background image

1

12

2

C

CH

HE

EC

CK

KIIN

NG

G  IIN

NP

PU

UT

T  R

RA

AT

TE

E

T

Ta

ab

blle

e  4

4  --  M

Me

ette

err--T

Tiim

miin

ng

g  G

Ga

as

s

Time required for one revolution is charted for various size
meter dials and various rates of gas input in cu. ft. per hour. To
convert to BTUH, multiply by the heating value of the gas
used.

T

Tiim

me

e  ffo

orr  1

1

IIn

np

pu

utt,,  C

Cu

u..  F

Ftt..  p

pe

err  H

Ho

ou

urr,,

R

Re

ev

vo

ollu

uttiio

on

n,,

W

Wh

he

en

n  M

Me

ette

err  D

Diia

all  S

Siiz

ze

e  iis

s::

1

1//2

2  c

cu

u..  fftt..

1

1  c

cu

u..  fftt..

2

2  c

cu

u..  fftt..

5

5  c

cu

u..  fftt..

10

180

360

720

1800

12

150

300

600

1500

14

129

257

514

1286

16

112

225

450

1125

18

100

200

400

1000

20

90

180

360

900

22

82

164

327

818

24

75

150

300

750

26

69

138

277

692

28

64

129

257

643

30

60

120

240

600

35

51

103

206

514

40

45

90

180

450

45

40

80

160

400

50

36

72

144

360

55

33

65

131

327

60

30

60

120

300

70

26

51

103

257

80

22

45

90

225

90

20

40

80

200

100

18

36

72

180

120

15

30

60

150

S

Se

ec

c..

T

Ta

ab

blle

e  6

6  --  O

Orriiffiic

ce

e  D

Drriillll  S

Siiz

ze

es

s  w

wiitth

h  D

De

ec

ciim

ma

all  E

Eq

qu

uiiv

va

alle

en

ntts

s

M

Ma

aiin

n  B

Bu

urrn

ne

err  O

Orriiffiic

ce

es

s

D

Drriillll

D

Diia

a..

D

Drriillll

D

Diia

a..

S

Siiz

ze

e

D

De

ec

ciim

ma

all

S

Siiz

ze

e

D

De

ec

ciim

ma

all

E

Eq

qu

uiiv

va

alle

en

ntt

E

Eq

qu

uiiv

va

alle

en

ntt

48

.0760

31

.1200

45

.0820

30

.1285

43

.0890

27

.1440

42

.0935

26

.1470

40

.0980

25

.1495

37

.1040

23

.1540

20

.1285

P

Piillo

ott  O

Orriiffiic

ce

e  S

Siiz

ze

es

s  ((iin

nc

ch

he

es

s))

P

Piillo

ott  T

Ty

yp

pe

e

N

Na

attu

urra

all

P

Prro

op

pa

an

ne

e

J640DHA

.015

.010

J993DHW

0.18

.010

J994DHW

Q345

.018

.012

5CHL-6

.018

.010

5SL-6ER

.018

.010

T

Ta

ab

blle

e  5

5  --  M

Ma

an

niiffo

olld

d  P

Prre

es

ss

su

urre

e  a

an

nd

d    G

Ga

as

s  C

Co

on

ns

su

um

mp

pttiio

on

n**

T

Ty

yp

pe

e  o

off  G

Ga

as

s

N

Na

attu

urra

all

P

Prro

op

pa

an

ne

e

M

Mo

od

de

ell

B

BT

TU

U//C

Cu

u..  F

Ftt..

1

10

04

40

0

2

25

50

00

0

N

No

o..  o

off

S

Siiz

ze

e

S

Sp

pe

ec

ciiffiic

c  G

Grra

av

viitty

y

0

0..6

60

0

1

1..5

53

3

O

Orriiffiic

ce

es

s

M

Ma

an

niiffo

olld

d  P

Prre

es

ss

s..  IIn

n..  o

off  H

H2

2O

O

3

3..5

5

1

10

0""

Cfh

72.1

30.0

D

DJ

JE

E7

75

5

Gal./Hr. Propane

.82

1

SEC/Cu. Ft.

50

120

Orifice Drill Size

20

37

Cfh

96.1

40.0

D

DJ

JE

E1

10

00

0

Gal./Hr. Propane

1.09

2

SEC/Cu. Ft.

