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Terminal Unit Overview
T.U. Overview Terminal Unit Overview Evan Himelstein, P.Eng. Application Engineering Price Industries October 11, 2004
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Agenda Terminal Unit types and characteristics Pressure Definitions
T.U. Overview Agenda Terminal Unit types and characteristics Single Duct Terminals LGF – Flow Measurement LGE - Exhaust Terminal LGS - Supply Terminal Construction & tube construction Flow Sensors (SP200 & Orifice Ring) Venturi Air Valve Pressure Definitions Terminal Unit Sound / Acoustics Hot Water Coils General Pitfalls Questions On the agenda today, we will be covering the terminal unit types and characteristics. This will be split up between single duct blade terminals and venturi air valves. We will then move along to pressure definitions, terminal unit sound and acoustics. Finally we will cover off hot water coils and general pitfalls people end up having. Finally we will have time for questions.
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Terminal Unit Types Single duct terminal units
T.U. Overview Terminal Unit Types Single duct terminal units Controller type – Siemens LGS Mechanical type Control / Exhaust Valves Siemens LGE Venturi Air Valves Dual Duct Terminals Fan Powered Terminals Constant Volume / Series Flow Variable Volume / Parallel Flow Induction Terminal Units Retrofit Terminal Units Flow Measurement Devices Siemens LGF Discussed Today Discussed Today Discussed Today There are many types of terminals. Not all of which are relevant for this discussion. For information on other terminal types you can go to the Price website. The terminals that will be discussed today are the Siemens LGS, LGE and venturi valves. For more information on terminal unit types not covered see the Price website, Discussed Today
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Flow Measuring Devices Siemens LGF
Laboratory Air Flow Station Not really a terminal unit, but... Galvanized Steel with optional 316L Stainless Steel Continuously Welded Construction Orifice Ring Sensor Available in sizes 4, 6, 8, 10, 12, 14, 16, 18, 20, 22 SP200 Sensor Available in sizes 6, 8, 10, 12, 14, 16 New shorter version (8”)
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Single Duct - Exhaust Terminals Siemens LGE
T.U. Overview Single Duct - Exhaust Terminals Siemens LGE Basic unit includes Damper Flow Sensor SP200 Orifice Duct Type Galvanized Stainless Steel Teflon Coated Model LGH discontinued
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Single Duct Terminals Siemens LGS
T.U. Overview Single Duct Terminals Siemens LGS Basic unit includes Damper Flow Sensor (SP200) Heating Coil (optional) Attenuator (optional) Operation Varies air volume to space Monitors air flow sensor Pressure independent Single duct terminals – most common and economical. Reliable & simple operation. Includes damper, flow sensor, heating coils, and attenuator. Operation generally varies supply air volume to space based on temperature or pressure. Unit is pressure independent as the controls monitors the airflow sensor.
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Pressure Dependent vs Independent
T.U. Overview Pressure Dependent vs Independent Pressure Dependent Flow rate varies with system inlet pressure fluctuations. Flow rate dependent on inlet pressure and damper position Pressure Independent Flow rate is constant regardless of inlet pressure fluctuations Achieved by adding a flow sensor and flow controller Controller maintains a preset flow through the inlet by modulating the damper in response to the flow signal. What is the difference between a pressure dependent and pressure independent boxes.
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Single Duct Terminals Options Price can support Specials!
T.U. Overview Single Duct Terminals Options Hot Water Coils 1, 2, 3 or 4 rows Standard access door for inspection & cleaning Sound Attenuators 3 or 5 foot Price can support Specials!
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Single Duct Terminals Liner
T.U. Overview Single Duct Terminals Liner This system integrates an engineered polymer foam which provides excellent insulating characteristics. The foam edges are self sealing due to the material’s composition. Material has a water vapor permeability of 0.0%, and will not initiate mold growth.
