Title: Sugar Automation
1AVANT-GARDE
ENGINEERS AND CONSULTANTS (P) LTD.
(ISO 90012000 ORGANISATION)
NO. 68A, PORUR KUNDRATHUR HIGH ROAD, PORUR,
CHENNAI 600 116. INDIA.
TEL 91-44-24827843, 24828532, 24828717, 18, 19,
20 FAX 91-44-24828531 E-Mail
avantgarde_at_vsnl.com Web Site
http//www.avantgarde-india.com
2SUGAR PLANT AUTOMATION
ITS BENIFITS
BY
AGEC
3?
WHY THERE IS NEED FOR
SUGAR PLANT AUTOMATION ?
AGEC
4REASONS
THERE ARE MANY BENEFITS WHICH CAN BE QUALIFIED
AFTER AUTOMATION OF SUGAR PLANT.
AGEC
5There will be considerable reduction in Steam
cane, resulting in savings of Bagasse / Increase
in export power in cogeneration power plant by
the way of controlling steam to evaporators /
pans.
AGEC
6IMPROVEMENT IN RBHR AS A RESULT OF REDUCTION IN
LOSS OF SUCROSE,
- Due to..
- Auto Lime Feeding
- Optimum Juice Temperature
- Regulating Vacuum for cake formation
AGEC
7- Regulating Juice level in Evaporator
- Regulating steam / Vapour in Evaporator
- for uniform brix
- Regulating fan feed according to
- conductivity
- Maintaining uniform / optimum melt brix
- and condition of molasses.
8There will be substantial reduction in man power
resulting in better and effective utilization of
man power.
AGEC
9There are many benefits resulting from Sugar
Plant Automation which could not be quantified in
terms of savings, but would help in improvement
of plant performance.
AGEC
10Reduced mill extraction would improve due to fine
and continuos control of mill / carrier load /
speed
AGEC
11Crushing rate would become more uniform
continuous resulting in smooth operation of
plants.
AGEC
12This would also result in reduction of down time
of mills other crushing equipments eventually
reduction of losses / man power.
AGEC
13The Distributed Control System is Fed with
enormous amount of data regarding plant
operation. The data stored can be retrieved and
used for analysis regarding equipment / plant
performance.
AGEC
14Automation of Sugar Plant will open flood gates
to acquire latest technologies /
trends Examples 1. Automatic Generation of
Reports 2. Remote Monitoring of Plant
Performance .
AGEC
15The entire plant can be Automated OR Plant can
be Automated Section Wise
AGEC
16DIFFERENCE SECTIONS FOR AUTOMATION
- Mills Preparatory Devices
- Juice Section
- Liming Sulphitation
- Clarification / Filter
AGEC
17- Evaporators
- Pans
- Crystallisers pugmills Centrifugal
- Molasses Tanks
18IMBIBITION CONTROL
Proportional control of Imbibition water flow
rate with respect to crushing rate
AGEC
19MILL CONTROL SPEED CONTROL The First Mill Speed
Control comes with respect to crushing rate and
Donolly Chute level of Second Mill
AGEC
20CANE CARRIER SPEED CONTROL This Control comes
with respect to rake carrier speed and all cane
preparatory devices
AGEC
21EVAPORATOR JUICE LEVEL CONTROL The Optimum
Calendria Level Maintains with respect to juice
brix
AGEC
22EVAPORATOR CALELDRIA PRESSURE CONTROL This Steam
Pressure Control comes with respect to Caleldria
Pressure and juice brix
AGEC
23EVAPORATOR BRIX CONTROL
The Evaporator body brix maintains with respect
to brix of the syrup in the same body
AGEC
24SECOND BODY VAPOUR CONTROL Vapour pressure in
second body maintains by opening the steam valve
to pan floor and juice heater
AGEC
25MOLASSES CONDITIONER TEMPERATURE CONTROL Steam
inlet to Molasses Conditioner maintains with
respect to molasses temperature
AGEC
AGEC
26MOLASSES CONDITIONER BRIX CONTROL Hot water flow
to Molasses Conditioner is controlled with
respect to molasses brix
AGEC
27MELTER TEMPERATURE CONTROL Steam flow to melter
is controlled with respect to melt temperature
AGEC
28MELTER BRIX CONTROL Hot water flow to melter is
controlled with respect to melt brix
AGEC
29PUG MILL LEVEL CONTROL Pug mill level maintains
by controlling the discharge valve of
crystalisers
AGEC
30CENTRIFUGAL MACHINES FEED CONTROL Pug mill
discharge valve is controlled with respect to
load of continues centrifugal machines
AGEC
31CONTINUOS PAN VAPOUR CONTROL Vapour inlet to the
pan is controlled with respect to massecuite
brix in the last compartment
AGEC
32CONTINUOS PAN LEVEL CONTROL Massecuite outlet is
controlled with respect to massecuite level in
the last compartment
AGEC
33CONTINUOS PAN MOLASSES CONTROL Massecuite flow to
the second compartment controlled with respect to
brix of massecuite in second and third compartment
AGEC
34CONTINUOS PAN HOT WATER CONTROL Hot water inlet
to the ninth compartment is controlled with
respect to massecuite brix in the last
compartment
AGEC
35BATCH PAN STEAM CONTROL Steam inlet to the pan is
controlled with respect to Vapour pressure
buildup in the pan
AGEC
36BATCH PAN WATER CONTROL Water inlet to the pan is
controlled with respect to massecuite brix
AGEC
37BATCH PAN FEED CONTROL Syrup / Massecuite inlet
to the pan is controlled with respect to
massecuite brix
AGEC
38TRANSIENT HEATER HOT WATER CONTROL Hot water flow
is controlled with respect to temperature
transient heater
AGEC
39VACUUM FILTER DRUM SPEED CONTROL Drum speed
control comes with respect vacuum filter saucer
level
AGEC
40VACUUM FILTER HIGH VACUUM PRESSURE This control
comes with respect to vacuum filter high vacuum
AGEC
41VACUUM FILTER LOW VACUUM PRESSURE This control
comes with respect to vacuum filter low vacuum
AGEC
42VACUUM FILTER TROUGH LEVELCONTROL This control
comes with respect to vacuum filter trough level
AGEC
43LIME FLOW CONTROL Lime flow control comes with
respect to crushing rate and juice pH
AGEC
44JUICE SULPHITOR SO2 CONTROL Sulphated juice pH
maintains by controlling the flow of so2 in
terms of controlling the flow sulphur to the
furnace.
AGEC
45SYRUP SULPHITOR SO2 CONTROL Sulphated syrup pH
maintains by controlling the flow of so2
AGEC