37.5

90

Orifice Drill Size

30

45

Cfh

120.2

50.0

D

DJ

JE

E1

12

25

5

Gal./Hr. Propane

1.37

3

SEC/Cu. Ft.

29.9

72

Orifice Drill Size

31

48

Cfh

144.2

60.0

D

DJ

JE

E1

15

50

0

Gal./Hr. Propane

1.64

3

SEC/Cu. Ft.

24.9

60.0

Orifice Drill Size

30

45

Cfh

192.0

80.0

D

DJ

JE

E2

20

00

0

Gal./Hr. Propane

2.19

3

SEC/Cu. Ft.

19

45

Orifice Drill Size

23

40

Cfh

216.3

90.0

D

DJ

JE

E2

22

25

5

Gal./Hr. Propane

2.46

3

SEC/Cu. Ft.

16.6

40.0

Orifice Drill Size

20

37

Cfh

240.0

90.0

D

DJ

JE

E2

25

50

0

Gal./Hr. Propane

2.74

4

SEC/Cu. Ft.

15

36

Orifice Drill Size

25

42

Cfh

288.4

120.0

D

DJ

JE

E3

30

00

0

Gal./Hr. Propane

3.28

5

SEC/Cu. Ft.

12.5

30.0

Orifice Drill Size

26

43

Cfh

336.0

140.0

D

DJ

JE

E3

35

50

0

Gal./Hr. Propane

3.83

6

SEC/Cu. Ft.

10.7

25.7

Orifice Drill Size

27

43

Cfh

385.0

160.0

D

DJ

JE

E4

40

00

0

Gal./Hr. Propane

4.37

6

SEC/Cu. Ft.

9.3

22.5

Orifice Drill Size

23

40

*Above gases based on average standards. Units can be furnished for gases of

different values and specific gravities. (

Gal./Hr. based on 60°F. 30" Hg., 91,500

BTU/Gal.).

In Canada, refer to rating plate on side of unit for orifices at high altitude.

Summary of Contents for DJE

Page 1: ...ou ut t n no ot ti ic ce e C Co on nt te en nt ts s Page Inspection on arrival 1 Installation 2 8 Operation 9 10 Checking input rate 10 12 Performance data 13 16 Dimensional data 17 Service instructio...

Page 2: ...00 square inches for each opening 13 Do not install unit outdoors 14 Do not locate unit closer to combustible materials than 6 inches 15 The maximum allowable temperature rise through any Modine duct...

Page 3: ...downstream of cooling systems may experience condensation therefore provisions should be made for disposal of condensate Means have been provided in the bottom pan of the unit to accommodate a condens...

Page 4: ...Be certain that neither the sensing bulb nor the capillary tube come in direct contact with the heat exchanger The exposed capillary tube should be protected from damage due to cuts blows or wear from...

Page 5: ...lications however where it is desirable to have the control string on the same side of the unit as the vent connector For these applications the control string position may be reversed To reverse the...

Page 6: ...as having non positive pressure vent systems and must not be common vented with positive pressure vent systems serving Category III and IV appliances 5 Category II vent systems must be installed to pr...

Page 7: ...p pocket before each unit and in the line where low spots cannot be avoided See Figure 6 7 Take off to unit should come from top or side of main to avoid trapping condensate 8 Piping subject to wide t...

Page 8: ...0 1 10 05 5 1 12 20 0 1 15 50 0 1 18 80 0 2 21 10 0 2 24 40 0 2 27 70 0 3 30 00 0 4 45 50 0 6 60 00 0 D Di ia am me et te er r o of f P Pi ip pe e I In nc ch he es s T Ta ab bl le e 3 3 S Sp pe ec ci...

Page 9: ...and pressure P Pi il lo ot t F Fl la am me e A Ad dj ju us st tm me en nt t The pilot is orificed to burn properly with an inlet pressure of 6 7 W C on natural gas and 11 14 W C on propane gas but fi...

Page 10: ...opane gas some yellow tipping is always present but is not objectionable C Ch he ec ck ki in ng g I In np pu ut t R Ra at te e I In np pu ut t A Ad dj ju us st tm me en nt ts s Gas pressure regulators...

Page 11: ...by the second formula the input is 100 cu ft per hr Table 4 indicates the time for one revolution of various size meter dials with various input rates If a 1 cu ft meter dial is used we proceed down...