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Siemen’s Specific Features
T.U. Overview Siemen’s Specific Features Standard FF (Fiber Free) Liner Access door in LGS casing not in water coil Sensor tubes in brass fittings not rubber grommets Standard Extra low leakage construction Individually packaged – 2x Weight Cardboard Cartons Special Siemens Labeling
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LGS Casing Leakage Unit in CFM in % of Max Flow Size 1.00” 3.00” 6.00”
T.U. Overview LGS Casing Leakage Unit in CFM in % of Max Flow Size 1.00” 3.00” 6.00” 4 1 2 3 0.40% 0.90% 1.30% 6 0.30% 0.60% 8 0.20% 0.70% 10 0.50% 12 0.10% 14 5 16 7 18
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LGS Damper Leakage Unit Size in CFM % of Maximum Flow 1.50” 3.00”
T.U. Overview LGS Damper Leakage Unit Size in CFM % of Maximum Flow 1.50” 3.00” 6.00” 4 5 6 1.78% 2.22% 2.67% 11 0.89% 1.33% 2.44% 8 7 10 0.63% 0.88% 1.25% 0.44% 0.52% 0.74% 12 19 0.38% 0.57% 0.90% 14 16 0.20% 0.33% 0.53% 13 21 38 0.95% 18 98 154 305 1.23% 1.93% 3.81%
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Single Duct Damper Construction
T.U. Overview Single Duct Damper Construction Toggle-Lock Sandwich Construction 2 pieces of 22 gauge galvanized sheet-metal riveted together No welding required Zinc anti-rust protection is not ruined No heat distortion of blade (leakage) ** Request from Jerry 2 or 3 damper blades **
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Single Duct Damper Seal
Polyurethane Gasket Flexible material provides excellent seal Does not dry out and crack with age 1.5 million cycle operational test resulted in no measurable change in leakage rate Equates to 100 full damper cycles per day, ( complete open and closures) for 42 years Gasket
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Single Duct Damper Shaft
T.U. Overview Single Duct Damper Shaft Solid Steel Shaft Anti-rust Nickel Plating Damper position indicator on end of shaft Self-lubricating, tight-fit, low-leak bearings Much stronger than plastic or aluminum shafts Retaining-Clips for accurate centering
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Single Duct Damper Shaft Bearings
T.U. Overview Single Duct Damper Shaft Bearings Set of three bearings Made from high density Polyethylene Will operate to inlet static pressures up to 6 inches W.G. with minimal leakage Only manufacture to use 3 bearings Tested to 1.25 million cycles Equates to 100 full damper cycles per day, ( complete open and closures) for 35 years
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Single Duct Inlet Tube Construction
T.U. Overview Single Duct Inlet Tube Construction Rolled Bead Stronger More Round Stop for hard duct Seam Riveted connection Sealed with caulk Long Eliminates need for straight duct before the inlet Cross flow sensors will be demoed and are not covered in this presentation.
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Valve Sizing Size Valve based on maximum and minimum airflow
T.U. Overview Valve Sizing Size Valve based on maximum and minimum airflow With Maximum Flow review Sound Pressure Drop Flexibility Cost With Minimum Flow Control Accuracy Type of Controls Select above 400 FPM duct velocity
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SP200 Air Volume Sensor The “Heart” of VAV Control
T.U. Overview SP200 Air Volume Sensor The “Heart” of VAV Control Velocity Sensor performance is a function of: Cross Sectional Area Number and Pattern of Sensing Ports Amplification Factor Center averaging capabilities
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Air Volume Sensing T.U. Overview Pt = Total Pressure – Combination of Static and Velocity Ps = Static Pressure – The Pressure in the duct pressing in all directions Pv = Velocity Pressure – The pressure in the duct due to the velocity of the air (NOT DIRECTLY MEASURABLE) Pt = Ps + Pv OR Pt - Ps = Pv
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Sensible Sampling Port Locations Total-Pressure Ports Static-Pressure
T.U. Overview Sensible Sampling Port Locations Total-Pressure Ports Static-Pressure Ports Price’s SP-200 has strategically-located Total Pressure ports, based on extensive lab-tested fine-tuning. Better than the “duct- traverse” method.
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Unbiased Representation
T.U. Overview Unbiased Representation Center-Averaging Collection Chamber Pressure-averaging at the center of the SP-200 gives assurance that all four of the quadrants’ velocities have equal representation.
