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K N O W L E D G E B R I E F
Pumice as a Filtration Media
Pumice is, at its essence,
foamed glass, formed by
the expansion of trapped
gases when molten lava
rapidly cools. When
crushed, pumice still
retains its frothy structure,
making it effective at any
filtration grade.
As a filtration media, pumice is an aggressively-filtering alternative to sand (and other
filtration media). The low specific gravity and high porosity of pumice make it ideal for
irrigation filtration systems and other water treatment processes and provides several
advantages over other filtration media such as sand, expanded clay, and anthracite.
BENEFITS OF PUMICE FORWATERTREATMENT APPLICATIONS INCLUDE:
โ–  Improved filtration rates โ–  Better filtration bed expansion
โ–  Less energy consumption โ–  Larger effective surface area
โ–  Less intensive backwash requirements โ–  Low-cost filter refurbishment
KEY PUMICE CHARACTERISTICS:
โ–  Specific gravity weight of 2.35 g/cc
โ–  Low unit weight: 40 - 50 lbs cubic foot (depending on grade)
โ–  MOHS-scale hardness: 6 (reference: feldspar is a 6 and quartz is a 7)
โ–  Due to its amorphous characteristics, pumice is not considered a health risk to
the workers who handle it.
โ–  Chemically, pumice is primarily Silicon Dioxide (Amorphous Aluminum Silicate),
some Aluminum Oxide, and trace amounts of other oxides.
RESEARCH STUDIES
The information that follows, from a pair of research studies, examines the perfor-
mance of pumice as a granular media to replace or supplement common sand
media in agriculture irrigation filtration media tank systems such as those used to
protect drip and micro-irrigation systems from fine particle and organic solids.
close-up of a 1-inch pumice stone
crushed pumice (G2) at 100x magnification
(208) 766-4777 x111
email: rd@hesspumice.com
www.hesspumice.com
TITLE: The performance of pumice as a filter bed material under rapid
filtration conditions*.
ABSTRACT: Deep bed sand filters are used extensively in drinking water and wastewater
treatment. In this study, sand and pumice were used as a filtration media under rapid
filtration conditions and performance results for both were compared.Turbidity removal
performance and head losses were investigated as functions of filtration rate, bed depth
and particle size. Under the same experimental conditions such as 750 mm bed depth,
7.64m3/m2.h flow rate and, 0.5-1.0 mm grain size, turbidity removal rates for sand and
pumice were found to be 85-90% and 98-99%, respectively. Furthermore, the head loss for
sand and pumice were found to be 460 mm and 215 mm, respectively.The results
obtained have shown that pumice has a high potential for use as a filter bed material.
* Burhanettin Farizoglu, Bulent Keskinler. Published in Filtration and Separation, April 2003
EXCERPTS FROM PUBLISHED
RESEARCH: โ€œDue to the high porosity of
pumice, a filter bed consisting of
pumice retains more suspended solids
than a sand filter bed (head loss 0~ e-4).
Thus, the clogging observed in the
pumice bed is smaller than a sand filter
bed with a similar grain size.The
increase in head loss over time for
pumice progresses more slowly than
with sand media.โ€(FIGURE 9)
HEADLOSS(MM)
TIME (MINUTE) โ–  PUMICE โ–  SAND
FIGURE 9: The comparison of head loss values with time for
the sand and pumice bed (750 mm bed depth, 7.64 ma/m~.h
flow rate & 0.5-1.0 mm grain size).
0 40 80 120 160 200
500
400
300
200
100
CONTINUED: The performance of pumice as a filter bed
material under rapid filtration conditions
โ€œSand is not a porous material and particulate material can only
be retained in the spaces between the grains in the filter bed, so
smaller particulate matter can more easily drain through the
sand media and escape in the effluent water.โ€(FIGURE 10)
โ€œWhen pumice is used as filter bed material it is possible to
distinguish between two levels of porosity, one of the pumice
itself and the other of the filter bed.Thus, while bigger particles
are retained in the filter bed, smaller particles are retained inside
the pores of the pumice. Consequently, in a pumice bed
clogging progresses more slowly, and the volume of the bed is
used more efficiently than in a sand bed. Backwashing effective-
ly cleans the pumice.โ€
โ€œFor a pumice bed, smaller head loss and greater turbidity
removal efficiency was observed in comparison to a sand bed
under the same experimental conditions.โ€
โ€œA pumice bed has a greater porosity and higher deposition
capacity of particulate compared to sand bed, so pumice bed
filters have longer periods between backwashes.โ€
โ€œPumice is resistant to acid and base solutions. No deformation
because of the water was observed during the study.โ€
TITLE: A comparison study on the removal of suspended
solids from irrigation water with pumice and sandโ€“gravel
media filters in the laboratory scale*.
ABSTRACT: In this study, different bed materials in media filter
systems were examined to determine the solids removal
efficiency, total outlet flow volume, and outlet flow velocity of
P U M I C E A S A F I L T R A T I O N M E D I A
REMOVALRATE(%)
TIME (MINUTE) โ–  PUMICE โ–  SAND
FIGURE 10: The comparison of turbidity removal ratios with time for the pumice and
sand bed (750 mm bed depth, 7.64 m3/m2.h flow rate & 0.5-1.0 mm grain size).