Page 12: ...p pa an ne e J640DHA 015 010 J993DHW 0 18 010 J994DHW Q345 018 012 5CHL 6 018 010 5SL 6ER 018 010 T Ta ab bl le e 5 5 M Ma an ni if fo ol ld d P Pr re es ss su ur re e a an nd d G Ga as s C Co on ns s...

Page 13: ...rating table Less than the minimum air flow CFM through the duct furnace will cause air temperature rise to exceed the maximum rise allowed The maximum allowable final air temperature is 150 F The ma...

Page 14: ...ve 1 at 2000 cfm Read up the graph until the 2000 cfm line intersects the performance curve for a size 100 At the point of intersection read across to the left and find the air temperature rise For th...

Page 15: ...80 75 70 65 60 55 50 45 40 35 30 25 20 1 1 5 2 2 5 3 3 5 4 4 5 5 5 5 6 6 5 7 7 5 8 8 5 P Inches Water Column P PR RE ES SS SU UR RE E D DR RO OP P V VS S C CF FM M With Air Baffle C CA AU UT TI IO ON...

Page 16: ...5 50 45 40 35 30 25 20 2 3 4 5 6 7 8 9 10 11 12 300 300 P PR RE ES SS SU UR RE E D DR RO OP P V VS S C CF FM M P Inches Water Column CFM x 1000 With Air Baffle C CA AU UT TI IO ON N Do not exceed 100...

Page 17: ...i ip pp pi in ng g W Wt t 85 95 138 183 183 206 260 308 For natural gas Weight in pounds L Li im mi it t C Co on nt tr ro ol l O Ov ve er rh he ea at t S Sw wi it tc ch h The limit control will shut o...

Page 18: ...n reverse order being careful to align the burner assembly properly on the alignment pins on the access panels on both sides of the duct furnace see Figure 12 B Bl lo oc ck ke ed d V Ve en nt t S Sa a...

Page 19: ...ion of negative pressure is that outside doors tend to swing toward inside of building Note 1 Note 2 F Fi ig gu ur re e 1 14 4 B BV VS SS S T Tr ro ou ub bl le es sh ho oo ot ti in ng g F Fl lo ow w C...

Page 20: ...ion usually can be eliminated by reducing primary air The burner may also be operating below its rated capacity Check input rate and adjust to correct value by increasing orifice size or manifold gas...

Page 21: ...off gas supply to main burners This may result from a plugged orifice dirty pilot valve or poor adjustment 2 Check electrical connections from the thermocouple element to the safety valve to assure g...

Page 22: ...ockage in main burner orifice P Po os ss si ib bl le e R Re em me ed dy y 3a Check flame sensing rod ceramic sensor sensor lead and connections for damage or loss of continuity Replace defective eleme...

Page 23: ...t P Pi il lo ot t I Ig gn ni it ti io on n 1 10 00 0 S Sh hu ut t O Of ff f w wi it th h C Co on nt ti in nu uo ou us s R Re et tr ry y 63 115V 25V natural Utilizes a two stage combination gas contro...

Page 24: ...9 Series Identity Number Identifies which series of controls were furnished on the unit Year of Manufacture 96 1996 97 1997 etc Sequence number Week of Manufacture 01 First week of year 26 26th week o...

Page 25: ...ation Serviced By Initials I In ns st ta al ll le ed d D Da at te e S Se er rv vi ic ce e D Da at ta a N No ot te e t to o S Se er rv vi ic ce e T Te ec ch hn ni ic ci ia an n F Fi il ll l i in n d da...

Page 26: ......

Page 27: ...OF EQUIPMENT MANUFACTURED BY BUYER BUYER S REMEDY FOR BREACH AS LIMITED HEREIN SHALL BY LIMITED TO ONE YEAR FROM DATE OF SHIPMENT FROM MODINE FOR GAS FIRED PRODUCTS INSTALLED IN HIGH HUMIDITY APPLICA...

Page 28: ...H HV VA AC C R R D Di iv vi is si io on n Modine Manufacturing Company 1221 Magnolia Avenue Buena Vista Virginia 244416 Phone 1 800 828 4328 HEAT Fax 540 261 1903 Service Parts Modine Manufacturing C...

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