NOTES:
1. ALL DIMENSIONS ARE IN
INCHES THOSE IN PARENTHESES
ARE CENTIMETERS.
2. LOCATION DIMENSIONS
ARE ALL ±1/2".
3. GAS TRAIN AND CONTROL WILL
VARY DEPENDING ON JOB
SPECIFICATIONS & CONDITIONS.
4. DIMENSIONS ARE SUBJECT
TO CHANGE WITHOUT NOTICE.
CONSULT FACTORY FOR
CERTIFIED DIMENSIONS.
5. ALL FLANGES ARE 150#
UNLESS OTHERWISE NOTED,
FLANGES TO STRADDLE
CENTER LINE.
6. SEE FORMS 1594 AND 1595 FOR
FLOW RATES AND PRESSURE DROPS
OF 2 PASS AND 4 PASS EXCHANGERS
K SERIES ATMOSPHERIC GAS
INDIRECT WATER HEATERS (K450WT-K650WT)
D
D
A
V
B
19"
(48.26)
48 1/4"
(122.56)
6 5/8"
(17.48)
9"
(22.86)
PLAN VIEW
J-2
3
14
G
SUPPLY
C
5
10
4
1
32"
(81.3)
HOT & COLD WATER
CONNECTIONS INLET & OUTLET
(SEE DETAIL 1)
17
16
EFFECTIVE DATE:
REPLACES:
4 1/2"
2 1/8"
3" NPT
4 PASS EXCH. HEAD (STD.)
6 1/4"
2 PASS EXCH. HEAD (OPT.)
MINIMUM TUBE
REMOVAL CLEARANCE
09/11/97
(SEE NOTE #6)
(SEE NOTE #6)
05/05/03
DETAIL 1
1/2"
NPT
DRAIN
4" NPT
C
2
7
12
73 1/2"
(186.69)
G
RETURN
REAR VIEW
1. PROBE TYPE LWCO-
2. BARO DRAFT CONTROL (LOOSE)
3. RELIEF VALVE
4. PRESS/TEMP GAUGE
5. CONTROL TAP 3/4" NPT
70 1/2"
(179.07)
11
6. JACKET ACCESS PANELS
7. DRAIN VALVE (EXP TANK)
8. CLNOUT./INSP. OPNG.-1 1/2"NPT
9. ELEC. ENCLOSURE-
BOILER MODEL
A-LENGTH OVER JACKET
B-FLUE LOCATION
C-FLUE DIAMETER
D-LENGTH OVER BASE
F-HEIGHT TO BAROMETRIC
SPACE HEATING SUPPLY
G-AND RETURN CONN (IF USED)
V-FLOW NOZZLE LOCATION
J1-HEAT EXCH REMOVAL CLEARANCE
J2-HEAT EXCH REMOVAL CLEARANCE
BRYAN BOILERS
J-1
1
LEFT SIDE VIEW
K450WT
129 3/4"
(329.57)
65 3/8"
(166.05)
26"
(66.04)
145 3/4"
(370.21)
99 1/2"
(252.73)
6" FLG
(15.24)
98 1/4"
(249.56)
75"
(190.50)
75"
(190.50)
11. HEIGHT OVER JACKET
12. HEIGHT OVER SUPPLY
13. DRAIN CONN 2" NPT
14. LIFTING LUGS
15. FILL VALVE10. EXP. TANK (SHIP LOOSE) 20.
6
K500WT K550WT K600WT
142 1/2"
(361.95)
71 3/4"
(182.25)
28"
(71.12)
158 1/2"
(402.59)
101 1/2"
(257.81)
6" FLG
(15.24)
111"
(281.94)
75"
(190.50)
88"
(223.52)
783 NORTH CHILI AVE
PERU, INDIANA 46970
STOP VALVE
8
15
13
FRONT VIEW
16. INDIRECT HEAT EXCHANGER
17. EXPANSION TANK CONN
18.
19.
