Tower Press Filter (TPF)

Tower Press Filter (TPF)

Intended use: Filtration (dewatering) of highly dispersed suspensions (pulps):

  • Copper flotation concentrates
  • Cobalt
  • Nickel
  • Lead
  • Tin
  • Magnetite
  • Apatite
  • Talc, etc.

Industries:

  • Mining
  • Metallurgical and mining
  • Chemical and petrochemical
  • Coal mining

Applications:

The filters are used for filtering a wide range of suspension classes and are suitable for separation of suspensions with small solids concentrations and high-temperature suspensions that can't be cooled due to crystal crashing out.

Main advantages:

  • Filtration, washing and air purging processes in one unit in automatic mode according to pre-programmed algorithms

  • Minimum time of auxiliary operations (filter cloth regeneration and dewatered sludge discharge are combined in one operation)

  • Filtration of suspensions in a wide range of solid particle sizes: from fine (less than 40μm) to several millimeters and with various solid to liquid ratios

  • Due to the horizontal position of filter plates, the filtration process is optimized as the direction of gravity and filtrate movement coincide

  • Uniform chamber filling

  • Cake thickness and, respectively, sludge moisture content adjustability in a wide range 

  • Cake washing ability, if necessary 

  • Guaranteed full cake discharge 

  • Flexible selection of construction materials - from carbon steel to stainless steel - depending on the operational requirements


General principle of operation:

Filtration (separation of suspensions into two phases – liquid and solid). The press filter is a batch process plant with a key component being a frame-mounted filter plate block.



Efficiency:

Capacity, kg/m2*h

Solids content, %

Moisture content, %

Material

350


9.5-10.5

Cu-Ni conc.

830-850


7.5

Zn conc.

90


20

Zn leach residue

72


20

ZnO leach residue

100


17-21

Zn leach residue

230


12.5

Сu conc.

320


14

Talc

90


15-20

Scrubber slurries 

Pb Zn sulfides 

200

150÷300 g/l

19÷22

4A zeolite

250÷280

50%

7÷8

sulfur concentrate

120

50%

30

molten sulfur

35

50%

15÷20

molten lead compounds

320

600 g/l

8÷9

copper smelting slags

100÷150

5%÷10%

28÷35

calcium sulfate in wastewater

200÷250

40%

14÷18

gold-bearing rock waste

23÷69

15%÷20%

29÷32

super fine aluminum hydroxide

360

50%÷65%

9.78

copper-nickel concentrates

300÷400

45%÷50%

7.6

copper concentrates

200

45%÷50%

8

nickel concentrates

122÷150

10%

20÷25

molten tantalum-niobium

300

10%

11.3

K-acids

280

30%÷35%

16÷17

coal sludge

300

40%

≤9

iron slags

220

20%÷30%

12÷18

gold-bearing rock flotation waste

160÷180

30%

32

modified starch

90


12

mannitol

72

57%

20

zinc oxide 

choose powder

257

50,50%

18÷20

leaching of zinc residues

65÷75

50%

30÷40

arsenic sulfide

200÷220

30%

32

starch


Main filtration process stages:

1. Filtration

Process pulp is pumped simultaneously into all filter chambers. Cake starts to accumulate, while filtrate is displaced by the next portion of pulp entering the chamber. As the cake accumulates, the pump pressure increases, and filtrate is squeezed through the cloth until the required cake thickness is reached.


2. Pressing

Water or high-pressure air automatically fills the above-membrane space at the top of each chamber, reducing the chamber volume and compressing the cake to remove additional filtrate. This cake filtration process and a tightly woven filter cloth provide extra pure filtrate, while high pressure maximizes the filtration efficiency. Membrane pressing results in a homogeneous dewatered cake of uniform thickness with minimum residual moisture, which makes its washing with water and blowing with air easier.


3. Cake washing (optional)

Wash fluid is fed through the suspension feed pipe for solid cake washing and removal of dissolved substances.


4. Re-pressing (optional)

Repetitive pressing evenly pushes the wash fluid through the cake layer and removes it.


5. Air blowing

Compressed air is blown through the cake for final dewatering. The moisture content is reduced to a minimum. This process can be fine-tuned by changing the blowing pressure and duration.


6. Cake discharge and cloth washing

After plate block opening, the dewatered cake is removed from each chamber by a movable filter cloth. A built-in high-pressure washing unit sprays fluid on both sides of the cloth for minimum clogging and uniform filtration.

Name / Description

 Total filtering area, m2  

Number of chambers, ea.

TPF-100 

 100

14

TPF-85 

85

12

TPF-70 

70

10

TPF-55 

55

8



Marking:

TPF-100 

Tower Press Filter 100 – filtering area, m2

Tower Press Filter


Optional equipment: (to be supplemented)

1. Sensors:

Load cells

Cake weight

Pressure sensors

Feed, pressing, cake wash, cloth wash, hydraulic system

Position sensors

Hydraulic cylinder shift, cloth position, cloth drift

Flowmeters

Feed, air, water, filtrate

Turbidimeter

Filtrate turbidity

Temperature sensors

Liquids and air

Density meter

Cake height adjustment


2. Air and filtrate separation tank

3. Pulp conditioning tank with agitator

4. Pumping equipment

5. Compressor station



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