Automatic Candle Type Filter for Sugar and Syrup Industry

  • 0.5-800μm
  • candle filter cartridge
  • S.S 304, 316L, Carbon steel
  • 1 Year
  • 1-60m²
  • 1-200°C
  • Description
  • Video

Overview

The Automatic Candle Filter is a closed, fully automatic pressure filtration device. Its interior consists of multiple “candle filter elements,” making it suitable for high-precision, continuous or semi-continuous liquid clarification filtration.
In the sugar and syrup industry, it is primarily used to : Remove suspended impurities, activated carbon, pigment particles, and fine solids, thereby enhancing the clarity and purity of sugar solutions.

Key Advantages

  • Direct filtration and pre-coating filtration can be selected according to particle size.
  • Multi-level filtration accuracy up to 0.5 microns.
  • Competent for high precision, high solids content (limited to 5%) and high viscosity.

Typical Application Scenarios

  • Activated carbon decoloration for granulated sugar and glucose
  • Filtration of sucrose, fructose syrup, high fructose syrup, glucose syrup, beet sugar, Maple syrup, honey, etc
  • Cane sugar mills and raw sugar refineries filtration.
  • Raw sugar re-melt.
  • Thin juice filtration and polishing.

Our Case

Specification

Model Cartridge QTY Cartridge Size(mm) Filtering Area(m2) Capacity(t/h) Housing Volume(L) Inlet Cake Discharging Outlet Total Height(mm)
DZZS-1 7 90*500 1 2.2 140 DN25 DN150 1902
DZZS-1.5 10 90*500 1.5 3.3 180 DN25 DN200 1928
DZZS-2 7 90*1000 2 4.4 220 DN32 DN150 2402
DZZS-3 10 90*1000 3 6.6 280 DN40 DN200 2428
DZZS-4 14 90*1000 4 8.8 400 DN40 DN200 2502
DZZS-6 19 90*1000 6 13.2 560 DN50 DN250 2578
DZZS-8 24 90*1000 8 18 740 DN65 DN250 2644
DZZS-12 40 90*1000 12 26 1200 DN65 DN300 2854
DZZS-18 64 90*1000 18 40 1800 DN80 DN400 2904
DZZS-30 106 90*1000 30 66 3000 DN100 DN500 3440
DZZS-40 140 90*1000 40 88 3815 DN150 DN500 3560
DZZS-60 190 90*1000 60 132 5700 DN150 DN500 3700

Selection Notes (Limitations)

  • Equipment investment costs are relatively high. Automation systems, pressure vessel structures, and control systems result in higher initial investment compared to traditional plate-and-frame filters.
  • Operational management demands are relatively high. Proper control of precoat aid application and operating parameters is required; otherwise, filtration efficiency will be compromised.

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