NCSX Helium Bakeout System M. Kalish 3/25/02

Slides:



Advertisements
Similar presentations
1 Optimal Control of Chiller Condenser Sub-cooling, Compressor Speed, Tower Fan and Pump Speeds, and IGV Omer Qureshi, Hassan Javed & Peter Armstrong,
Advertisements

1 Ann Van Lysebetten CO 2 cooling experience in the LHCb Vertex Locator Vertex 2007 Lake Placid 24/09/2007.
STEAM TRAPS.
The First Law of Thermodynamics
CHAPTER 5: Mass and Energy Analysis of Control Volumes
Heat Exchange Design and Optimization Project Presented: May 6 th, 2010 Professor: Mr. Toksoy Group Members: Nathan Dart Andrew Kinney Paul Thompson Joe.
ENERGY CONVERSION ES 832a Eric Savory Lecture 11 – A small-scale power plant worked example Department of Mechanical.
Hydraulics.
Rotating Equipment PUMPS.
HCS Series Screw Compressor Packages. 2 HCS Series.
EUROTRANS - Helium cooled EFIT Probabilistic assessment of different DHR designs Karlsruhe, November Sophie EHSTER, Laurent VINCON.
Presented to: International Aircraft Systems Fire Protection Working Group By: Date: April 2-3, 2008 Federal Aviation Administration Next-Generation Oil.
PROJECT AND STUDY DRAWINGS & DIAGRAMS
COMMERCIAL REFRIGERATION
MER Design of Thermal Fluid Systems Pumps and Fans Professor Anderson Spring Term
Fcal upgrade for sLHC: Cryogenics modifications – TE-CRG/ C.Fabre 1 ATLAS FCal Upgrade for sLHC: Modifications to the Calorimeter Cryogenic.
For Cardinal Newman Hall Randall Lessard ET Fall 2013 Dr. Cris Koutsougeras Advisors: Dr. Rana Mitra Mr. Byron Patterson.
Air Conditioning Circuit
NCSX NCSX CDR May 21-23, 2002 Larry Dudek Slide 1 Facility Systems (WBS 62-65) L. Dudek, G. Gettelfinger, M. Kalish.
Maggie Alvarado Diego Azevedo Raphael Santos Cavalcanti Natalie Levings Richard Robards Bruno Vieira.
Achieving Efficiency in Abrasive Blasting William P. Nelson Schmidt Engineered Abrasive Systems Sponsored by:
23 Jan 2007 LASA Cryogenics Global Group 1 ILC Cryomodule piping L. Tavian for the cryogenics global group.
The First Law of Thermodynamics
NSTX TF Bundle & Center Stack Curing Oven Mike Viola Joe Rushinski Frank Jones April 14, 2003.
© 2008 Data Power Services, LLC By: Tom Taranto 2010 Energy Expo Hosted by National Grid NYSERDA Reducing Compressed Air Energy Cost Using a Systems Approach.
Hydraulic Kit (pump and tank) Pictures from prototype.
CRYOGENICS FOR MLC Cryogenic Cooldown Scheme Eric Smith External Review of MLC October 03, October 2012Cryogenics for MLC1.
Presented to: By: Date: Federal Aviation Administration Burnthrough Test Method for Aircraft Thermal/Acoustic Insulation: Burner Replacement Investigation.
CHAPTER 5: Mass and Energy Analysis of Control Volumes
Hydrogen system R&D. R&D programme – general points Hydrogen absorber system incorporates 2 novel aspects Hydrogen storage using a hydride bed Hydrogen.
CRYOGENICS FOR MLC Cryogenic Piping in the Module Eric Smith External Review of MLC October 03, October 2012Cryogenics for MLC1.

