Xylem Bell & Gossett Hoffman Speciality Series Скачать руководство пользователя страница 41

42

Flow Rate

Supply Pressure= 100 psig

(lbs./hr.)

Return Pressure=0 psig

p/L, psi/100 ft.

Pipe
Size
(in.)

1

16

1

4

1

1

2

28

62

133

3

4

62

134

290

1

120

260

544

1

1

4

250

540

1130

1

1

2

380

810

1700

2

750

1590

a

2

1

2

1200

2550

a

3

2160

4550

a

4

4460

9340

a

6

13,200

a

a

8

27,400

a

a

Flow Rate

Supply Pressure= 150 psig

(lbs./hr.)

Return Pressure=0 psig

p/L, psi/100 ft.

Pipe
Size
(in.)

1

16

1

4

1

1

2

23

51

109

3

4

50

110

230

1

100

210

450

1

1

4

200

440

930

1

1

2

310

660

1400

2

610

1300

a

2

1

2

980

2100

a

3

1760

3710

a

4

3640

7630

a

6

10,800

a

a

8

22,400

a

a

Flow Rate

Supply Pressure= 100 psig

(lbs./hr.)

Return Pressure=15 psig

p/L, psi/100 ft.

Pipe
Size
(in.)

1

16

1

4

1

1

2

56

120

1100

3

4

120

260

2400

1

240

500

4540

1

1

4

500

1060

9500

1

1

2

750

1600

14,200

2

1470

3100

a

2

1

2

2370

5000

a

3

4230

8860

a

4

8730

18,200

a

6

25,900

53,600

a

8

53,400 110,300

a

Flow Rate

Supply Pressure= 150 psig

(lbs./hr.)

Return Pressure=15 psig

p/L, psi/100 ft.

Pipe
Size
(in.)

1

16

1

4

1

1

2

43

93

200

3

4

93

200

420

1

180

390

800

1

1

4

380

800

1680

1

1

2

570

1210

2500

2

1120

2350

4900

2

1

2

1800

3780

7800

3

3200

6710

a

4

6620

13,800

a

6

19,600

40,600

a

8

40,500

83,600

a

Flow Rate

Supply Pressure= 30 psig

(lbs./hr.)

Return Pressure=0 psig

p/L, psi/100 ft.

Pipe
Size
(in.)

1

16

1

4

1

1

2

60

130

274

3

4

130

280

590

1

250

530

1120

1

1

4

520

1110

2340

1

1

2

780

1670

3510

2

1540

3270

a

2

1

2

2480

5250

a

3

4440

9360

a

4

9180

19,200

a

6

27,300

a

a

8

56,400

a

a

Flow Rate

Supply Pressure= 15 psig

(lbs./hr.)

Return Pressure=0 psig

p/L, psi/100 ft.

Pipe
Size
(in.)

1

16

1

4

1

1

2

95

210

450

3

4

210

450

950

1

400

860

1820

1

1

4

840

1800

3800

1

1

2

1270

2720

5700

2

2500

5320

a

2

1

2

4030

8520

a

3

7200

15,200

a

4

14,900

31,300

a

6

44,300

a

a

8

91,700

a

a

Flow Rate

Supply Pressure= 5 psig

(lbs./hr.)

Return Pressure=0 psig

p/L, psi/100 ft.

Pipe
Size
(in.)

1

16

1

4

1

1

2

240

520

1100

3

4

510

1120

2400

1

1000

2150

4540

1

1

4

2100

4500

9500

1

1

2

3170

6780

14,200

2

6240

13,300

a

2

1

2

10,000

21,300

a

3

18,000

38,000

a

4

37,200

78,000

a

6

110,500

a

a

8

228,600

a

a

Condensate that collects ahead of a steam
trap is approximately at saturation
temperature and corresponds to the
operating pressure. As the condensate
(normally above 212°F.) drains into the
return line, it must flash to reach saturation
temperature at atmospheric pressure. The
excess Btu’s are released in the form of
flash steam in the return lines. The return
lines must be sized to handle the volume of
steam and condensate at reasonable
velocities to minimize any backpressure.
The volume of steam is normally several
times the volume of condensate and is
generally maintained at less than 7,000 feet
per minute.
The following tables are for horizontal return
lines draining to a return system. Return
lines should pitch 1

1

2

in. per 10 ft. of

horizontal run. Select the return line size

ASHRAE
Method for
Sizing Return
Lines

based on the steam operating pressure and
the allowable    p/L, psi/100 ft. Selections for
100 and 150 psig steam for either a vented
return system or a 15 psig pressurized return
system such as a flash tank, deaerator or closed
return system.

