The filter body is St-37 or stainless-steel optionalityThe filtering in pressured linesHigh performance during the back washingExtensive Filtering SurfaceEasy-to assembly and fitler components, not required to change100% back washing performanceThe back washing time for 50-30 sec.Working opportunity, not required additional energyThe minimum head and water loss
Body Material: S195T / SS 316L / SS 304 L
Screen Material: SS 304L, PA6GFR30
Maximum Working Pressure: 10 Bar (145 PSI)
Minimum Working Pressure: 1 Bar (15 PSI)
Maximum Working Temperature : 60 °C (140 °F)
Back Flush Operation Criteria: Time and / or Pressure Differential
Back Flush Controlling Unit : Electronic (AC) Control
Filtration Degree: 20-2000 micron (µ)
Painting Method: Electrostratic Powder Coating
Painting Material: Epoxy Polyester
|CODE||INLET/OUTLET||A||B||L1||L||D||F||DRAINAGE FLOW||FLOW||FILTER SURFACE AREA||NOZZLE||SIEVE||WEIGHT|
|RF104 CRF104||4||100||500||287||920||1685||10||2||12||120||2634||2||4||85 78|
|RF104S CRF104S||4||100||600||287||1120||1885||10||2||18||140||3951||3||6||94 86|
|RF105 CRF105||5||125||600||287||1120||1885||10||2||18||150||3951||3||6||96 88|
|RF105S CRF105S||5||125||900||287||1430||2195||10||2||24||160||5268||4||8||103 95|
|RF106 CRF106||6||150||900||287||1430||2195||10||2||24||180||5268||4||8||106 98|
|RF126S CRF126S||6||150||1100||312||1822||2585||12||2||36||220||7902||6||12||135 117|
|RF128 CRF128||8||200||1100||312||1822||2585||12||2||36||320||7902||6||12||138 120|
|RF1210 CRF1210||10||250||1100||312||1822||2585||12||2||36||400||7902||6||12||149 130|
Water, entered from input collector, puts partcules, contained by itself, in rough screen (3) passes top art which include multiplex filter (4). It is protected with a rough material with screen over of multiplex screen. The thin filter goes to output collector side (2). Particles, collected on multiplex screen, constitute a pollution layer over of the filter and a pressure difference in the outsite collector. This pressure difference open a back flushing unit washing decharge valve (9) in the value, designed previously (12) and a powerful back flushing flow consists from decharge pipeto atmosphere (10). This flow cleans the particle layyer, collected on filter by creating a vacuum from holes over of nozzle (6).
The dirty water, absorbed on multiplex filter, creates a volution by passing from water cleaning nozzle pipe (7) and hydraulic turbine (8). The pressure loss, consisted of turbine container (5) and plunger dreinage (9) constitutes an axial movement. The spiral headway, constituted by this axial and volution together, obtains the absorbing whole filter surface by vacuum nozzles.
When this process is done, the cleaning collector makes a second back flushing with warns with its warning switches and turns its first position. Transaction is completed.
During the back washing, the filtration process contiunes and after the back washing process, the filter stands by until next pressure difference signal.