Trane UH-PRC001-EN Formula, Determining Special Steam Capacities, Useful Data, Surplus Capacity

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Formula

Selection Procedure

Formula

The following formula is used to arrive at final air temperature volume when 70 F (Standard Air Basis) is known or vice versa:

Cfm at final temp. =

Cfm at 70 F x 460 + Final temp. 460 + 70

Cfm at 70 F =

 

460 + 70

Cfm final air x

460 + Final temp.

Determining Special Steam Capacities

Where capacity of the unit under standard conditions is known – 2 lbs. steam, 60 F entering air – and it is desired to know the capacity of this same unit under different steam and air conditions, follow instructions given in Example 1 below.

Where a set of conditions is given – Btu, temperature rise, final temperature, cfm, steam pressure available, etc. Refer to Example 2.

Useful Data

Btu240 = Sq. ft. of radiation (EDR)

Sq. ft. of radiation =Lbs. of condensate

4

per hour

Btu

= Lbs. of water per hour

Latent heat

Cfm xTemp. rise x 1.085 = Btu.

Specific heat of air (70 F) = .241

Specific weight of one cubic foot of air (70 F) =.075.

Cfm x 60 = cfh.

Therefore, .241 x .075 x 60 = 1.085

Example 1

Given: Model 60S Horizontal Propeller Unit Heater with a rated capacity of 60,500 Btu at 2 lbs. steam with 60 F entering air.

Desired: Capacity of this unit using 15 lbs. steam and 40 F entering air.

Under 40 F and across from 15 lbs. in SP-2, page 14, we find the factor 1.34. 60,500 x 1.34 = 81,070 Btu per hour.

Equivalent Direct Radiation

If working in EDR, rather than Btu, multiply the EDR by the same factor in the same way.Thus:

252 (FromTable 3) x 1.34 =

338 sq. ft. or 81,070

240

Determining Amount of Condensate

To determine the amount of condensate, divide the capacity in BTU by the latent heat of steam:

81,070 = 86 lbs per hour.

945

945 = Latent Heat of Steam at 15 psi.

(SeeTable SP-9, page 18.)

Determining FinalTemperature

Final temperature of air leavingTrane Unit Heaters may be determined as follows:

Inlet AirTemp. +

Btu rating

= FinalTemp

Cfm at 70F x 1.085

Inlet AirTemp. 40F +

81,070

= FinalTemp

815(from table 3) x 1.085

Example 2:

Problem: ATrane Model S Horizontal Unit Heater is desired to deliver 280,000 Btu per hour in a garage where ventilation is required. Entering air temperature is 40 F. Steam at 30 lbs. pressure is available.Temperature to be maintained is 70 F.

Solution: Under 40 F and across from 30 lbs. inTable SP-2 page 14, find the factor 1.51.

Equivalent capacity of required unit at 2 lbs. steam 60 F entering air is

Required Btu per hour = 280,00 =185,400

F

1.51 Btu

FromTable SP-3, page 15, select a Number 186S Unit Heater with a capacity of 185,200 Btu per hour with standard coil, and at 2 lbs. steam and 60 F entering air.

The capacity of this unit at 30 lbs. steam and 40 F entering air is

1.51 x 185,200 = 279,650 Btu per hour.

Surplus Capacity

While the ventilation load is being handled, any air entering the space over the desired room temperature should be considered in the heating calculations. This surplus capacity can be found by multiplying the difference between the final temperature leaving the heater and the room temperature to be maintained by 1.085 and that by the cfm.That amount of heat can be used to offset heat losses.

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UH-PRC001-EN

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Contents UH-PRC001-EN Propeller Unit Heaters/Unitary17.4 to 705.6 MBh OctoberIntroduction The Industrial Designed Model P Unit HeaterContents Features and BenefitsSelection Procedure Electric PowerFeatures and Benefits Put HeatWhere It’s NeededThe Model S Coil The Model P MotorCompact Design Rectangular Draw-ThruCoilsModel P Model SFeatures and Benefits External Couplings Features and BenefitsApplication Considerations General RulesTypical Factory HotWater System - Using Circulating Pump General NotesApplication Considerations Vapor orVacuum System HotWater System with Circulating PumpApplication Considerations Figure AC-4 Figure AC-5 Figure AC-6Selection Procedure Trane Propeller Unit HeatersBTU Requirements Type of BuildingFormula Determining Special Steam CapacitiesUseful Data Equivalent Direct RadiationModel S Nomenclature D BESelection Procedure Model S Model PSelection Procedure Table Based on 2 PSIG and 60 F Entering AirSelection Procedure 2 Lbs. Steam 60 F Entering AirTempSelection Procedure 2 Lbs. Steam 60 F Entering AirTempSelection Procedure Table SP-6- Maximum Spread FtAdditional Selection Data Model P NomenclatureMotor and Fan Speeds Selection ProcedureSelection Procedure HotWater Selection ExampleSelection Procedure StepCorrection Factors for Propylene Glycol/Water Propylene GlycolPropylene GlycolModel Number Description MODEL P UNIT HEATERMotors D B E Model Number DescriptionMotors Performance Data Performance Data WaterPerformance Data WaterPerformance Data WaterPerformance Data Entering WaterTemperaturePerformance Data Entering WaterTemperaturePerformance Data 117.6Performance Data Entering WaterTemperaturePerformance Data Entering WaterTemperaturePerformance Data WaterPerformance Data WaterPerformance Data WaterPerformance Data 115.1Performance Data WaterPerformance Data WaterPerformance Data Entering WaterTemperaturePerformance Data Entering WaterTemperaturePerformance Data Entering WaterTemperaturePerformance Data 100.1Performance Data Entering WaterTemperaturePerformance Data Entering WaterTemperatureElectric Power Electric Power AccessoryElectric Power ModelDimensions and Weights Figure DW-1Motor MountType-1 Motor MountType-2Dimensions and Weights Figure DW-2Dimensions and Weights In Dimensions Figure DW-4Figure DW-3 Table DW-4- Louver Cone Diffuser RoughingMechanical Specifications Model P GeneralCasing Model S GeneralPage NRTL/C TheTrane Company