Example: 

A condensate return system has a

steam supply at 100 psig and the return line is
at 0 psig and not vented. The return line is
horizontal and must have a capacity of 2500
lbs./hr. What size pipe is required?

Solution: 

Since the system will be throttling

non-subcooled condensate from 100 psig to 0
psig there will be flash steam and the system
will be a dry-closed return with horizontal pipe.
Select a pressure drop of 

1

4

psi/100 ft. and

use a 2

1

2

in. pipe for this system.

For these sizes and pressure losses, the velocity is above 7000 fpm.
Select another combination of sizes and pressure loss.

Reprinted by permission of the American Society of Heating, Refrigeration and Air-Conditioning
Engineers, Atlanta, Georgia, from the 1989 ASHRAE Handbook-Fundamentals

a

FLOW RATE (lbs./hr.) FOR DRY RETURN LINES

Flow Rate

Supply Pressure= 50 psig

(lbs./hr.)

Return Pressure=0 psig

p/L, psi/100 ft.

Pipe
Size
(in.)

1

16

1

4

1

1

2

42

92

200

3

4

91

200

420

1

180

380

800

1

1

4

370

800

1680

1

1

2

560

1200

2520

2

1110

2350

a

2

1

2

1780

3780

a

3

3190

6730

a

4

6660

13,800

a

6

19,600

a

a

8

40,500

a

a

Содержание Bell & Gossett Hoffman Speciality Series

Страница 1: ...Hoffman Specialty Steam Traps HS 203C ENGINEERING DATA MANUAL Application Selection Installation Piping Diagrams...

Страница 2: ...ng Pressure Limits 17 Installation and Calculating Differential Pressure 18 Drip Traps for Distribution Pipes 20 Chapter 3 Selecting Traps for Heat Exchangers 24 Lock out Traps for Start up Loads 27 D...

Страница 3: ...charge To assure condensate drainage there must be a positive differential pressure across the trap under all load conditions Water Hammer When a trap drains high temperature conden sate into a wet re...

Страница 4: ...ntages Completely drains condensate at satura tion temperature Modulates to handle light or heavy loads continuous discharge equal to condensing load Large ports handle high capacities Separate thermo...

Страница 5: ...hon type or tilting kettles 6 INLET OUTLET COVER BODY V BUCKET A STEAM BUBBLES THROUGH WATER INLET OUTLET COVER BODY V BUCKET A STEAM BUBBLES THROUGH WATER INLET OUTLET COVER BODY V BUCKET A BUCKET TR...

Страница 6: ...inexpensive Fast response to changing conditions Fail open models Disadvantages Water hammer can damage bellows Superheat can damage bellows if it exceeds trap temperature rating Pressure limit of 125...

Страница 7: ...re maximum tem perature is required Outdoor applications including drips on steam mains Drying tables Tire mold press and vulcanizing equipment Dry kilns Pressing machines Rugged applications superhea...

Страница 8: ...hitting the disc Operating As the condensate nears saturation tempera ture greater amounts of flash steam will appear Some of the flash steam escapes to the area above the disc causing the pressure ab...

Страница 9: ...sed only as a guide 10 Chapter 1 Condensate must be completely removed at saturation condition to prevent water hammer Type of Steam Trap Required Based on System Conditions Modulating load wide range...

Страница 10: ...p 3 Apply Safety Factor A SFA Recommended 1 Float Thermostatic Trap 1 5 to 2 5 2 Bucket Trap 2 to 4 3 Thermostatic 2 to 4 4 Disc Traps 1 to 1 2 See specific applications B The SFA Will Depend On Degre...

Страница 11: ...cury 13 6 inches water column Size condensate receivers for 1 min net storage capacity based on return rate Size condensate pumps at 2 to 3 times condensate return rate W x Sh x T2 T1 L x T Helpful Hi...

