effiqamax deliver process steam maximising efficiency & quality to · traveling grate: mainly...
TRANSCRIPT
SAFETY FEATURES
Pressure Safety Valves Low, Medium & High Level switches
Bed Temperature Sensors & Monitoring
HMI with SCADA provides comfort to the operatorsIt monitors & controls the fuel feeding & balances the draft. Combustion Control manages the fuel savingsTurn down is maintained based on the steam demand
Automation:
Product Features:Packaged and CompactSaddle or skid mountedReady to installQuick startup & reduced supervisionHigh efficiency
An ISO 9001:2015 Certified EPC Company and
ASME,U,S, PP & R Certified ManufacturerIBR 1950,
REGISTERED OFFICETagore Towers, H.No 1-62-191, Plot No 191,
st1 Floor, Tagore Towers, Kavuri Hills,
Madhapur, Hyderabad - 500 033, India
Phone: +91(40)4002 3338, Fax: +91(40)4002 3336
E-Mail: [email protected]
SOUTH EAST ASIAE-Mail: anant.mahore@
mahathiinfra.com
Ph: +66 92 33 65 500
FACTORYE-Mail: [email protected]
SALES & MARKETINGE-Mail: [email protected]
Ph: +91-90000-70851
AFRICAE-Mail: [email protected]: +256-759 647 131
EffiQamax Maximising Efficiency & Quality to deliver Process Steam
We add value to your needs....
SOLID FUEL FIRED BOILERS COMBINED FIRE & WATER TUBE DESIGN
OIL & GAS FIRED BOILERS WITH ECCENTRIC FURNACE DESIGN
Up to 25 bar operating pressure for Processindustries
PRESSURE CAPACITY
1 tph to 30 tph Standard products & abovecapacities as customized products
18
72
Allows greater disposabilityof water therefore a quicker response to the steam demand fluctuations in the process.
Tube bundles are placed on one side with a fully wet back furnace which allows smooth flow of flue gases in reversal chamber.
PRINCIPLE OF OPERATION FOR OIL & GAS FIRED BOILERS
Oil & Gas fired boilers generate steam by combustion of Liquid or gaseous fuels like FO,
LPG, NG etc.
3 Pass design brings higher efficiency whichutilizes maximum heatof flue gas.
ECCENTRIC FURNACE DESIGN
We add value to your needs....
2
We
ad
d va
lue
to yo
ur n
ee
ds....
General A
rrangement D
rawing
FL
UE
GA
S IN
LE
T &
OU
TL
ET
AIR
INL
ET
OV
ER
FL
OW
RC
CB
LO
WD
OW
N
PIT
FE
ED
PU
MP
WIT
HM
OT
OR
VIE
W-A
A
(ID F
AB
, CH
IMN
EY
& F
D F
AN
AR
E N
OT
SH
OW
N IN
TH
IS V
IEW
)
H
FD
FA
N, A
PH
, MD
C, ID
FA
N &
CH
IMN
EY
AR
E N
OT
SH
OW
N IN
TH
IS V
IEW
)
EL
EV
AT
ION
SY
ST
EM
AS
H C
ON
VE
YIN
G
FE
ED
ER
TO
P H
EA
DE
R
FU
EL
ST
OR
AG
E
SIL
O 6
CU
.M
TO
P F
RA
ME
BU
CK
ET
EL
EV
AT
OR
L
W
RO
OM
CO
NT
RO
L
ST
OR
AG
E T
AN
K
CO
NT
RO
LP
AN
EL
PL
AN
AS
H S
ILO
2.5
CU
.MC
LIE
NT
SC
OP
E
ID F
AN
WIT
HM
OT
OR
CH
IMN
EY
(SP
AC
E F
OR
TU
BE
CL
EA
NIN
G)
BO
ILE
R
MO
TO
RF
D F
AN
WIT
H
7
36
Descrip
tion
Unit
E
fficiency
Cap
acity (Actual O
utput)
kg/hr
40
00
6
00
0
800
0
100
00
120
00
14
00
0
160
00
%
Desig
n pressure (SV
LOP
) kg
/cm2g
10.54
/ 17.5
E
fficiency
A
s per B
S 8
45 P
art 1 NC
V B
asis
Fuels
Co
al / Bio
mass / P
alm W
aste / MSW
Fuel consum
ptio
n
W
ith Eco
nom
iser
C
om
bustio
n Technolo
gy
Flud
ised B
ed C
om
bustio
n
Wo
od
Chip
s (290
0 kC
al/kG G
CV
) kg
/hr 8
56
1284
1712
2140
256
8
299
6
3424
78
Indo
nesian Co
al (580
0 kC
al/kG G
CV
) kg
/hr 4
43
66
5 8
87
1108
1330
1552
1773 84
Rice H
usk (3200
kCal/kG
GC
V)
kg/hr
856
128
4
1712 214
0
2568
29
96
34
24
82C
onnected
