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ILC GDE meeting Cryogenics

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Presentation on theme: "ILC GDE meeting Cryogenics"— Presentation transcript:

1 ILC GDE meeting Cryogenics
L. Tavian, CERN T. Peterson, Fermilab Bangalore, 10 March 2006

2 Contents Sloped system comments Cryoplant capacity and margin
Cryogenic unit length Segmentation Cryogenic system arrangement Cryogenic plant architecture Plan for cost estimate GDE Bangalore, Cryogenics, 10 March 2006

3 GDE Bangalore, Cryogenics, 10 March 2006

4 Sloped system concerns
Want heat removal without bubbling or boiling Saturated superfluid heat flux limit about 1 W/sq-cm 54.9 mm dia down-pipe means 23.7 sq-cm or about 24 W per cavity can be transferred away But a claim was made that surface area limit is 1/10 of that, 0.1 W/sq-cm, so 2.4 W/cavity limit Hence, want to pool liquid in 2-phase pipe by means of dams in order to provide large surface area for evaporation Conclusion in subsequent discussions -- dams not needed Even just 2.4 W/cavity is enough, expect 1.7 W/cavity at 36 MV/m Most experience does not support the claim of the surface area heat flux limit Sloped system should not be a problem, within limits LHC will run some areas with 1.4% slope DESY will test sloped modules for XFEL GDE Bangalore, Cryogenics, 10 March 2006

5 CERN LHC capacity multipliers
Cryo capacity = Fo x (Qd + Qs x Fu) Fo is overcapacity for control and off-design or off-optimum operation and for cooling down Fu is uncertainty factor on load estimates, taken on static heat loads only Qd is predicted dynamic heat load Qs is predicted static heat load ILC Proposal: Fo= 1.4 and Fu= 1.5 GDE Bangalore, Cryogenics, 10 March 2006

6 Heat Load evolution in LHC
Basic Configuration: Pink Book 1996 Design Report: Design Report Document 2004 Temperature level Heat load increase w/r to Pink Book Main contribution to the increase 50-75 K 1,3 Separate distribution line 4-20 K Electron-cloud deposition 1,9 K 1,5 Beam gas scattering, secondaries, beam losses Current lead cooling 1,7 Separate electrical feeding of MB, MQF & MQD At the early design phase of a project, margins are needed to cover unknown data or project configuration change. GDE Bangalore, Cryogenics, 10 March 2006

7 Cryogenic unit parameters
GDE Bangalore, Cryogenics, 10 March 2006

8 Cryogenic unit length limitations
25 KW total equivalent 4.5 K capacity Heat exchanger sizes Over-the-road sizes Experience Cryomodule piping pressure drops with 2+ km distances Cold compressor capacities With 192 modules, we reach our plant size limits, cold compressor limits, and pressure drop limits 192 modules results in km long cryogenic unit -- 5 units per 250 GeV linac Divides linac nicely for undulators at 150 GeV GDE Bangalore, Cryogenics, 10 March 2006

9 Cryogenic unit segmentation and other cryogenic boxes
Segmentation issue is ultimately tied to reliability RDR should include features for vacuum segmentation Assume 4 cryo strings (48 modules, 563 meters) per segmentation unit Cryogenic string supply and end boxes (cryogenic service modules), which may (should!) be separate from modules, are also required within the ILC linac GDE Bangalore, Cryogenics, 10 March 2006

10 Full segmentation concept (ACD)
A box of slot length equal to one module Can pass through cryogens or act as “turnaround” box from either side Does not pass through 2-phase flow, so must act as a supply or end of a cryogenic string Includes vacuum breaks May contain bayonet/U-tube connections between upstream and downstream for positive isolation May contain warm section of beam pipe May also want external transfer line for 4 K “standby” operation (4 K only, no pumping line) GDE Bangalore, Cryogenics, 10 March 2006

11 Cold devices ~940 main linac modules per 250 GeV linac (so 940 x 2)
Pre-accelerators up to 5 GeV (1 electron, 1 positron) ~10 special low-energy magnet/RF modules (x2) 21 standard modules in each (x2) Damping rings (1 electron, 2 positron) Electron side MHz SRF, about 15 cavities plus 200 m of CESR-c type SC wigglers = 1200 W total at 4.5 K Positron side MHz SRF, about 10 cavities plus 200 m of CESR-c type SC wigglers x 2 rings = 2000 W total at 4.5 K RTML (1 electron, 1 positron) 61 standard modules, equiv to 5 strings (x2) (possibly also crabs) Superconducting solenoids (x2) 200 meters of SC undulators in electron linac (~300 W) SC magnets and crab cavities in interaction regions Various cryogenic service modules Several km of cryogenic transfer lines GDE Bangalore, Cryogenics, 10 March 2006

12 Cryoplant location options (electron side)
Undulators RTML Undulators GDE Bangalore, Cryogenics, 10 March 2006

13 Cryogenic architecture
For shaft depth above 30 m, the hydrostatic head in the 2 K pumping line becomes prohibitive and active cryogenics (e.g. cold compressor system) has to be installed in caverns (LBC), i.e. additional cost for cryogenics and civil engineering. GDE Bangalore, Cryogenics, 10 March 2006

14 Cost Breakdown Structure
A more precise layout including the location of the cold device is required for the cost estimate of the cryogenic system (impact on number of technical service modules and transfer line length) GDE Bangalore, Cryogenics, 10 March 2006

15 Schematic layout vs integration layout (next step is incorporating real locations in cryo system design) Real location ? GDE Bangalore, Cryogenics, 10 March 2006

16 LHC Helium Refrigerator Coldbox 18 kW @ 4.5 K
GDE Bangalore, Cryogenics, 10 March 2006

17 LHC Helium Compressor Station
GDE Bangalore, Cryogenics, 10 March 2006

18 Cryogenic He Refrigerators Capital Cost
Covering Modified Claude cycle, no permanent LN2 precooling Capacity range 0.8 to K equivalent Iso-exergetic assessment of mixed cooling duties Not included LN2 precooler for cooldown of load Coldbox interconnection lines & pipework Process control hardware & software Best practical fit Cost = 2.2 x Capacity0.6 [MCHF 1998] 4.5 K] GDE Bangalore, Cryogenics, 10 March 2006

19 Specific Cost of Bulk He Storage
Type Pressure [MPa] Density [kg/m3] Dead volume [%] Cost [CHF*/kg He] Gas Bag 0.1 0.16 300(1) MP Vessel 2 3.18 5-25 HP Vessel 20 29.4 0.5 500(2) Liquid 125 13 (3) *: CHF 1998 year (1): Purity non preserved; not including storage building (2): Not including HP compressors (3): Not including reliquefier GDE Bangalore, Cryogenics, 10 March 2006

20 2 MPa GHe Storage Vessels
GDE Bangalore, Cryogenics, 10 March 2006

21 He Compound Transfer Line
CERN experience return for compound lines: From few 10’s of m up to several 10’s of km with singularities (steps, elbows, technical service modules…) For large series, row material becomes one of the main cost drivers (e.g. variation on stainless-steel cost). Cost Standard length: between 5 to 15 kCHF/m for compound lines of ~600 mm external diameter depending on the unit length. Singularities: Each singularity equivalent to 3 to 6 m of standard length. GDE Bangalore, Cryogenics, 10 March 2006

22 Conclusions Sloped system should not be a problem, within limits
5 cryogenic units per linac 192 modules per unit, 2.3 km long Limited by plant size, cold compressor capacities and piping pressure drops Next step is incorporating real locations in cryo system design -- needed for cost Cost estimate based on LHC experience GDE Bangalore, Cryogenics, 10 March 2006


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