Страница 12: ...of objects as opposed to latent heat In the sat uration tables it is the Btu remaining in the condensate at saturation temperature Latent Heat The amount of heat expressed in Btu required to change 1...

Страница 13: ...5 353 3 21 324 1193 867 130 355 3 12 327 1194 867 135 358 3 02 329 1194 864 140 361 2 92 332 1195 862 145 363 2 84 335 1196 860 Specfic Heat Content Latent Pressure Saturated Volume Btu per Ib Heat of...

Страница 14: ...600 Pipe Size PRESSURE PSI GAUGE Inches 5 10 15 30 50 75 100 125 200 250 1 2 30 40 45 60 90 120 150 180 270 330 3 4 55 70 80 110 160 220 280 340 510 620 1 90 110 125 180 270 390 460 560 840 1020 11 4...

Страница 15: ...the flash loss and required heating of make up water to replace the flash loss The amount of make up water and water cost can also be determined using this form How to Calculate Your Own Flash Steam...

Страница 16: ...al operating pressure is higher than the seat rating the differential pressure across the seat will prevent the trap from opening Thus the trap must be selected for the maximum differential pressure t...

Страница 17: ...e of the trap required Piping Details A dirt pocket should be provided ahead of the steam trap to collect scale and dirt A shut off valve should be provided ahead of the trap to permit service Straine...

Страница 18: ...ressure in the return line minus static head in the discharge piping Trap capacities should be calculated at the minimum differential pressure to assure com plete condensate drainage Lifts in the retu...

Страница 19: ...ators The size and type of drip traps used will depend on the method used in heating the steam mains to final pressure and tempera ture The two methods commonly used are automatic start up and supervi...

Страница 20: ...x T1 T2 x 114 L W Weight of pipe see table below for weight per ft T1 Steam temperature at saturation T2 Initial pipe temperature at ambient L Latent heat of steam at final operating pressure 114 Spec...

Страница 21: ...a gravity return line this would be 30 psi Step 4 Select the trap Based on the previous description of traps if the trap from a steam header is not subject to freezing conditions the normal selection...

Страница 22: ...o allow conden sate to flow back into main When the branch line is over 10 ft pitch the branch line toward the control valve and install a steam trap The steam trap should be as close to the control v...

Страница 23: ...ing rate at design pressure is not the only load the trap must handle The condens ing load of a heat exchanger designed for 15 psi may in fact be in excess of 90 at 0 psig When the heat exchanger is s...

Страница 24: ...ws Select capacity based on maximum con densing load at minimum differential pressure that can occur The heat exchanger manufac turer can provide this information No lifts should be installed in the r...

Страница 25: ...bottom outlet for the condensate drainage When a modulating steam regulator is used on the steam to water heat exchanger the vacuum breaker will allow air to enter to pre vent an induced vacuum from h...

Страница 26: ...ground steam lines during start up The low pressure trap con nected to an open drain or sump drains con densate during start up When the steam line pressure exceeds the trap rating it will close and r...

Страница 27: ...ted to the overhead return line with a check valve to prevent backflow The second trap may be a low pressure trap When condensate backs up 4 inches it will drain into the second trap which will drain...

Страница 28: ...ized one pipe size smaller than the trap inlet but never less than 1 2 pipe size The coils in Figures 2 3 and 4 are of the con tinuous type Coils are often multi circuited A safety factor of 4 is need...

Страница 29: ...y The excellent air handling capability of Thermostatic Traps makes them suitable for trapping applications where quick air removal is required For example batch processes resulting in on off operatio...

Страница 30: ...heat load is required Small low pressure unit heaters up to 15 psi often use Thermostatic Traps Large unit heaters or those operating at higher pressure may use F T as first choice and Bucket Traps a...

Страница 31: ...elation to other types of traps This makes them attractive for heating systems where many large numbers of traps are required Trap Damage from Water Hammer When automatic temperature controlled sup pl...

Страница 32: ...NPULL SUPPLY MAIN NO PRESSURE WET RETURN REDUCING ELL NOT LESS THAN 24 WATERLINE OF BOILER SUPPLY VALVE WITH CHAINPULL TRAP FULL SIZE OF TAPPING DRY RETURN MAIN MINIMUM COOLING LEG 5 0 LONG SUPPLY VAL...

