ME444 ENGINEERING PIPING SYSTEM DESIGN CHAPTER 10A : INDUSTRIAL HOT AND CHILLED WATER UTILITY SYSTEM.

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Presentation transcript:

ME444 ENGINEERING PIPING SYSTEM DESIGN CHAPTER 10A : INDUSTRIAL HOT AND CHILLED WATER UTILITY SYSTEM

CONTENT 1.INTRODUCTION 2.GENERATION PLANTS 3.DISTRIBUTION SYSTEM 4.INSULATION

1. INTRODUCTION APPLICATIONS (OPEN LOOP SYSTEM) DOMESTIC USE INDUSTRIAL USE –PROCESS SUPPLY –CLEANING

CONSIDERATION GENERATION STORAGE CIRCULATION INSULATION

2. GENERATION PLANTS STEAM INJECTION STEAM COIL ELECTRIC HEATER GAS BURNER

HOT WATER PLANT

CHILLED WATER PLANT

3. DISTRIBUTION SYSTEM LOOP A = PARALLEL CIRCULATION LOOP B = SERIAL CIRCULATION BRANCH C = NON-CIRCULATED BRANCH (NOT TO BE LONGER THAN 10 METERS)

TYPICAL DISTRIBUTION SYSTEM

CIRCULATION CIRCULATE WATER TO MAINTAIN TEMPEATURE HEAT LOSS T1T1 T2T2 HEAT INPUT TO END USER

CIRCULATION RATE  COMPUTE TOTAL VOLUME OF WATER IN PIPE (V)  COMPUTE TOTAL HEAT LOSS RATE  SPECIFY ALLOWABLE TEMPERATURE DROP  COMPUTE TIME REQUIRED FOR TEMPERATURE TO DROP (t)  CIRCULATION RATE > V / t

EXAMPLE COMPUTE CIRCULATION RATE FOR:  3” PIPE 200 M. LENGTH  HEAT LOSS 25 WATT/M  TEMPERATURE DROP < 2 CELCIUS VOLUME OF WATER (V) = = 3.65 CU.M. HEAT LOSS RATE = 25*200 = 5000 WATT = 5 kW HEAT LOSS FOR 2 CELCIUS DROP = 3.65m 3 x 1000kg/m 3 x 4.2kj/kg *2 C = kj TIME REQUIRED = 30660/5 = 6132 sec = 1.7 hours MIN. CIRCULATION RATE = 3.65/1.7 = 2.15 m 3 /hr = 9.45 GPM

PIPE SIZING SUPPLY PIPE DESIGN TO MEET THE DEMAND PLUS MARGIN RETURN PIPE DESIGN TO MEET THE MINIMUM CIRCULATION RATE PLUS SOME MARGIN NORMALLY RETURN PIPES ARE ONE STEP DOWN FROM THE SUPPLY PIPE KEEP POSITIVE PRESSURE WITH A BACK PRESSURE CONTROL VALVE LARGE PIPE = HIGH INITIAL COST SMALL PIPE = HIGH OPERATING COST

4. INSULATION ELASTOMICFIBRE GLASSROCK WOOL

TYPE OF INSULATION GLASS FOAM AND CELLULOSE FOAM -270C TO 100C CALCIUM SELICATE100C TO 500C CERAMIC FIBRE500C UP

THERMAL CONDUCTIVITY OF HOT INSULATION

THERMAL CONDUCTIVITY OF COLD INSULATION

INSULATION THICKNESS CONSIDERATION THICK INSULATION – TOO COSTLY THIN INSULATION – ENERGY LOSS OPTIMUM POINT EXISTS OTHER CONSTRAINTS HOT PIPE INSULATION -KEEP THE SURFACE TEMPERATURE BELOW 48 C FOR HUMAN SAFETY -KEEP WATER FROM FREEZING (IN COLD WEATHER) COLD PIPE INSULATION -PREVENT CONDENSATION -ASHRAE RECOMMEND THE THICKNESS FOR 25 W/SQ.M HEAT GAIN

RECOMMENDED HOT PIPE INSULATION THICKNESS FIBRE GLASS INSULATION

HEAT LOSS FLUID SURFACE AMBIENT CONDUCTION CONVECTION+ RADIATION FLUID INSULATION AMBIENT

HEAT TRANSFER CONDUCTION CONVECTION+ RADIATION FLUID INSULATION AMBIENT SURFACE TFTF TSTS TATA Q COND = Q CONV+RAD

CONDUCTION

CONDUCTION IN COMPOSITE CYLINDER Assumption: inside pipe temperature is close to fluid temperature. Q cond

CONVECTION Q CONV

RADIATION Q RAD =

CALCULATION OF HEAT LOSS CONDUCTION CONVECTION+ RADIATION FLUID INSULATION AMBIENT SURFACE TFTF TSTS TATA Q COND = Q CONV+RAD KNOW T F AND T A KNOW PIPE SIZE, PIPE THICKNESS AND INSULATION THICKNESS SOLVE FOR T s SET

CALCULATION SHEET

HEAT LOSS TABLE (SEE THE FULL TABLE IN THE BOOK)