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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 :

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Presentation on theme: "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 :"— Presentation transcript:

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2 NO. 68A, PORUR KUNDRATHUR HIGH ROAD, PORUR, CHENNAI – INDIA. TEL: , , , 18, 19, 20 FAX: Web Site :

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5 THERE ARE MANY BENEFITS WHICH CAN BE QUALIFIED AFTER AUTOMATION OF SUGAR PLANT. REASONS

6 There 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.

7 Due to..  Auto Lime Feeding  Optimum Juice Temperature 3. Regulating Vacuum for cake formation IMPROVEMENT IN RBHR AS A RESULT OF REDUCTION IN LOSS OF SUCROSE,

8  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.

9 There will be substantial reduction in man power resulting in better and effective utilization of man power.

10 There 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.

11 Reduced mill extraction would improve due to fine and continuos control of mill / carrier load / speed

12 Crushing rate would become more uniform & continuous resulting in smooth operation of plants.

13 This would also result in reduction of down time of mills & other crushing equipments & eventually reduction of losses / man power.

14 The 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.

15 Automation of Sugar Plant will open flood gates to acquire latest technologies / trends Examples 1. Automatic Generation of Reports 2. Remote Monitoring of Plant Performance.

16 The entire plant can be Automated OR Plant can be Automated Section Wise

17  Mills & Preparatory Devices  Juice Section  Liming & Sulphitation  Clarification / Filter DIFFERENCE SECTIONS FOR AUTOMATION

18 K Evaporators K Pans K Crystallisers pugmills & Centrifugal K Molasses Tanks

19 Proportional control of Imbibition water flow rate with respect to crushing rate IMBIBITION CONTROL

20 MILL CONTROL SPEED CONTROL The First Mill Speed Control comes with respect to crushing rate and Donolly Chute level of Second Mill

21 CANE CARRIER SPEED CONTROL This Control comes with respect to rake carrier speed and all cane preparatory devices

22 EVAPORATOR JUICE LEVEL CONTROL The Optimum Calendria Level Maintains with respect to juice brix

23 EVAPORATOR CALELDRIA PRESSURE CONTROL This Steam Pressure Control comes with respect to Caleldria Pressure and juice brix

24 The Evaporator body brix maintains with respect to brix of the syrup in the same body EVAPORATOR BRIX CONTROL

25 SECOND BODY VAPOUR CONTROL Vapour pressure in second body maintains by opening the steam valve to pan floor and juice heater

26 MOLASSES CONDITIONER TEMPERATURE CONTROL Steam inlet to Molasses Conditioner maintains with respect to molasses temperature

27 MOLASSES CONDITIONER BRIX CONTROL Hot water flow to Molasses Conditioner is controlled with respect to molasses brix

28 MELTER TEMPERATURE CONTROL Steam flow to melter is controlled with respect to melt temperature

29 MELTER BRIX CONTROL Hot water flow to melter is controlled with respect to melt brix

30 PUG MILL LEVEL CONTROL Pug mill level maintains by controlling the discharge valve of crystalisers

31 CENTRIFUGAL MACHINES FEED CONTROL Pug mill discharge valve is controlled with respect to load of continues centrifugal machines

32 CONTINUOS PAN VAPOUR CONTROL Vapour inlet to the pan is controlled with respect to massecuite brix in the last compartment

33 CONTINUOS PAN LEVEL CONTROL Massecuite outlet is controlled with respect to massecuite level in the last compartment

34 CONTINUOS PAN MOLASSES CONTROL Massecuite flow to the second compartment controlled with respect to brix of massecuite in second and third compartment

35 CONTINUOS PAN HOT WATER CONTROL Hot water inlet to the ninth compartment is controlled with respect to massecuite brix in the last compartment

36 BATCH PAN STEAM CONTROL Steam inlet to the pan is controlled with respect to Vapour pressure buildup in the pan

37 BATCH PAN WATER CONTROL Water inlet to the pan is controlled with respect to massecuite brix

38 BATCH PAN FEED CONTROL Syrup / Massecuite inlet to the pan is controlled with respect to massecuite brix

39 TRANSIENT HEATER HOT WATER CONTROL Hot water flow is controlled with respect to temperature transient heater

40 VACUUM FILTER DRUM SPEED CONTROL Drum speed control comes with respect vacuum filter saucer level

41 VACUUM FILTER HIGH VACUUM PRESSURE This control comes with respect to vacuum filter high vacuum

42 VACUUM FILTER LOW VACUUM PRESSURE This control comes with respect to vacuum filter low vacuum

43 VACUUM FILTER TROUGH LEVELCONTROL This control comes with respect to vacuum filter trough level

44 LIME FLOW CONTROL Lime flow control comes with respect to crushing rate and juice pH

45 JUICE SULPHITOR SO 2 CONTROL Sulphated juice pH maintains by controlling the flow of so 2 in terms of controlling the flow sulphur to the furnace.

46 SYRUP SULPHITOR SO 2 CONTROL Sulphated syrup pH maintains by controlling the flow of so 2


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