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Amplification and Error
T.U. Overview Amplification and Error Reliable Accuracy at Low Airflows Most controls require at least 0.02”-0.03”w.g. sensor-output signal for reliable operation The SP-200 flow sensor provides 0.025”w.g. at 400 FPM, Sensors w/ low gain & poorly-averaged (worst case) have a safe low-end of 700 to 800 FPM
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Flow Sensing Problems Inlet Condition Problems No Velocity (turbulent)
T.U. Overview Flow Sensing Problems No Velocity (turbulent) Inlet Condition Problems 90 deg. Elbow High Velocity
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Orifice Plate Air Volume Sensing
T.U. Overview Orifice Plate Air Volume Sensing Orifice Ring Sensing 4 Sensing points Non Clogging design Very Robust Measures static pressure differential Airflow = k * (ΔP)½ Watch for inlet conditions
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Venturi Air Valves Mechanically pressure independent
T.U. Overview Venturi Air Valves Mechanically pressure independent Requires a minimum static pressure ( 0.3” L.P., 0.6” M.P.) Consists of Cone Springs Aerodynamic shape Orifice Ring (Flow sensing) Price only supplies accessories for Venturi Air Valves
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Venturi Air Valve Flow ~ Area*Sqrt(dP)
T.U. Overview Venturi Air Valve Flow ~ Area*Sqrt(dP) Spring inside cone expands or compresses to compensate for changes in pressure across valve. At low pressure drop, spring pushes cone out, increasing flow area. At high pressure drop, cone compresses spring, decreasing flow area. Change diagrams to use Siemens pictures (symmetrical venturi shape)
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Venturi Air Valve Pressure & Flow Variation
T.U. Overview Venturi Air Valve Pressure & Flow Variation
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Venturi Air Valves Accessories Sound Attenuators Hot Water Coils
T.U. Overview Venturi Air Valves Accessories Sound Attenuators 3 or 5 foot Hot Water Coils 1 Row 2 Row 3 & 4 Row optional Materials Standard: aluminum body & cone, teflon-coated stainless steel cone rod, brackets, linkage and control arm Heresite-coated body and cone available for corrosive exhaust applications
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Pressure What do all these catalog terms mean?
T.U. Overview Pressure What do all these catalog terms mean? Minimum operating pressure Inlet Static pressure Downstream Static Pressure Differential Static Pressure (ΔPs)
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Minimum Operating Pressure
T.U. Overview Minimum Operating Pressure Static Pressure Drop or Loss Wide Open Damper Position Minimum Operating Pressure Pressure Loss of Terminal and Accessories
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T.U. Overview Inlet Static Pressure Pressure From Inlet to Atmosphere
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Downstream Static Pressure
T.U. Overview Downstream Static Pressure Pressure from Downstream of Terminal Unit to Atmosphere
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Differential Static Pressure
T.U. Overview Differential Static Pressure Pressure Drop Across Terminal Only Not Inlet Static Pressure ΔPS = Inlet SP-Downstream SP
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Sound Standards ARI 880-98 Air Terminal Test Standard
T.U. Overview Sound Standards ARI Air Terminal Test Standard ASHRAE Air Terminal Test Method ARI Application Standard ADC 1062 – Obsolete and replaced with ARI Standards
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Testing Standards ASHRAE Standard 130-1996 ARI Standard 880-98
T.U. Overview Testing Standards ASHRAE Standard Specifies the methods and procedures for performance testing of constant and variable volume air terminal units. ARI Standard Determines the requirements for testing and rating air terminals References ASHRAE Standard Establishes the procedures, rating points and tolerances for conformance to the ARI 880 Certification Program.
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T.U. Overview Catalog Sound Data Due to the vast scale of sound pressures over the normal range of human hearing, the Log of the actual value is used. (Makes scale smaller) Reference power is Watts The reference pressure is MicroBars. dB are measured with respect to frequency The frequencies are grouped into ‘octave bands’
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T.U. Overview Octave Band Octave band 2 through 7 usually associated with terminal units Refers to centerline frequencies of 125 to 4000 Hz Octave Band Mid Frequency Hz 2 125 3 250 4 500 5 1000 6 2000 7 4000
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T.U. Overview Noise Sources
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T.U. Overview Catalogue Sound Data Certified in accordance with ARI 880 Certification Program
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T.U. Overview ARI Certification Price units are ARI Certified, Siemens working on there Application for Certification. Test data submitted to ARI Data listed in ARI Directory (and website) Yearly Random Tests Tested at an Independent Lab Test Failures are Published and Penalized Price has had a 100% Test Success Rates since 1994
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T.U. Overview Noise Criteria (NC) The NC value is the most commonly specified sound criteria for diffusers and terminal equipment. Standard curves used to describe a spectrum of measure sound pressure levels with a single number. Sound pressure is not cataloged. Must be calculated from Sound Power (in catalog) and taking deductions (from ARI Standard 885)
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T.U. Overview NC Curves
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Sound Warning Compare NC values between manufacturers carefully!
T.U. Overview Sound Warning Compare NC values between manufacturers carefully! Attenuation allowances between manufacturers are not always the same. Engineers do not specify this correctly Need to educate engineer on ARI Standard 885 Prudent for labs to examine attenuation allowances since they are usually harder, i.e. noisier than the typical office space.
