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Chapter 9

System Installations

This Chapter contains information on:

 

Appliance Installation

  1. Install shut-off valve between supply line and appliance at all appliance connections.
  2. Check pilot flame and main burner air.
  3. Check all connections on application as well as hook-up connection for leaks with leak detector.
  4. Re-light all pilot burners.
  5. Check for good venting, when venting is required.
  6. For additional information on appliance hook-up and venting refer to NFPA Pamphlet 54.
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Venting of Propane Fired Appliances

Law requires the proper venting for a Propane appliance unless the appliance is listed and approved as an unvented unit. The vent system may not be required for low output BTU clean burning units. However, it is very necessary to remove harmful combustion gases to the outside atmosphere.

The temperature of Propane products for combustion is very low when compared to liquid or solid fuel. Vent gases from Propane have been recorded as low as 93° F and as high as 450° F. This low temperature makes it possible to use smaller vents and the vents can be located in 2 X 4 walls using specially designed vents for the venting system.

For each 100,000 BTU of Propane consumed, the vent must remove 240 pounds of vent gases to the outside. The low temperature vent system makes the job harder, as the energy to move the 240 pounds is heat.

In the event the vent is too large or located where it is exposed to very cold air, the vent gases may start to condense and change to sulfuric acid, which attracts metal, wood, etc., and in addition, does not remove the vent gases to the outside.

Check all units for proper venting using a Carbon Monoxide Detector smoke or a match flame at the draft hood. With burning operating, the smoke or flame should be drawn into the vent hood opening for proper venting. If match of smoke is blown out, vent is spilling flue gases, and must be corrected.

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Refer to NFPA Pamphlet 54, Part 7, Venting of Equipment for proper installation regulations.

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Propane Service Precautions

Dirt, chips, or moisture are the greatest problems of the Propane system. The items listed below are to assist you in reducing troubles from these causes:

  1. All empty containers should always have valves closed. Tanks are dehydrated. If valve is opened, they will breathe, causing moisture to form.
  2. Tanks received or found with valve open at any time should have alcohol installed on the first fill of the tank. Alcohol can be used, as a precaution, on all new tanks at time of first fill. (Usually ½ gallon in 500-gallon tank and 1 gallon in 1000-gallon tank.)
  3. Regulators should always have openings plugged or taped over when removed from system or in stock. KEEP DIRT AND CHIPS OUT OF REGULATORS.
  4. Al tubing should be plugged, taped or mashed closed as soon as the piece to be used id removed from the coil. KEEP DIRT, CHIPS AND MOISTURE OUR OF TUBING.
  5. All tubing should be reamed and flared in position so dirt and chips will fall out instead of down into tubing. KEEP DIRT AND CHIPS OUT OF TUBING.
  6. Where it is possible, tubing should be blown out before regulator is hooked up. This may remove dirt or chips that would give you trouble later. KEEP DIRT AND CHIPS OUT OF PROPANE SYSTEMS.
  7. All cylinders, filled or empty, should be stored in upright position with cylinder cap or collars in place to protect the valve wheel.

When making installations of Propane, think of what can make trouble for you later on and take precautions to prevent these things from happening.

Always install regulator with the vent down or install vent suppressor (Fisher 4602-1 or 4602-11 or a Rego 1493A) when a regulator must be mounted with the vent up or on its side.

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Regulator Failures

Chips or dirt getting into the regulator orifice at the seat causes most regulator failures and becoming embedded in the seat, which causes the seat to leak when closed. The pressure will build up under the diaphragm to 28" water column and at that point, a relief valve at the diaphragm stem will open and bypass the excess pressure out through the regulator vent. For this reason, all regulators installed inside of buildings MUST be vented outside.

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A recommended practice is to replace regulators after fifteen (15) years of service. See the NFPA Propane Regulator Date Code Chart below.

  

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REGO

Propane Regulator Selector

Type of

System

Maximum

Load BTU/Hr.

Suggested

Regulator

First Stage in a

Two Stage System

500,000 (a)

LV2302TR

2,500,000 (b)

LV4403SR Series
LV4403TR Series
Second Stage in a

Two Stage System

935,000 (C)

LV4403B Series

1,600,000 (C)

LV5503B4/B6/B9

2,300,000 (c)

LV5503B8
Integral

Twin Stage

200,000 (d)

LV404B23 Series

525,000 (d)

LV404B4 Series
LV404B9 Series
Automatic

Changeover

180,000 (d)

7523B23 Series

500,000 (d)

7523B4 Series
  1. Maximum load based on 25 psig inlet, 8 psig delivery pressure.
  2. Maximum load based on inlet pressure 20 psig higher than setting and delivery pressure 20% lower than setting.
  3. Maximum load based on 10 psig inlet, 9" water column delivery pressure.
  4. Maximum load based on 25 psig inlet, 9" water column delivery pressure.

