific EffectEvaporative cooling: Evaporative Cooler

Data Source

PatentUSRE48414E1Anhydrous ammonia fertilizer liquid and vapor separator
Publication Date: 2021.02.02 360 YIELD CENT LLC
  • USRE48414E1 patent drawing
  • USRE48414E1 patent drawing
  • USRE48414E1 patent drawing

AI summary

The vapor exhaust assembly, for anhydrous ammonia, includes a closed filter tower and a closed exhaust tower with vertical tubes. The filter tower is connected to the vapor tower by a vapor upper pipe and a liquid lower pipe. A filter tube is mounted in the filter tower. Ammonia enters the filter tower above an open end of the filter. Ammonia vapor moves from the filter tower through the vapor upper pipe to a vapor chamber in the vapor tower. Liquid moves from the filter tower through the liquid pipe to the vapor tower. Liquid received in the vapor tower is moved upward by a dam. Vapor in the liquid moves upward to the vapor chamber. Liquid moves downward from the dam top to a liquid discharge exit. A vapor discharge valve in the top of the vapor tower is opened to discharge vapor and increase liquid in both towers.