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Application Standards
T.U. Overview Application Standards ARI Standard “Procedure for Estimating Occupied Space Sound Levels in the Application of Air Terminals and Air Outlets.” Provides methods to use ARI Standard 880 sound ratings to estimate the sound levels which will occur in the conditioned, occupied space. Appendix E created with “Typical Attenuation Values” for offices
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Hot Water Coil General Construction
T.U. Overview Hot Water Coil General Construction ½” Copper Tubes Aluminum Fins for Heat Transfer Access door for cleaning and inspection Right or left handed connections
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Water Coil Construction Features
T.U. Overview Water Coil Construction Features Construction features that have the most effect on performance … Fin Height / Fin Length (Coil Area) Number of Rows Fin Spacing (FPI) 10 FPI is standard, 8 and 12 are optional
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Water Coil Application Variables
T.U. Overview Water Coil Application Variables Variable that have the most effect on performance … Target Variable – Coil Capacity - BTU’s / Hr (MBH) Airflow – CFM (cubic feet per minute) Water Flow – GPM (gallons per minute) Entering Air Temperature – EAT (°F) Entering H2O Temperature – EWT (°F)
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Water Coils Other Important Factors
T.U. Overview Water Coils Other Important Factors Water Pressure Drop (ft.wg.) Can affect pump / pipe / valve sizing Depends largely on Number of Circuits Air Pressure Drop (in.wg.) Effects central fan sizing Effects units fan capacity Leaving Water Temperature Can cause problems in Hydronic System
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Water Coils Factors Water Velocity
T.U. Overview Water Coils Factors Water Velocity Laminar flow in coils produces very large MBH variations from small changes in Flow (GPM). Fully turbulent flow variations produce small MBH changes, high head loss, and tube pitting. Transitional flow is desirable, which is between the laminar and turbulent regions. Transitional flow range occurs between 0.5 and 8 FPS depending on many factors.
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Water Coil Calculation Givens
T.U. Overview Water Coil Calculation Givens CFM or Airflow rates More air = more heat But not PROPORTIONAL Entering Water & Air Temperatures EWT has significant impact on capacity EAT can be a mix of return, supply and fan air Standard coil configuration FPI, # of circuits and rows, find type, metal thickness.
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Water Coil How variables inter-relate
T.U. Overview Water Coil How variables inter-relate As the GPM Increases Heat transfer & leaving air temp increases Leaving water temperature increases Water pressure drop increases (fast!) As the number of rows increase Air pressure drop and leaving air temp increases Water Pressure drop might increase Leaving water temperature decreases
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Water Coils Prioritization of Parameters
T.U. Overview Water Coils Prioritization of Parameters Coil must meet or exceed true MBH load If a little low on capacity, call engineer or check Double check MBH using Air delta T calcs ATR (°F) = 927 x MBH / CFM Do not exceed the sum of specified GPMS’s OK for a given coil to vary Total cannot be higher, or pump & pipe change Keep the head below the max scheduled Could increase the equipment requirements
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Water Coils Hardware Related Choices
T.U. Overview Water Coils Hardware Related Choices Number of Coil Rows Extra expense and air pressure drop Sometimes specified by the Engineer Check Spec. Overall Terminal or Coil Size Larger boxes have more coil area = more potential capacity Can create control problems
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Terminal Selection Pitfalls
T.U. Overview Terminal Selection Pitfalls Smaller terminals for lower discharge noise Don’t oversize Size 12 and over locate over non critical area
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Terminal Unit Suggestions
T.U. Overview Terminal Unit Suggestions Do not over pressurize ductwork Increases Sound & Noise Use lined duct (in non-critical areas) Reduces high frequency noise Do not have any diffuser closer than 4’ from the outlet of the terminal unit Limit velocity in ductwork to 1000 fpm Best sound performance.
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TU Noise - Troubleshooting
T.U. Overview TU Noise - Troubleshooting Noise from a terminal can be due to a variety of conditions, and sometimes can be difficult to eliminate. First steps is to isolate the type, source and direction of the noise If noise is heard at the air outlet – discharge noise If noise is heard through the ceiling – radiated noise
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Discharge Noise Usually caused by Can be reduced by High Static
T.U. Overview Discharge Noise Usually caused by High Static Little or no internal duct lining downstream of the terminal. Sometimes air outlet dynamics (damper?) Can be reduced by Reducing flow Increasing air outlet size Reducing inlet static pressure Adding attenuation materials
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T.U. Overview Questions & Comments??
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