Continuous cooking thermochemically degraded native starch sorts in semi-automated or automated modes. The degrading agent is a strong oxidant, usually ammonium or sodium persulphates. The starch solutions prepared this way are suitable for usage as surface applications in size or film presses
Performance groups: TCC450,TCC1100
Performance range: 450to1100kg/hr
Slurry concentration: 22to28%
Power input: 2.2 to 8 kW
Powder starch is dosed by means of precise worm dosing device into a slurry tank where it is mixed with water and slurry is formed. The slurry concentration depends on a starch sort and use. Starch slurry is continuously pumped by means of a screw pump into a static mixer where saturated steam is injected into slurry. Before the steam inlet, the oxidizing agent is dosed into slurry in an exact ratio to starch.
That is the beginning of the cooking process being underway in a cooking tube following the mixer. The cooking temperature is set by means of control circuit on a preset value depending on the starchsort. The cooking tube is followed by another static mixer bringing diluting/cooling water into the cooked starch solution. The outlet concentration is controlled by means of dilution water quantity. Its through put is controlled by control circuit.
Starch diluted onto a required outlet concentration and cooled down to 60 to 85°C enters the storage tank and it is ready for further use. The process is identical for both cationic and oxidized starch. The oxidant dose controls the cooked starch final
viscosity
The machinery design and safety comply with the EU and EAC industrial standards.
K
Compact– slurry unit installed in the frame together with the cooking part
O
separate– slurry unit installed separately from the cooking part
–
none– – the cooker is controlled by means of an external control system
S
Simatic– the cooker is equipped with a PLC based on Simatic type S7
L
logo– the cooker is equipped with a simple programmable controller
A
automatic– water throughput into the slurry tanks is controlled by an automatic control valve
P
float– water throughput into the slurry tank is controlled by a float valve
F
frequency converter– the slurry pump is controlled by a frequency converter the slurry pump without a performance control
A
automatic– the cooking tube pressure is controlled by an automatic control valve
M
manual– the cooking tube pressure is controlled by a manual valve
A
automatic– the dilution water flow through the cooking tube is controlled by an automatic control valve
M
manual– the dilution water flow through the cooking tube is controlled by a manual valve
P
water for quick flushing is connected to the slurry pump suction side
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flushing cooker enabled by water connected to the slurry tank
A
automatic– – the cooker works with a performance proportional control
–
the cooker works with a constant performance in an on/off mode
N
– a starch hopper installed in the support frame is part of the cooker
–
no hopper, the starch source is a silo
An example diagram of a TCC type cooker with an integrated hopper, with a slurry diluting water throughput controlled by means of an automatic control valve and an automatic control circuit with a control valve. An oxidant preparing and dosing system is included. The cooker is controlled by means of a Simatic based PLC.
The TCC cookers are delivered including SW enabling a fully automated cooker operation in predefined steps – sequences. The sequences enable cooking and flushing automated modes at reproducible values before and after finishing the cooking process, including a precise oxidant dosing control. The cooker can be switched to a manual mode and the operation can be carried out by means of control board installed on the switchboard front door.
During the cooker operation the cooking process conditions like media parameters, functions and statuses of particular cooker key elements and control circuit statuses are monitored; if any parameter deviates from a control range an alarm message is generated and saved in an alarm bank. The system controls the oxidant preparation as well.
The cooker performance is usually controlled depending on the cooked starch storage tank level height either in an on/off mode (the cooker works with a constant performance, starts on the bottom level and stops after reaching the top level) or it works with a variable performance depending on the storage tank level fall speed.
Starch sort: native
Starch origin: potato, corn, wheat, tapioca
Starch source: hopper integrated in the cooker support frame 3 (volume 100 to 400 dm )
Starch packing: paper sacks 25 to 40 kg “Big-Bags” 600 or 1 000 kg road tanker, starch stored in a high-capacity silo
Oxidant dosing: precise dosing pump with performance control and flow measuring
Cooking time: 4 minutes for all starch sorts
Heating medium: saturated steam 4 to 5 bar abs
Water: fresh or treated without mechanical impurities, minimum pressure 3.5 bar
Instrument air: dew point -20°C, pressure 5 bar
Performance change speed: dQ = 5 kg/min or a ramp change
An example of TCC cooker diagram filled from a medium silo, water throughput into the slurry tank controlled by an automatic control valve and an automatic control circuit with an automatic control valve. The system preparing and dosing oxidant is
included as well. The cooker is controlled by a Simatic based PLC.
An example of TCC cooker diagram filled from a large-volume silo, water throughput into the slurry tank controlled by an automatic control valve and an automatic control circuit with an automatic control valve. The system preparing and dosing oxidant is included as well. The slurry part is installed in a separate support frame below the silo output cone and connected to the cooking part by a pipeline. The cooker is controlled by a Simatic based PLC.
Category
UncategorizeLength
4 feetWidth
6 feetHeight
10 feetWeight
580 kgSpace Require
14 sq. feetCompany Presentation
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