SC Project Review of NCSX, April 8-10, 2008 NCSX Cryogenics Systems WBS-62 Steve Raftopoulos NCSX Cryogenic Systems WBS(62)
Claudio Bortolin 03/09/2012. SPD (RP analyses required) 1) Pump 17b replacement and leak test 2)Pressure test on the old inlet lines (technicians coming.
Full Scale Thermosyphon Design Parameters and Technical Description Jose Botelho Direito EN/CV/DC 19 November, th Thermosyphon Workshop.
NCSX VACUUM VESSEL HEATING/COOLING PL Goranson Preliminary Results February 17, 2006 MDL Testing of Coolant Tracing NCSX.
SC Project Review of NCSX, April 8-10, 2008 NCSX Cryogenics Systems WBS-62 Steve Raftopoulos NCSX Cryogenic Systems WBS(62) Manager.
Problems 3 Dr. Kagan ERYURUK.
NCSX VACUUM VESSEL HEATING/COOLING PL Goranson Final Design Review April 4, 2006 Coolant Hose Assemblies and Thermo- hydraulics NCSX.
Euromet-meeting in Thessaloniki - March FORCE Technology Building up a high-pressure loop in FORCE Technology Historic: The investment.
EUROPEAN ORGANIZATION FOR NUCLEAR RESEARCH Design of the thermosiphon Test Facilities Thermosiphon Cooling Review A. MORAUX PH Dpt / DT Group CERN SEPTEMBER.
PIP-II Cryogenics Arkadiy Klebaner and Jay Theilacker PIP-II Collaboration Meeting 9 November 2015.
TITLE OF THE PROJECT:- AUTOMOBILE AIR CONDITIONING AIM OF THE PROJECT:- TO STUDY ABOUT AIR CONDITIONING SYSTEM OF AN AUTOMOBILE PRESENTED BY: INAMUL.
MECH1300 Pneumatic Components Topics Pneumatic Cylinders Pneumatic Motors Other Pneumatic Actuators Pneumatic Directional Control Valves Pneumatic Flow.
Hybritec Refrigerated/Blower Purge Dryers (Combination Dryer)
Development of Cryo-Module Test Stand (CMTS) for Fermi Lab (R.L.Suthar, Head,CDM, BARC) Cryo-Module Test stand (CMTS) is a very sophisticated equipment.
Mass and Energy Analysis of Control Volumes Chapter 5a.
13 Januar 2011 Immanuel Gfall (HEPHY Vienna) Annekathrin Frankenberger (HEPHY Vienna) SVD Cooling Cooling Meeting Karlsuhe.
ARÇELİK TİCARİ KLİMA EĞİTİM DÖKÜMANI APPENDIX.
Chapter 5 Part 2 Mass and Energy Analysis of Control Volumes Study Guide in PowerPoint to accompany Thermodynamics: An Engineering Approach, 8th edition.
EMERGING TECHNOLOGIES AVAILABLE TO REDUCE COMPRESSED AIR DEMAND Double Acting Air Cylinder Double Acting Air Cylinder Air Operated Diaphragm Pumps Air.
MVD COOLING STATUS COOLING PLANT: -UPDATE of THE HYDRAULIC SYSTEM -INTEGRATION OF THE MVD COOLING CIRCUIT PATHS INSIDE THE PANDA AREA -DEFINITION OF THE.
MVD COOLING STATUS MVD COOLING PROJECT: CHOICE of COOLING FLUID,
First Law of Thermodynamics applied to Flow processes
Vishy Ravindranath LCLS-II 2 K Cold Box FDR March 9, 2017
2 K Coldbox Safety and ESH
Design of the thermosiphon Test Facilities 2nd Thermosiphon Workshop
ARAC/H/F Air-cooled water chillers, free-cooling chillers and heat pumps Range: kW.
RECIPROCATING COMPRESSORS BY DEEPA M S VARUNA TANDON
FPix Cooling Circuit. FPix Cooling Circuit FPix Shared HD - Nominal Flow ΔPtotal = 5bar Δm = 0.5g/s mnominal = 2.6g/s ΔPtotal = 10bar Δm = 0.2g/s mnominal.
Tracker cooling loop “check out” draft for discussion
Date of download: 3/4/2018 Copyright © ASME. All rights reserved.
2K Cold Box Process Design
Chapter 5 The First Law of Thermodynamics for Opened Systems
Status of Hydrogen System Development
ENERGY CONVERSION ES 832a Eric Savory
Steam traps Applications and Recommendations
12. Heat Exchangers Chemical engineering 170.
Presentation transcript:

NCSX Helium Bakeout System M. Kalish 3/25/02 Outline NCSX Helium System Requirements System Description P&ID Operational Parameters Calculations Cost and Schedule

NCSX Helium System Requirements System will provide heating to hold vessel at 150C Inlet Helium gas temperature will be at 165C and outlet gas temperature will be 150C 12 kW nominally required to make up vessel losses Per “non conservative inputs” provided by Paul Goranson No heating provided at this time for PFCs Vessel will accommodate use of ½” tubing to carry helium 30 parallel paths Each path approximately 13 meters long encompassing two complete revolutions around the vessel Design will require iterations with ORNL Job scope includes skid and supply and return piping up to vessel. Does NOT include manifolds or tubing on vessel.

System Description Instrumentation Compressed Helium Inert Gas provides heating with low consequence from leaks High Cp (high pressure makes up for low density) Blower used in lieu of compressor Recuperative Heat Exchanger makes energy balance feasible Control Temperature control via heater controller Pressure control via gas regulator More elaborate PLC and VFD control of NSTX system eliminated as cost savings Instrumentation Temperature and Pressure measurement provide safety interlocks via simple mechanical relays Costs reflect installation in NCSX Test Cell.

Operational Parameters 12 KW required to make up vessel losses 24 KW available to allow for an acceptable ramp rate 165 C to 150 C drop across NSTX 270 psig helium at 207 icfm (at blower) 313 cfm through vessel 172 ft/sec in vessel

Helium Heating P&ID NCSX 30 parallel paths 24 kW 165 C 150 C 62 kW Heater Helium Heating P&ID 127 C 155 kW HE #1 56 C Bypass Cooling 32 C Valve 60 kW HE #2 Water 270 psi Blower Assy. 19 C 250 psi RV Orifice 21 kW Pressure Kalish 3/25/02 Regulating Valve

Blower With Casing Assembly Retracted Placing the blower in a pressure vessel allows the helium system to be operated at an elevated pressure without the expense of a sophisticated helium compressor. The elevated pressure is necessary to achieve the mass flow rate required to impart enough heat to NCSX.

Blower and Motor with housing retracted (NSTX Skid)

Front View of Similar NSTX Helium Skid