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FILTRATIONPILOT TEST WORKSMELTING

Case Study: Filtration of Scrubber Dust

Filter press pilot test work on a smelter’s scrubber dust slurry, turning a problem waste stream into a dry filter cake that is fed back to the furnace for metal recovery.

By Filtaquip Global Published 6 min read DOWNLOAD PDF
Filter cake discharged from the Filtaquip pilot filter press

Background

The Client’s smelter consists of a furnace that produces dust which is very harmful to the environment, so a scrubber is used to capture the dust, which forms a slurry. This slurry is then pumped to a slurry storage facility. However, this handling method creates environmental challenges.

Filtaquip offered a solution to dewater the scrubber slurry into a dry filter cake, which is then returned to the furnace, enabling the valuable metals to be recovered. As these solids have commercial value, the Client’s overall revenue is improved, whilst at the same time significantly reducing environmental impact.

Scrubber dust slurry sample supplied by the client
Figure 1: Sample from Client

Objectives of the test work

  • To assess: filtration behaviour, cake formation time, and final moisture content.
  • Assess optimal operating conditions: chamber depth, membrane squeeze and air-blow.

It was essential to obtain a cake as dry as possible, as it will be fed back to the furnace.

Why a filter press?

  • High capture efficiency of solids: particles are retained by a filter cloth, producing clear filtrate.
  • Low final cake moisture: the use of membrane squeeze plates reduces cake moisture significantly.
  • Water recovery and re-use: filtrate can be recycled back into the process, reducing overall water consumption.
Filtaquip filter press pilot plant
Figure 2: FILTAQUIP Filter Press pilot plant
Filtaquip filter press pilot plant, feed side
FILTAQUIP Filter Press pilot plant, feed side

Filtration test results

The filter press pilot plant test work assessed three different operating configurations by varying the pre-squeeze chamber depth and the dewatering sequence.

Pilot filter press test configurations and resulting cake thickness
TESTCHAMBER DEPTHDEWATERING SEQUENCECAKE
Test 130 mmMembrane squeeze, then air-blow19 mm, well-formed
Test 240 mmSqueeze, then air-blow30 mm, thicker
Test 330 mmModified sequence23 mm

Across all tests, firm, dry-to-the-touch cakes were produced with consistently low final moisture contents with an average of 25% w/w, confirming effective dewatering under all tested conditions, which includes clear filtrate production.

Scrubber dust filter cake on the filter plate
Figure 3: Filter cake on the plate

Before & after filtration

Scrubber dust feed slurry before filtration
Figure 4: Feed slurry
Scrubber dust filter cake after filtration
Figure 5: Filter cake
Clear filtrate from the pilot filter press
Figure 6: Clear filtrate

Conclusions

  • Pilot test work confirmed that a filter press is effective for dewatering the scrubber dust sludge, consistently producing firm, stable cakes with moisture contents of ~25% w/w.
  • Membrane squeezing was the primary driver for moisture reduction, with air-blowing providing additional dewatering benefits.
  • Variations in chamber depth influenced final cake thickness and cycle times.
  • Initial filtrate quality was poor, however, this was easily addressed in the design of a full-scale filter press plant.
  • The results provide a reliable technical basis for the selection and design of a full-scale filter press plant, with membrane plates for clarification and dewatering, as well as materials handling.

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Test your slurry: Christo van Niekerk

+27 (0)73 710 2438