With the ever increasing demand for sand and the corresponding increase in demand for water, customers are forced to look into effective ways for water recycling apart from the conventional pond sedimentation techniques. Consistent solids under flow and clear water overflow has enabled modern day thickeners to be a part of seamless mineral processing and aggregate sand washing circuits. The uses of thickeners in a beneficiation process are five fold, they are
Nesans fitch series thickeners consists of the following sub-assemblies
The overflow from a Hydrocyclone or a sand washing equipment is introduced into the inlet of the fitch series thickener where optional dilution is done before the slurry stream is taken into the feed well. The flocculant is added here.
The involute design of the feed-well allows for a laminar flow of the feed slurry so that the flocs are not broken, reducing its efficiency. The dewatering cones attached to the feed-well allows for the even mixing of the feed around the circumference of the feed-well.
Heavier particles formed by the action of flocculating agents enters the transition zone after which they will eventually end up in the compression zone. Water, clear of suspended particles moves upward through the zone of free settling into the clarifier zone.
The weir discharge launder given around the inner edge of the thickener tank at a predetermined height allows the overflowing clear water to exit the thickener.
Solids settled in the bottom cone of the thickener are removed by the movement of the rakes which propels them towards the underflow exit.
Bed Pressure Sensor:
Turbidity sensor :
The quality of the overflow is monitored with a turbidity sensor which will further increase or decrease the loading rate of the flocculating agent.
Flow meter :
The input slurry flow rate is monitored to keep the handling capacity of the thickener under check and to avoid over loading of the thickener. The underflow flow rate is also monitored to keep the mass-balance of the thickener.
Rake torque Sensor :
The Rake arm of the thickener is suspended from above the feedwell of the thickener. Temporary plant shut-downs or power failure will allow free solids to settle and undergo compaction when the thickener is started again. There is a chance the rakes may fail due to overload. In order to avoid a possible scenario, the torque of the rake drive gearbox is monitored closely. Should the torque increases above the pre-determined limit, the entire rake assembly is raised up to avoid failure of the gearbox. Once the torque is restored, the rakes are again lowered back.
Underflow density :
The underflow density is monitored to make sure the compressed solids have reached their required density. The retention time inside the thickener is selected based on the underflow density of the solids.
THICKENER DIAMETER : 6 m
THICKENER HEIGHT : 2 m
UNDERFLOW RATE : 12 TPH
SLURRY LOADING RATE : 72 m³/hr
INPUT % SOLIDS : < 15 %
UNDERFLOW % SOLIDS : 25 – 35 %
TOTAL POWER REQUIRED : 30 kW
THICKENER DIAMETER : 20 ft
THICKENER HEIGHT : 7 ft
UNDERFLOW RATE : 13 STPH
SLURRY LOADING RATE : 2543 ft³/hr
INPUT % SOLIDS : < 15 %
UNDERFLOW % SOLIDS : 25 – 35 %
TOTAL POWER REQUIRED : 40 HP
THICKENER DIAMETER : 10 m
THICKENER HEIGHT : 3 m
UNDERFLOW RATE : 30 TPH
SLURRY LOADING RATE : 180 m³/hr
INPUT % SOLIDS : < 15 %
UNDERFLOW % SOLIDS : 25 – 35 %
TOTAL POWER REQUIRED : 40 kW
THICKENER DIAMETER : 33 ft
THICKENER HEIGHT : 10 ft
UNDERFLOW RATE : 33 STPH
SLURRY LOADING RATE : 6357 ft³/hr
INPUT % SOLIDS : < 15 %
UNDERFLOW % SOLIDS : 25 – 35 %
TOTAL POWER REQUIRED : 54 HP
THICKENER DIAMETER : 12 m
THICKENER HEIGHT : 4 m
UNDERFLOW RATE : 40 TPH
SLURRY LOADING RATE : 250 m³/hr
INPUT % SOLIDS : < 15 %
UNDERFLOW % SOLIDS : 25 – 35 %
TOTAL POWER REQUIRED : 55 kW
THICKENER DIAMETER : 39 ft
THICKENER HEIGHT : 13 ft
UNDERFLOW RATE : 44 STPH
SLURRY LOADING RATE : 8829 ft³/hr
INPUT % SOLIDS : < 15 %
UNDERFLOW % SOLIDS : 25 – 35 %
TOTAL POWER REQUIRED : 74 HP
THICKENER DIAMETER : 15 m
THICKENER HEIGHT : 5 m
UNDERFLOW RATE : 50 TPH
SLURRY LOADING RATE : 300 m³/hr
INPUT % SOLIDS : < 15 %
UNDERFLOW % SOLIDS : 25 – 35 %
TOTAL POWER REQUIRED : 60 kW
THICKENER DIAMETER : 49 ft
THICKENER HEIGHT : 16 ft
UNDERFLOW RATE : 55 STPH
SLURRY LOADING RATE : 10594 ft³/hr
INPUT % SOLIDS : < 15 %
UNDERFLOW % SOLIDS : 25 – 35 %
TOTAL POWER REQUIRED : 80 HP
The most prominent types of thickeners are
1. Conventional thickeners
2. High rate thickeners
3. High density thickeners
4. Deep cone thickeners
The thickener type is selected based on the following factors
1. Feed flow rate
2. Percentage of solids in the feed
3. Underflow density required
4. Underflow and overflow capacity required
5. Space availability
6. Availability of investment and finance options
The size of the thickener can be arrived with the below listed tests. However, more sophisticated tests may be required for deep understanding of the process design parameters.
1. Batch sedimentation test
2. Feed characterisation test
3. floculant / Coagulant test
No, feed dilution is not required at all the times and may vary with application.
The underflow of the thickeners can be taken to a filter press, where they can be further dried and made into cakes. These cakes find a variety of applications from landfills to filler materials
Though both the equipment work on the same principle, a thickener is a device where the underflow solids play an important role. The percentage solids and the density are important in a thickener whereas in a clarifier, the clarity of the water reclaimed and the percentage of suspended solids is of almost importance.
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