Страница 33: ...CKET SUPPLY LINE STRAINER UNIT HEATER MINIMUM COOLING LEG 5 0 LONG SAME SIZE AS TRAP TRAP TRAP SUPPLY MAIN GATE VALVE GRAVITY VACUUM DRY RETURN MAIN FULL SIZE OF TAPPING Low pressure closed gravity sy...

Страница 34: ...UNION PITCH DOWN PITCH DOWN PITCH DOWN Distance from center of radiator tapping to face of sill must be given Straight extended stem on supply valve TRAP DIRT POCKET TRAP GATE VALVE DIRT POCKET DIRT...

Страница 35: ...ALVE TRAP MINIMUM COOLING LEG 5 0 LONG RISER PITCH DOWN FROM HERE PACKLESS RADIATOR VALVE AIR VALVE SUPPLY MAIN PITCH DOWN FROM HERE PACKLESS RADIATOR VALVE AIR VALVE Upfeed connection to radiator Rad...

Страница 36: ...LEAST 24 DIRT POCKET AT LEAST 18 ABOVE W L WET RETURN AT LEAST 12 One pipe steam systems convector connections Venting concealed radiator of header type air vent tapping in top Dripping end of one pi...

Страница 37: ...n at 45 Expansion joint made up of pipe for risers Drop riser branch taken from top of main at 45 Drop riser taken from bottom of main Riser branch taken from bottom of main and dripped into wet retur...

Страница 38: ...xi mum heat transfer They are inexpensive and the Hoffman 650 Series allow com plete replacement of the seat and disc without removing the trap body from the line 3 Thermostatic Traps open in response...

Страница 39: ...Friction Factor where flow of condensate does not inhibit the flow of steam Basic Chart for Weight Flow Rate and Velocity of Steam in Schedule 40 Pipe Based on Saturation Pressure of 0 PSIG Figure 10...

Страница 40: ...le size 41 Velocity Multiplier Chart Figure 10 continued Reprinted by permission from ASHRAE 1972 Handbook of Fundamentals Example of Use of Basic and Velocity Multiplier Charts Given a Weight Flow Ra...

Страница 41: ...0 a a 8 228 600 a a Condensate that collects ahead of a steam trap is approximately at saturation temperature and corresponds to the operating pressure As the condensate normally above 212 F drains in...

Страница 42: ...to test operation You will be looking for two phase flow in the discharge line Two phase flow has steam in the discharge line and will be over 212 F along the piping Flash steam normally con denses i...

Страница 43: ...osion Must distinguish between live steam flash steam Crushed ball failure mode is closed 44 THERMOSTATIC TRAP IS TRAP CYCLING TIGHT CLOSURE BETWEEN CYCLES GOOD TRAP REPLACE OR REPAIR IS RUSHING STEAM...

Страница 44: ...AP CAN CYCLES BE HEARD SHUT TIGHT BETWEEN DISCHARGES GOOD TRAP IS RUSHING STEAM HEARD OR SEEN NO YES YES NO CONTINUOUS DISCHARGE LOAD APPROACHING TRAP CAPACITY NO IS RUSHING STEAM SEEN OR HEARD YES GO...

Страница 45: ...re The weight of a column of air one square inch in cross section and extending from the earth to the upper level of the blanket of air surrounding the earth This air exerts a pressure of 14 7 pounds...

Страница 46: ...ater with steam without mixing the two It may be used for supplying hot water for domestic purposes or for a hot water heating system Cooling Leg A length of uninsulated pipe through which the condens...

Страница 47: ...vectors base boards finned tubing coils embedded in floor wall or ceiling or any device which transmits the heat from the heating system to the room and its occupants Horsepower A unit to indicate the...

Страница 48: ...n EDR By definition that amount of heating surface which will give off 240 Btu per hour when filled with a heating medium at 215 F and surrounded by air at 70 F The equivalent square foot of heating s...

Страница 49: ...ar atmo spheric pressure and returns the condensation to the boiler or receiver by gravity Velocity Pressure The pressure used to create the velocity of flow in a pipe It is expressed as a unit pressu...

Страница 50: ...to meet our world s water needs Developing new technologies that will improve the way water is used conserved and re used in the future is central to our work We move treat analyze and return water t...

Отзывы: