Bryant 340MAV United States, Ðaltitude Derate Multiplier for U.S.A, Canada, Ðgas Rate CU FT/HR

Page 40

f.Look through sight glass in burner enclosure and check burner flame. Burner flame should be clear blue, almost transparent. (See Fig. 45.)

BURNER FLAME

BURNER

MANIFOLD

A89020

Fig. 45ÐBurner Flame

3. Verify natural gas input rate by clocking gas meter.

NOTE: Be sure all pressure tubing, combustion-air and vent pipes, and burner enclosure front are in place when checking input by clocking gas meter.

a.Calculate high-altitude adjustment (if required).

UNITED STATES

At altitudes above 2000 ft, this furnace has been ap- proved for a 2% derate for each 1000 ft above sea level. See Table 10 for derate multiplier factor.

TABLE 10ÐALTITUDE DERATE MULTIPLIER FOR U.S.A.

ALTITUDE

% OF

DERATE MULTIPLIER

(FT)

DERATE

FACTOR FOR U.S.A.*

0Ð2000

0

1.00

2001Ð3000

4Ð6

0.95

3001Ð4000

6Ð8

0.93

4001Ð5000

8Ð10

0.91

5001Ð6000

10Ð12

0.89

6001Ð7000

12Ð14

0.87

7001Ð8000

14Ð16

0.85

8001Ð9000

16Ð18

0.83

9001Ð10,000

18Ð20

0.81

 

 

 

* Derate multiplier factor is based on midpoint altitude for altitude range.

EXAMPLE:

100,000 Btuh input furnace installed at 4300 ft.

Furnace Input

 

Derate

 

Furnace Input Rate

Rate at

X

Multiplier

=

at Installation

Sea Level

 

Factor

 

Altitude

100,000

X

0.91

=

91,000

CANADA

At installation altitudes from 2000 to 4500 ft, this furnace must be derated 5% by an authorized Gas Conversion Station or Dealer. To determine correct input rate for altitude, see example above and use 0.95 as derate multiplier factor.

b.Turn off all other gas appliances and pilots.

c.Start furnace and let operate for 3 minutes.

d.Measure time (in sec) for gas meter test dial to complete 1 revolution.

Ð40Ð

e.Refer to Table 11 for cu ft of gas per hr.

TABLE 11ÐGAS RATE (CU FT/HR)

SECONDS

SIZE OF TEST DIAL

SECONDS

SIZE OF TEST DIAL

FOR 1

1

2

5

FOR 1

1

2

5

REVOLUTION

cu ft

cu ft

cu ft

REVOLUTION

cu ft

cu ft

cu ft

10

360

720

1800

50

72

144

360

11

327

655

1636

51

71

141

355

12

300

600

1500

52

69

138

346

13

277

555

1385

53

68

136

340

14

257

514

1286

54

67

133

333

15

240

480

1200

55

65

131

327

16

225

450

1125

56

64

129

321

17

212

424

1059

57

63

126

316

18

200

400

1000

58

62

124

310

19

189

379

947

59

61

122

305

20

180

360

900

60

60

120

300

21

171

343

857

62

58

116

290

22

164

327

818

64

56

112

281

23

157

313

783

66

54

109

273

24

150

300

750

68

53

106

265

25

144

288

720

70

51

103

257

26

138

277

692

72

50

100

250

27

133

267

667

74

48

97

243

28

129

257

643

76

47

95

237

29

124

248

621

78

46

92

231

30

120

240

600

80

45

90

225

31

116

232

581

82

44

88

220

32

113

225

563

84

43

86

214

33

109

218

545

86

42

84

209

34

106

212

529

88

41

82

205

35

103

206

514

90

40

80

200

36

100

200

500

92

39

78

196

37

97

195

486

94

38

76

192

38

95

189

474

96

38

75

188

39

92

185

462

98

37

74

184

40

90

180

450

100

36

72

180

41

88

176

439

102

35

71

178

42

86

172

429

104

35

69

173

43

84

167

419

106

34

68

170

44

82

164

409

108

33

67

167

45

80

160

400

110

33

65

164

46

78

157

391

112

32

64

161

47

76

153

383

116

31

62

155

48

75

150

375

120

30

60

150

49

73

147

367

 

 

 

 

 

 

 

 

 

 

 

 

f.Multiply gas rate (cu ft/hr) X heating value (Btu/cu ft) using natural gas heating value from local gas utility/supplier.

