Argon - PowerPoint PPT Presentation

About This Presentation
Title:

Argon

Description:

Tank heat load 0.05%/day 47kW. Flash during filling, assuming. 5 psig supply 6kW ... Fermilab usage 45 to 78 tons/day. CHL liquefier 100 ton/day. 12 trucks or ... – PowerPoint PPT presentation

Number of Views:991
Avg rating:3.0/5.0
Slides: 15
Provided by: RLS4
Category:
Tags: argon | flashing | public

less

Transcript and Presenter's Notes

Title: Argon


1
Argon
  • Refrigeration
  • Supply
  • Purity

2
Argon Refrigeration
  • Heat load summary
  • LN circulation
  • LN supply

3
Heat Load Summary
  • Tank heat load 0.05/day 47kW
  • Flash during filling, assuming
  • 5 psig supply 6kW
  • Vapor displaced during filling 1.5 kW
  • Total with 1.25 factor 68 kW

4
LN Supply Perspective
  • Flare Usage 34 tons/day
  • Fermilab usage 45 to 78 tons/day
  • CHL liquefier 100 ton/day
  • 12 trucks or 5 railcars per week
  • LN cost at Fermilab 62/ton
  • 2002 budget price for 100 ton/day liquefier 2.9
    million

5
Nitrogen Circulation
  • Condensers inside tank to minimize argon handling
  • Redundant pumps, heat exchangers, etc.
  • Nothing extraordinary
  • Needs further development to improve cost
    estimate
  • Present estimate 460k

6
LN Supply Tasks
  • Five liquefier vendors contacted recently
  • Failures
  • Power failures
  • Mechanical breakdowns
  • LN leak inside detector tank
  • Supply interruptions
  • Detector Tank loses 25 tons argon/day without
    cooling
  • Zero backflow vent system needed

7
Argon Supply
  • Praxiar quotation in January 2004
  • 37 million, truck delivery, 1ppm
  • RR cars would be less expensive
  • Oxygen concentration is negotiable, 1ppm is
    proven without extraordinary effort
  • Could use multiple suppliers

8
Argon Receiving
  • Procedure proven at Dzero, NWA and E706
  • Connect to truck
  • Test carefully, accept or reject
  • Testing includes oxygen concentration, electron
    lifetime, possibly other tests
  • Pump through purifier into intermediate tank
  • Test and pump into detector tank

9
Receiving Further Development
  • Failure scenarios
  • Adding contaminated delivery to main tank
  • Spill during connection
  • Further development
  • Piping Schematic
  • Instrumentation requirements
  • Estimated time to connect and test

10
Sources of impurity
  • Argon Supply
  • Surfaces
  • Tank shell
  • Cable insulation
  • Other material
  • Leaks and permeation
  • Mechanical seals
  • Dead volumes

11
Argon Purifiers
  • Purifying equipment would probably run for the
    life of the project as well as during filling
  • ICARUS used Messer Oxisorb, proprietary
    regeneration
  • Air Liquide offers a packaged liquid purifier,
    400k. Regeneration would consume 800k of argon
    during filling. Possibly can recover most of it.
  • Praxair offers gas purifier for 600k
  • Earnhart(Trigon) offers regenerable adsorbent
  • All of these should be evaluated further

12
High Purity Specifications
  • Rough tank purging
  • High capacity intermediate system?
  • Further purging?
  • High purity system with high regeneration?
  • Specification for leak testing
  • Specification for tank surfaces, tank cleaning,
    procedures during detector construction, cable
    insulation
  • Specification for all argon handling equipment
    and piping
  • Further development needed

13
Purification Testing
  • Testing is needed to prove high purity can be
    achieved without evacuation and with reasonable
    fabrication requirements
  • Outgassing in vacuum has been studied, but how is
    the rate affected by an Argon atmosphere or
    temperature?
  • Testing can be done on a reasonable scale

14
Effort estimates
  • Purity issues, a man-year of process engineering,
    plus technician and drafting support
  • MS budget to avoid re-inventing parts that are
    commercially available, 100k
  • Refrigeration and Supply, two man-months of
    engineering to improve cost estimate
Write a Comment
User Comments (0)
About PowerShow.com