1 HVAC OVERVIEW and VALUE ENGINEERING ITEMS August 13, 2008 CLIC Working Group CES Lee Hammond, Fermilab.

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Presentation transcript:

1 HVAC OVERVIEW and VALUE ENGINEERING ITEMS August 13, 2008 CLIC Working Group CES Lee Hammond, Fermilab

2 RDR - Air treatment Design Basis Tunnel Ventilation – Conditioned dehumidified air from surface mounted equipment is ducted into the service tunnel at each shaft. A volume of 15000cfm (425meter³/min) flows at approximately 88fpm (1.6km/hr) to the midpoint between shafts where it is routed into the beam tunnel and returned to the shaft area. Fresh air at a rate of 20% (air change/16hr) is mixed into the air then conditioned and it is recirculated back to the service tunnel. Air volumes for the DR and BDS are similar. Hazardous Conditions - The air direction is reversible and capable of being doubled (unconditioned) during hazardous situations. Design temperature ML - The design temperature for the ML service and beam tunnels is 80-90F (27-32C). ML electronics' heat rejection is mainly to CHW direct cooling and FCUs with small amounts of heat to the ventilation air. AHU and FCUs are used at alcoves and shaft areas. Design temperature DR - The design temperature for the DR tunnel is 104F (40C), using process water fan coil units, and the tunnel wall as a heat rejection source.

3 RDR - Air treatment Design Basis Design temperature BDS - The design temperature for the BDS is 85-90F (29-32C). The low “heat to air” load is mainly absorbed by the tunnel wall. Air mixing fans will be used for temperature stability as required by the BDS. Used the basis that airflow could pass from the service tunnel to the beam tunnel through fire/smoke/ODH/radiation protected passages between the tunnels. This assumes that radiation/oxygen deficiency hazards (ODH) do not exist or can be mitigated between the tunnels from the standpoint of air mixing. This item needs concurrence from rad/ODH groups. AHU and FCU sizes in the alcoves and tunnels did not consider heat absorption by the rock wall. These units use chilled water from the surface as the heat rejection source.

4 Air Treatment WBS Air Treatment Cost is about 1% of CFS (or 5.5% when CHW system is moved to the air treatment WBS) RDR

5 CFS Air Treatment Layout

6 AIR SYSTEM CONCEPT (assume no issues with mixing airflow between service and beam tunnel) Shaft 7 Service tunnel Beam tunnel 64 waveguide penetrations Neutral air, ~15,000 cfm = 1 mph air speed (88 fpm) 85 F

7 Possible waveguide cooling - IF “Waveguide at Penetration” is aircooled and no issues with mixing airflow between service and beam tunnel Shaft 7 Service tunnel Beam tunnel 64 waveguide penetrations Neutral air, ~15,000 cfm = 1 mph air speed (88 fpm) KW per waveguide pene 7 air delta T X 64 = additional 19,200 cfm air Waveguide load in the beam tunnel will still need be picked up by fancoils Means of air balancing at each penetration needed Some part of tunnel will have ~200 fpm air speed 85 F 92 F

8 POST RDR

9 Rock Contribution? Some discussions and preliminary investigation, but not considered There still is considerable KW load to the air per RF - chilled fancoils are needed to maintain temperatures

10 RDR Chilled Water Schematic x 26 qty CHW Plant at Shaft 7

11 Surface Air/CHW Plant locations 1.1 DUMPS

12 Air Treatment Summary  Air Treatment Components in RDR:  Large air handling systems providing heating, cooling, dehumidification, humidification.  Fans for air purge, tunnel and shaft pressurization  Miscellaneous ducting and accessories, dampers, insulation, etc  Chilled water systems including chillers, cooling towers, piping and accessories will be moved to the Air Treatment WBS  Air treatment design is dependent on the ventilation requirements and the heat load criteria received from the area systems  Air treatment and purge systems have not been fully investigated for radiation and ODH issues. Need further input on air flow configuration concerning radiation and ODH issues  Air treatment and purge systems configuration were not developed with consensus of any AHJ (authority having jurisdiction, even who this is may not be identified for some time). Need fire protection consultant.

13 Specific V.E. List About 50+ list from V.E. in Nov 2007, List from value engineering sessions in Nov Some appear to have very good cost reduction potential. No pros/cons and cost impact evaluation done yet Color coded Red=Marc selected on Dec Yellow=potential VE but not necessarily cost reduction? Green= by others (HLRF), notCFS Gray=ignore White=not sure Most VE work effort stopped on Dec POST RDR

14 HVAC/CHW Value Engineering Studies Provide one hi-efficiency cogen power/cooling plant on site and distribute power and 33°F (0.6°C) CHW throughout the facility, –Removes power/CHW production systems costs from the project cost. –Removes one piping system from project. –33°F CHW = smaller pipes, lower HP pumps, smaller HXs, very HI delta T (90°F/50°C+) –Cogen plant builder/operator finances, builds, operates, and maintains power plant then sells utility power and CHW to ILC. –Allows cooling of tunnel and electronics mitigating high temperature disadvantages. –Centralize plant reduces shaft/support area footprints. Centralize the HVAC and reconfigure airflow from tunnel ends or center. Modify top-of-shaft HVAC to only process make up air, add blowers at tunnel level for recirculation. Investigate use of desiccants to dehumidify make up air. Could use heat recovery from cogen plant. Investigate alternate piping materials, PVC, copper, HDPE, etc.