155 1/2"
(294.97)
78 1/4"
(198.76)
30"
(76.20)
171 1/2"
(435.61)
103 1/2"
(262.89)
6" FLG
(15.24)
124"
(314.96) (339.09)
88"
(223.52) (223.52)
88"
(223.52)
165"
(419.10)
83"
(210.82)
30"
(76.20)
181"
(459.74)
103 1/2"
(262.89)
6" FLG
(15.24)
133 1/2"
88"
101"
(256.64)
D
R
O
ORDER REV. NO.:
FORM NO.:
63 5/8"
(161.61)
F
9
K650WT
178"
(452.12)
89 1/2"
(227.33)
30"
(76.20)
194"
(492.76)
103 1/2"
(262.89)
6" FLG
(15.24)
146 1/2"
(372.11)
101"
(256.64)
101"
(256.64)
:
.
O
N
R
E
1768
BRYAN BOILERS
K SERIES ATMOSPHERIC GAS
INDIRECT WATER HEATERS
BOILER MODEL K450 K500 K550 K600 K650
INPUT MBH 5,000 5,000 5,500 6,000 6,500
(KW) 1,465.0 1,465.0 1,611.5 1,758.0 1,904.5
OUTPUT* MBH 4,000 4,000 4,400 4,800 5,200
(KW) 1,172.0 1,172.0 1,289.2 1,406.4 1,523.6
BOILER HORSEPOWER HP 119 119 131 143 155
(KW) 1,171.0 1,171.0 1,288.1 1,405.2 1,522.3
TUBE DIAMETER INCHES 1.50 1.50 1.50 1.50 1.50
(CM) 3.81 3.81 3.81 3.81 3.81
NUMBER OF TUBES 67 75 83 89 97
PRESSURE VESSEL
VOLUME GAL 179 198 217 232 251
(L) 677.5 749.4 821.3 878.1 950.0
Form # >> 1768
Date >> 5/11/2004
HEATING SURFACE SQ FT 540 600 661 717 777
(SQ M) 50.2 55.8 61.4 66.6 72.2
INDIRECT HEAT EXCHANGER
HEAT EXCHANGER #1 INCHES 66 79 79 92 92
UTF(###)-(##)-(#) (CM) 167.6 200.7 200.7 233.7 233.7
HEAT EXCHANGER #2 INCHES 66 66 79 79 92
UTF(###)-(##)-(#) (CM) 167.6 167.6 200.7 200.7 233.7
OPERATING WEIGHT LBS 7,692 8,441 9,189 9,974 10,793
(KG) 3,489.2 3,828.7 4,168.2 4,524.3 4,895.5
SHIPPING WEIGHT LBS 6,200 6,790 7,380 8,040 8,700
(KG) 2,812.3 3,079.9 3,347.6 3,646.9 3,946.3
RELIEF VALVE TYPICAL - 30 PSIG (206.8 KPA)
QUANTITY 2 2 2 2 2
SIZE INCHES 1¼ x 2 2 x 2½ 2 x 2½ 2 x 2½ 2 x 2½
(CM) 3.17 x 5.08 5.08 x 6.35 5.08 x 6.35 5.08 x 6.35 5.08 x 6.35
CAPACITY-TOTAL MBH 5,800 10,500 10,500 10,500 10,500
(KW) 1,699.4 3,076.5 3,076.5 3,076.5 3,076.5
RELIEF VALVE TYPICAL - 125 PSIG (861.8 KPA)
QUANTITY 1 1 2 2 2
SIZE INCHES 1½ x 1½ 1½ x 1½ 1¼ x 1¼ 1¼ x 1¼ 1¼ x 1¼
(CM) 3.81 x 3.81 3.81 x 3.81 3.17 x 3.17 3.17 x 3.17 3.17 x 3.17
CAPACITY-TOTAL MBH 6,460 6,460 10,740 10,740 10,740
(KW) 1,892.8 1,892.8 3,146.8 3,146.8 3,146.8
* Output based on nominal 80% of input. Actual combustion efficiencies may vary.
(###) - - Indicates number of passes.
(##) - - Indicates number of tubes.
(#) - - Indicates length of exchanger.