CERAFILTEC_Logo_white
CONTACT USCONTACT

CERAMIC SOFTENING FILTRATION
FOR BEVERAGE PROCESSING

REFERENCE FACT SHEET

PROJECT DESCRIPTION

  • Filtered water capacity 4,800 m³/d:
    1,680 m³/d (phase 1); additional 3,120 m³/d (phase 2)
  • Brownfield EPC
  • Modification of pre-treatment process steps, replacement of pressurized polymeric ultrafiltration
  • Location: South Africa
  • In operation since 01/2020

PROCESS CHAIN

  • Blended feed water source from municipality and borehole 
  • Lime dosage for precipitation of calcium and magnesium for hardness reduction (lime softening)
  • No settling of precipitants – direct transfer to filtration tanks
  • Dead-end submerged ceramic flat sheet membrane filtration
  • Activated carbon filters for dechlorination
  • UV system 

PROCESS FLOW DIAGRAM

PERFORMANCE DATA

The feed water is a blend of municipal and borehole water. Both water streams have different properties. The overall blending ratio is dependent on water availability and quality. Sudden and strong peak events have led to the damage of the previously installed polymeric membrane system. 

CERAFILTEC’s softening filtration process enables operation even with high varying water properties. A small amount of lime is currently being dosed to reach a pH of about 9.6 to reduce calcium hardness only. During peak events, lime is overdosed to reach a pH of about 10.5 to additionally reduce magnesium hardness. In this case, the pH is subsequently adjusted to about 9.6 prior to the ceramic filtration to ensure stable long-term operation. 

Regardless of the total hardness level and lime dosing requirements, all precipitants are directly transferred to the ceramic flat sheet membrane without settling step in between.

PARAMETER
UNIT
FEED WATER
FILTERED WATER
T.H.
ppm
80 (331*)
26
Sulphate
ppm
98 (210*)
82
Silica
ppm
41 (80*)
36
TDS
ppm
365 (421*)
290
TSS
ppm
3 (301**)
< 1 (nil)
Turbidity
NTU
0.67 (49**)
0.17
pH
7.6 (9.6**)
9.6
* feed water max values during peak events; ** after lime dosage (inside filtration tank)
PARAMETER
UNIT
VALUE
No. of trains
9
Max. flow per train
m³/hr
36.2
Max. flux rate
LMH
251
Filtration time
hrs
4 x 3.93
Backwash time
sec
4 x 70
Recovery rate
%
96.1
Power consumption
kWhr/m³
0.02

PLANT PICTURES

Lime mixing
and
precipitation
tanks

Tower
installation

Tower
installation

Tower
installation

Air-scouring
piping

3 installed
towers

Completed
header piping

Systems
engineering

Systems
engineering

Completed
phase 2

Ready for a Quote?

Contact us for a ceramic membrane design or for a commercial proposal.
CONTACT US
chevron-up
linkedin facebook pinterest youtube rss twitter instagram facebook-blank rss-blank linkedin-blank pinterest youtube twitter instagram