Electrical Lo
ad
Wo
od
Chip
s kW
38
56
72
90
113
136
156
Indo
nesian Co
al kW
38
56
72
90
113
136
156
Rice H
usk kW
38
56
72
90
113
136
156
Co
mb
ustion Techno
log
y
Traveling G
rateW
oo
d C
hips
kg/hr
876
1314
1753
2191
2629
30
67
3505
76Ind
onesian C
oal
kg/hr
454
6
81
90
8
1134
1361
1588
18
15 82
Rice H
usk kg
/hr 8
76
1314
1753 219
1 26
29
306
7 350
5 80
Co
nnected E
lectrical Load
W
oo
d C
hips
kW
34
43
62
68
9
5 10
5 131
Indo
nesian Co
al kW
34
4
3 6
2 6
8
95
105
131 R
ice Husk
kW
34
43
62
68
9
5 10
5 131
Co
mb
ustion Techno
log
y
Recip
rocating
Grate
Wo
od
Chip
s kg
/hr 8
66
129
9
1732 216
5 259
8
3031
346
4
78
Indo
nesian Co
al kg
/hr 4
49
6
73 8
97
1121 134
6
1570
1794
83
Rice H
usk kg
/hr 8
66
129
9
1732 216
5 259
8
3031
346
4
81C
onnected
Electrical Lo
ad
Wo
od
Chip
s kW
36
4
6
65
72 9
8
110
135 Ind
onesian C
oal
kW
36
46
6
5 72
98
110
135
Rice H
usk kW
36
4
6
65
72 9
8
110
135 C
himney To
p D
iameter
mm
6
00
70
0
80
0
90
0
100
0
1100
1150
D
ry Weig
ht Ap
prx
tonne
36
42
52 6
2 8
1 8
8
90
F
loo
ded
weig
ht Ap
prx
tonne
41
48
6
2 72
96
10
4
109
Dim
ensions w
ith Fuel H
andling
arrangem
ent L
X W
X H
mtrs
20 X
10 X
10
22 X 12 X
13 24
X 14
X 15
25 X 14
X 15
26 X
15 X 16
27 X
16 X
16
29 X
18 X
18
No
menclature
EF
-XX
-YY
-SF
XX
- ton/hr o
f steam
Y
Y - D
esign P
ressure
SF
- So
lid fuel
E
xamp
le: 8 t/hr b
oiler o
n Wo
od
Chip
s
EF
-08
-10.5-W
oo
d C
hips
** A
ctual Effi
ciency value dep
ends o
n locatio
n & q
uality of fuels
** NC
V o
f fuels dep
ends o
n the actual fuel analysis during
measurem
ent of E
fficiency d
uring fi
nal test run of B
oiler
** Fuel H
andling
includes B
ucket or B
elt Co
nveyor to
bring
the fuel upto
Fuel F
eeding
Ho
pp
er ** C
hinmey (S
tack) height d
epend
s upo
n local p
ollutio
n norm
s. Generally it sho
uld b
e 24 m
trs
SO
LID FU
EL FIR
ED
BO
ILER
SP
EC
IFICATIO
NS
We
ad
d va
lue
to yo
ur n
ee
ds....
PRINCIPLE OF OPERATION FOR SOLID FUEL FIRED BOILERS
Solid Fuel fired boilers generate heat by combustion of fuels like Coal, Rice Husk, Wood Pellets, Wood Chips, Briquettes etc. Combustion chamber is designed based on type of fuel & moisture present.
Traveling Grate: Mainly designed for Biomass fuels like Palm kernel shell, Rice Husk, Wood Chips, Bagasse and other fuels like Coal.
The fuel is fired from opposite side of the grate which allows volatile matter to burn in air while spreading through the stoker. This provides immediate heat to support the fluctuating demands in process industries
Fluidized Bed: Mainly designed for fuels like coal where the moisture & ash percentage is higher.
Fuel is fed into the bed from bottom known as Under bed feeding. It enables proper mixing of coal with the hot sand at 900 Deg C. This method is used when the coal is low grade & uneven in size. Over bed feeding is also possible where the coal is of good quality & well sized.
Rice Husk, PKS, Wood Chips are also combustible in this technology.
Reciprocating Grate: Mainly designed for fuels like Palm EFB Pellets, Palm Fiber where there is a high moisture content.
Three zones of combustion allows the complete burning of fuels. The fuel tumbles down due to reciprocating action of the grate which allows fuel to burn completely.
We add value to your needs....
