The Milton S. Hershey Medical Center Academic Support Building - - PowerPoint PPT Presentation

the milton s hershey medical center academic support
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The Milton S. Hershey Medical Center Academic Support Building - - PowerPoint PPT Presentation

The Milton S. Hershey Medical Center Academic Support Building ASHRAE Student Presentation Night April 9, 2003 Kari Anne Donovan Penn State University AE - Mechanical Option Presentation Outline Existing Building Overview


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The Milton S. Hershey Medical Center Academic Support Building

ASHRAE Student Presentation Night April 9, 2003

Kari Anne Donovan Penn State University AE - Mechanical Option

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Presentation Outline

  • Existing Building Overview
  • Distributed Chilled Water Feasibility Study
  • Proposed Mechanical Redesign

– Integrated Fire Suppression and Hydronic Thermal Transport Systems – Electrical Service – Building Changes – Lighting Energy Savings

  • Summary
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SLIDE 3

Existing Building Systems

  • Project Description

– 5 story, 145,316 gross sq. ft – 19 million dollar project

  • Building Function

– Mixed office use – Houses departments of Penn State College of Medicine and Hershey Medical Center

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SLIDE 4

Building Layout

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Existing Mechanical System

Points of Interest

  • VAV underfloor air

distribution system

– Flexibility to accommodate

  • ffice churn
  • 7,513 sq. ft. return air

plenum mechanical penthouse

  • ASHRAE Standard 62

ventilation requirements not met

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SLIDE 6

Distributed Chilled Water

Feasibility Study

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SLIDE 7

Central Utility Plant

Conditions, 1998

12,5000 ton-hr capacity 1.4 mil gal CHWTR Storage Tank TES 1000 hp electric drive HCFC-22 1000 ton screw 9 1000 hp electric drive HCFC-22 1000 ton screw 8 1000 hp electric drive CFC-11 1000 ton centrifugal 7 Low Pressure Steam LiBr 800 ton absorber 6 1000 hp electric drive CFC-11 1000 ton centrifugal 5 1000 hp electric drive CFC-11 1200 ton centrifugal 4 Low Pressure Steam LiBr 800 ton absorber 3 Low Pressure Steam LiBr 800 ton absorber 2 Steam turbine drive CFC-11 1200 ton centrifugal 1

Summer 1997 – 9,5000 tons and 16,000 gpm Plant at full capacity

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SLIDE 8

Energy Analysis Comparison

$26,070.07 $53,180.51 $79,250.58 Annual Energy Cost 522,466 kWh 1,065,742 kWh 1,588,188 kWh Annual Energy Usage 0.425 kW/ton 0.869 kW/ton 1.294 kW/ton Efficiency CUP Savings CUP Electric Mode Operation Existing Standalone System Chilled Water Production

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Simple Payback Analysis

~ $260/ton for chiller and cooling tower installation ~ 2.7 year payback for the needed 450 tons with diversity factor of 60% ~ $52/ft of pipe installation ~ 9 year payback for the 4,500 ft run of distribution piping taken off the Mega-Structure supply.

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Distributed Chilled Water

Feasibility Conclusion

CUP Benefits

  • Reduced kW/ton of the CUP
  • Increased efficiency and

energy savings

  • Reduced campus electric

demand charge CUP Drawbacks

  • No existing utility piping
  • Remote building location
  • CUP at full capacity
  • Chiller #6 freeze-up and

replacement Recommendation: UTILITY SERVICE FROM CENTRAL UTILITY PLANT NOT ATTRACTIVELY FEASIBLE AT TIME OF DESIGN.

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SLIDE 11

Dedicated Outdoor Air System with Parallel Sensible System

Reduced overall building height ASHRAE Standard 62 compliance Reduced building first cost and operating cost Improved IAQ and thermal comfort Reduced plenum height Reduced mechanical equipment size Reduced electrical service for penthouse

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Dedicated Outdoor Air System

(DOAS)

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Radiant Panel System

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Installation Comparison

  • DOAS/Radiant installation cost $367,122

less than existing system

–IAQ and personal thermal comfort vs. Productivity –Control Valves

  • Control Packages not included
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SLIDE 18

Energy Savings

Proposed Redesign Existing 3,342,631 kBTU 8,210,545 kBTU Total 168,664 kWh 849,205 kWh Fans 67,523 kWh 30,267 kWh Pumps 726,758 kWh 503,723 kWh Chiller

Annual Savings of 4,867,914 kBTU - $43,352 Recommendation: ENERGY SAVINGS & BENEFIT OF IMPROVED IAQ CAN POTENTIALLY OFFSET AN INCREASE IN CONTROLS COST.

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Fire Suppression and Hydronic Thermal Transport System Integration

NFPA 13 allows dual use of sprinkler piping for other purposes

–Life safety requirements always come first –Water for sprinkler service must not pass through auxiliary equipment –Shut-off valves for auxiliary service –Closed-loop circulating system, less than 120F water temperature –No water additives to inhibit suppression

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Fire Suppression and Hydronic Thermal Transport System Integration

  • Redundant Piping Savings

– $75,540

Typical Radiant Cooling Panel Piping Detail

  • High interaction of disciplines during design and

construction

  • Added 1st Cost for

controls

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SLIDE 23

Electrical Service

System Comparison

17.9 kW 32.5 kW Pump 401.9 kW 854.7 kW Total 0.1 kW 0 kW ER 343.8 kW 607.8 kW Chiller 40.0 kW 214.5 kW Fan Redesign Existing Equipment Transformer resized from 1500 kVA to 1000 kVA First Cost Savings $4,400

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Overall Building Changes

  • Access Flooring Height Reduction
  • 1’-3” to 6”

Total Building Height Reduction: 5’-0”

  • Return Air Plenum Height Reduction
  • 1’-9” to 1’-6”
  • Total Floor to Floor Height Reduction
  • 1’-0”
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SLIDE 25

Overall Building Changes

  • Pre-Cast Concrete Panel Savings

– $175,610

Total Building Height Reduction Savings: $176,820

  • Structural Steel Column Height Savings

–$1,210

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SLIDE 26

Penthouse Changes

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SLIDE 27

Penthouse Changes

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SLIDE 28

Penthouse Changes

  • First Cost Savings on roofing and Steel

Panels

– $6,525

  • Reduction in chiller vibration and high

frequency compressor noise perceived on 5th floor

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Lighting Energy Savings

  • De-clutters ceiling to allow for radiant panels
  • Change T8 to T5 lamps

–Reduce number of units by 57% –Reduce installation cost by $44,141 (30%) –Annual Energy Savings of $567

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Proposed Integrated Redesign Potential Savings:

$594,608 Installation Cost Savings* $43,920 Annual Energy Savings

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Questions?