EXAMPLE: (0Ð2000 ft altitude)

Furnace input from rating plate is 100,000 Btuh. Btu heating input = Btu/cu ft X cu ft/hr Heating value of gas = 975 Btu/cu ft

Time for 1 revolution of 2-cu ft dial = 70 sec Gas rate = 103 cu ft/hr (from Table 11)

Btu heating input = 103 X 975 = 100,425 Btuh

In this example, the orifice size and manifold pressure adjustment is within ±2 percent of the furnace input rate.

B.Set Temperature Rise

CAUTION: Temperature rise must be within limits specified on unit rating plate. Recommended operation is at midpoint of rise or above. Failure to follow this caution may result in condensing or overheating the heat ex- changers.

Determine and adjust air temperature rise as follows:

1.Place thermometers in return and supply ducts as close to furnace as possible. Be sure thermometers do not see heat exchanger so that radiant heat does not affect readings. This practice is particularly important with straight-run ducts.

2.When thermometer readings stabilize, subtract return-air temperature from supply-air temperature to determine air temperature rise.

Image 40
Contents Ð1Ð ÐMultipoise OrientationsÐ2Ð DimensionsUnit Size Safety Considerations Electrostatic Discharge ESD PrecautionsMinimum Inches Clearance to Combustible Construction → ÐClearances to CombustiblesIntroduction Applications GeneralII. Upflow Applications Condensate Trap Location Factory-Shipped OrientationÐ5Ð Condensate Trap Location Alternate Upflow OrientationPressure Switch Tubing Ð6ÐCondensate Trap Freeze Protection III Downflow ApplicationsCondensate Trap Location Condensate Trap TubingIV. Horizontal Left SUPPLY-AIR Discharge Applications Ð8ÐConstruct a Working Platform Ð9ÐHorizontal Right SUPPLY-AIR Discharge Applications ÐAttic Location and Working Platform → ÐHorizontal Right Tube Configuration LocationII. Furnace Location Relative to Cooling Equipment III. Hazardous LocationsInstallation Leveling Legs if Desired → II. Installation in Upflow or Downflow ApplicationsFurnace Plenum Opening Floor Opening Casing Ðopening DimensionsWidth III. Installation in Horizontal Applications ÐDuct FlangesÐfilter Information IV. Filter ArrangementBottom Closure Panel Wiring VI. GAS PipingÐmaximum Capacity of Pipe Electrical Connections→ ÐHeating and Cooling Application Wiring Diagram II -V WiringÐWiring Diagram III. Accessories Ðelectrical DataAmps Gage AmpsDirect Venting Removal of Existing Furnaces from Common Vent SystemsII. COMBUSTION-AIR and Vent Piping GeneralExample Combustion-Air and Vent Pipe DiameterCombustion-Air and Vent Pipe Attachment COMBUSTION-AIR Intake Housing Plug Fitting ÐShort Vent 5 to 8 Ft SystemÐmaximum Allowable Pipe Length FT 2001 toÐmaximum Allowable Pipe Length FT 4001 to 5000³Vent Extension Pipe 8001 to 9000³Extended Exposed Sidewall Pipes Two-Pipe Termination KitÐRoof Termination Preferred Concentric Vent/Air Termination Kit IV. Multiventing and Vent TerminationsCondensate Drain General II. ApplicationÐConcentric Vent and Combustion-Air Sequence of Operation Heating ModeIII. Condensate Drain Protection II. Cooling Mode III. Continuous Blower ModeIV. Heat Pump Mode Component TestSTART-UP Procedures General II. Prime Condensate Trap with WaterIII. Purge GAS Lines IV. AdjustmentsSet Gas Input Rate BTU/CU FT Ð36Ð Ð37Ð Ð38Ð Ð39Ð Set Temperature Rise United StatesÐaltitude Derate Multiplier for U.S.A CanadaCheck Safety Controls Check Primary Limit Control II. Check Pressure SwitchChecklist Ðspeed SelectorChecklistðinstallation CHECKLISTÐSTART-UPLoad Calculation Combustion and Vent PipingÐ43Ð Service Training
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