 

 

FISHER

Propane Regulator Selector

Type of Regulator or Service

Capacity, BTU/Hr.

Recommended Fisher Regulator

First Stage 1

(Reduces tank pressure to 10 psig or less)

900,000

1,100,000-2,600,000

R312H

R522H

Second Stage2

(Reduces first stage outlet pressure to 14" W.C. or less

270,000

875,000-1,375,000

1,600,000-2,400,000

2,025,000

5,512,000

8,000,000-12,500,000

R312

R522

S102CL

R422

S302G

S202G

Integral Two-Stage

(Combines a high pressure and a second stage regulator)

275,000

685,000-1,100,000

1,700,000

R332

R522

R432

High Pressure3

(Reduces tank pressure to a lower pressure in excess of 1 psig)

600,000-1,150,000

2,625,000-5,250,000

9,800,000-20,400,000

6,080,000-10,773,000

14,000,000

29,295,000-36,225,000

67 or 67G

64 or 64SR

Type 299

627

630-104/78

99

2 PSIG2 Service

(Reduces first stage pressure to 2 PSIG)

400,000

R312E

  1. Based on 30 psig inlet pressure and 20% drop
  2. Based on 10 psig inlet pressure and 20% drop
  3. Based on inlet pressure 20 psig greater than outlet pressure with 20% drop

Note: The capacity BTU/Hr. column should be used for reference purposes only. The capacity will vary depending on the pipe size, orifice size and outlet pressure setting.

 

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Propane and Natural Gas Orifice Capacities

When converting gas burning equipment from one gas to another, the serviceman needs to know what a given drill size will handle in BTU’s of both Propane and Natural Gas. To assist you in converting gas equipment, we are attaching two sheets showing this information for your reference. These will come in handy when a serviceman is required to convert appliances to Propane from Natural Gas or Natural Gas to Propane.

 

Examples of how to use these charts on converting from Natural to Propane gas follows….

  1. Measure orifice, using drill kit. We will use #55 drill size for the example.
  2. Using the Natural gas chart, read across from #55 drill….which is 10,640 BTU.
  3. Using the Propane chart, read down to closest BTU to 10,640….which is 10,420 BTU.
  4. Read across to drill size….which is #62.
  5. Using new orifice pre-drilled to #80 pilot (so orifice will be drilled straight), drill using #62 drill.
  6. Install orifice.
  7. Install burner.
  8. Light burners
  9. Adjust air for correct flame.

(See Conversion Charts Below)

PROPANE ORIFICE CAPACITY

11 INCH WATER COLUMN

Drill Size

Propane

Butane

Drill Size

Propane

Butane

80

1248

1409

51

32630

36840

79

1448

1635

50

35730

40340

78

1769

1998

49

38950

44100

77

2275

2570

48

42375

47860

76

2842

3215

47

45560

51500

            

75

3120

3544

46

48900

55250

74

3624

4095

45

59440

56830

73

4152

4690

44

55500

62650

72

4510

5100

43

59440

67160

71

4880

5508

42

64620

74160

            

70

5660

6395

41

69175

78150

69

6156

6950

40

72000

81400

68

6940

7834

39

74380

84000

67

7382

8340

38

77400

87400

66

7853

8865

37

81125

91640

           

65

8841

9975

36

85170

96150

64

9350

10570

35

90800

120700

63

9877

11160

34

92500

104500

62

10420

11780

33

96000

108300

61

10986

12400

32

100900

114000

            

60

11540

13030

31

108125

122130

59

12115

13700

1/64

1680

1897

58

12720

14375

1/32

7030

7935

57

13355

15080

3/64

15960

17970

56

15600

17600

1/16

28320

32999

            

55

19550

22120

5/64

45150

51000

54

21960

24820

3/32

65920

74500

53

25630

29000

7/64

89825

101500

52

29220

33060

1/8

117150

132400

 

NATURAL GAS ORIFICE CAPACITIES

7 Inch Water Column,

1120 BTU/Cu. FT

Drill Size

BTU/Hr.

Drill Size

BTU/Hr.

60

6270

36

44580

59

6610

7/64

46930

58

6940

35

47490

57

7280

34

48380

56

8510

33

50180

         

3/64

8620

32

52860

55

10640

31

56560

54

11870

1/8

61380

53

13890

30

64740

1/16

15330

29

72580

         

52

15900

28

77390

51

17580

9/64

77620

50

19260

27

81420

49

20940

26

84780

48

22740

25

87700

         

5/64

23970

24

90720

47

24190

23

93070

46

25760

5/32

95760

45

26430

22

96770

44

29010

21

99230

         

43

31140

20

101810

42

34380

19

108190

3/32

34500

18

112780

41

36180

11/64

115920

40

37630

17

117490

         

39

38860

16

122980

38

40430

15

127230

37

42450

   

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Revised March, 1999

 
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