OUR TEAM OF ENGINEERS SHALL SUGGEST THE BEST COMBUSTION TECHNOLOGY BASED ON THE FUELS TO BE BURNT
3
54
Desig
n Co
de: IN
DIA
N B
OILE
R R
EG
UA
LTION
(IBR
) / ASM
ED
escriptio
n U
nit
C
apacity (A
ctual Outp
ut) kg/hr
100
0
1500
20
00
30
00
4
00
0
500
0
60
00
80
00
10
00
0
1200
0
140
00
16
00
0
1800
0
200
00
250
00
Desig
n pressure (SV
LOP
) kg/cm
2g
10.54
/ 17.5
Eff
ciency
As p
er BS
84
5 Part 1 N
CV
Basis
Furnace O
il / LDO
%
92
Natural G
as / LPG
%
94
Fuel
Furnace O
il / LDO
/ Natural G
as / LPG
Fuel consum
ptio
n
W
ith Eco
nom
iser
F
urnace Oil
kg/hr
61
91
122 18
2 24
3 30
4
365
48
7 6
08
730
8
52 9
73 10
95
1216
1521LD
O
kg/hr
58
86
115
173 230
28
8
345
46
0
575 6
91
80
6
921
1036
1151
1439
Natural G
as N
m3/hr
69
10
4
138
207
276
345
414
552
69
1 8
29
96
7 110
5 124
3 138
1 1726
LPG
N
m3/hr
22 34
4
5 6
7 8
9
112 134
179
224
26
8
313 358
4
02
44
7 559
Co
nnected E
lectrical Load
Furnace O
il / LDO
* kW
16
/17 16
/17 18
/19
26/28
.5 28
/30
37/40
4
0/4
4
50/59
58
/67
71/75 78
.5/86
8
6/9
3.5 9
3.5/101
101/10
8.5
120/127
Natural G
as / LPG
* kW
6
/7 7/8
11/12
15/17 19
/21 19
.5/23 23/26
.5 28
/37.5 4
1.5/45.5
49
/53 4
9/56
.5 56
.5/64
6
4/71.5
71.5/79
90
/98
Overall D
imensio
ns
FO o
r LDO
A
1 (Length)*
mm
74
00
79
00
8
200
8
700
9
500
10
300
1110
0
1200
0
13700
14
00
0
15100
159
00
16
750
1760
0
196
00
B1 (W
idth)*
mm
350
0
360
0
3550
3850
4
150
44
50
470
0
500
0
5300
550
0
580
0
610
0
6350
6
60
0
7300
C1 (H
eight)*
mm
36
00
36
00
36
00
38
00
4
00
0
4250
4
700
4
80
0
5050
530
0
5850
6
250
66
50
7050
8
100
LPG
/ NG
A
(Length)
mm
4
221 4
721 4
971
5221 58
22 6
322 6
89
4
7769
8
419
8
88
6
950
9
100
02
104
95
109
88
12221
B (W
idth)
mm
29
37 30
27 30
27 316
0
3415
3415
3560
3713
388
5 39
95
470
8
504
9
5390
5731
658
4C
(Heig
ht) m
m
3273 3353
3353 34
73 3773
3773 39
23 4
023
4223
4323
4573
48
23 50
73 5323
594
8
C
himney To
p D
iameter
mm
350
4
00
4
50
450
50
0
60
0
650
70
0
80
0
850
9
50
100
0
1050
110
0
1250
D
ry Weig
ht* to
nne 5/6
6
/7 6
.5/8
7/9.5
10/13
11/14
13/16
16/20
19
/23 21.5/27
27/34
32/41
37/48
4
2/55 55/8
3F
loo
ded
weig
ht* to
nne 9
/10
12/13 12.5/14
14
/16.2
20/23
21.8/25
26.5/29
32/35.5
39/43
44
/49
.5 55.2/6
2.2 6
7/76
80
/91
94
/107
133/151N
CV
F
urnace Oil
kcal/kg
96
50
LDO
kcal/kg
10
200
N
atural Gas
kcal/Nm
3 8
500
LP
G
kcal/Nm
3 2570
0
Burners
Make
Weishaup
t / Baltur / E
cofl
ame / A
s per client req
uirement
Mo
dels
No
menclature
EF
-XX
-YY
-OG
F
XX
- ton/hr o
f steam
YY
- Desig
n Pressure
OG
F - O
il & G
as fired
bo
ilers
E
xamp
le : 1t/hr bo
iler on N
G F
uel
E
F-0
1-10.54
-NG
OIL &
GA
S FIR
ED
BO
ILER
SP
EC
IFICATIO
NS
* Specifications may vary depending on the site location
We
ad
d va
lue
to yo
ur n
ee
ds....
4
General A
rrangement D
rawing W
e a
dd
valu
e to
you
r ne
ed
s....
BU
RN
ER
RE
FR
AC
TO
RY
DO
OR
CO
NT
RO
L P
AN
EL
ST
EA
M G
EN
ER
AT
OR
EL
EV
AT
ION
SM
OK
E C
HA
MB
ER
EC
ON
OM
ISE
R
L
W
(SP
AC
E F
OR
TU
BE
CL
EA
NIN
G/R
EM
OV
AL
)
PL
AN
VIE
W
WIT
HO
UT
EC
OM
OM
ISE
R
H
FW
to E
CO
FE
ED
WA
TE
RIN
LE
T
FE
ED
WA
TE
Rto
BO
ILE
R
EC
O.O
UT
LE
T D
UC
T
EC
ON
OM
ISE
R
OU
TL
ET
DU
CT
EC
O.S
UP
P.
ST
RU
CT
UR
E
AC
CE
SS
DO
OR
CO
LD
AIR
FO
R S
IGH
T
GL
AS
S C
OO
LIN
G
SIG
HT
GL
AS
S
R.H
SID
E V
IEW
5