0 25 50 100 150 200
100
90
80
70
RESEARCH STUDIES (continued)
pumice (with its numerous open spaces, vesicles and irregular
cavities) sandโ€“gravel, and combination of pumice and
sandโ€“gravel.Two different filter column diameters (150 and
200mm) and two different inlet flow pressures (100 and 150
kPa) were used.The results show that the total outlet flow
volumes increased logarithmically as the filtration test period
progressed, while the outlet flow velocities and the outlet
concentrations of suspended solids decreased logarithmically
for all filter types. Pumice media filters provided higher total
outlet flow volumes and lower solid removal efficiency in
comparison with sandโ€“gravel media filters. However, the
highest average solid removal efficiency was determined by
pumice plus a sandโ€“gravel media filter at 90.5%.
*Yasemin Kuslu & Ustun Sahin (2013). Agricultural Structures and
Irrigation Department, Ataturk University Faculty of Agriculture,
Erzurum 25240,Turkey. Published in Desalination and Water Treatment,
51:10-12, 2047-2054, DOI: 10.1080/19443994.2013.734492
EXCERPTS FROM PUBLISHED RESEARCH: โ€œIn the beginning
hours of the filtration test period, the outlet flow velocities of
pumice media filters were lower than sandโ€“gravel media filters.
This is because pumice is a material with very rough grains that
increase resistance to flow, and after the first few hours of the
test period, the outlet flow velocities of the pumice media
filters were higher than sandโ€“gravel media filters because of its
highly porous nature.โ€
โ€œWhen the pumice media was subjected to pressure, suspense
solids retained in irregular cavities went out at higher concen-
tration than the sandโ€“gravel media.โ€
โ€œ... the outlet concentration of suspended solids for pumice
media filters was lower than that of sandโ€“gravel media filters
without pressure flow conditions.โ€
โ€œThe average removal efficiencies of the different filter types
were calculated at 74.9% for pumice in 200mm diameter
column at 100 kPa inlet flow pressure, 73.0% for pumice in
200mm column at 150 kPa inlet flow pressure, and 90.5% for
pumice plus sand-gravel in 200mm diameter column at
150 kPa inlet flow pressure.โ€
โ€œThe pumice media filter, due to its higher total outlet flow
volumes, can be used for the filtration of waters
with a high suspended solid concentration.โ€
โ€œ... both pumice and pumice plus sandโ€“gravel
media filters are suitable for lower pressure
micro-irrigation [systems]โ€
TABLE: The Properties of Different Filter Layers
Number Layer Material Effective Diameter Uniformity PorosityValues of
of Layers Depth(mm) Sizes(mm) (mm) Coefficient Granular Medium(%)
Pumice Sand-Gravel Pumice Sand-Gravel Pumice Sand-Gravel
1โ€“7 64 8โ€“12.5 8.80 8.60 0.92 0.90 80.3 41.1
2โ€“6 64 4โ€“8 5.03 5.00 0.83 0.83 77.4 43.6
3โ€“5 128 2โ€“4 2.42 2.42 0.81 0.82 74.6 45.0
4 340 0.5โ€“1 0.58 0.61 0.97 0.85 71.7 46.4

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Pumice as a Water Filtration Media (knowledge brief)

  • 1. K N O W L E D G E B R I E F Pumice as a Filtration Media Pumice is, at its essence, foamed glass, formed by the expansion of trapped gases when molten lava rapidly cools. When crushed, pumice still retains its frothy structure, making it effective at any filtration grade. As a filtration media, pumice is an aggressively-filtering alternative to sand (and other filtration media). The low specific gravity and high porosity of pumice make it ideal for irrigation filtration systems and other water treatment processes and provides several advantages over other filtration media such as sand, expanded clay, and anthracite. BENEFITS OF PUMICE FORWATERTREATMENT APPLICATIONS INCLUDE: โ–  Improved filtration rates โ–  Better filtration bed expansion โ–  Less energy consumption โ–  Larger effective surface area โ–  Less intensive backwash requirements โ–  Low-cost filter refurbishment KEY PUMICE CHARACTERISTICS: โ–  Specific gravity weight of 2.35 g/cc โ–  Low unit weight: 40 - 50 lbs cubic foot (depending on grade) โ–  MOHS-scale hardness: 6 (reference: feldspar is a 6 and quartz is a 7) โ–  Due to its amorphous characteristics, pumice is not considered a health risk to the workers who handle it. โ–  Chemically, pumice is primarily Silicon Dioxide (Amorphous Aluminum Silicate), some Aluminum Oxide, and trace amounts of other oxides. RESEARCH STUDIES The information that follows, from a pair of research studies, examines the perfor- mance of pumice as a granular media to replace or supplement common sand media in agriculture irrigation filtration media tank systems such as those used to protect drip and micro-irrigation systems from fine particle and organic solids. close-up of a 1-inch pumice stone crushed pumice (G2) at 100x magnification (208) 766-4777 x111 email: rd@hesspumice.com www.hesspumice.com TITLE: The performance of pumice as a filter bed material under rapid filtration conditions*. ABSTRACT: Deep bed sand filters are used extensively in drinking water and wastewater treatment. In this study, sand and pumice were used as a filtration media under rapid filtration conditions and performance results for both were compared.Turbidity removal performance and head losses were investigated as functions of filtration rate, bed depth and particle size. Under the same experimental conditions such as 750 mm bed depth, 7.64m3/m2.h flow rate and, 0.5-1.0 mm grain size, turbidity removal rates for sand and pumice were found to be 85-90% and 98-99%, respectively. Furthermore, the head loss for sand and pumice were found to be 460 mm and 215 mm, respectively.The results obtained have shown that pumice has a high potential for use as a filter bed material. * Burhanettin Farizoglu, Bulent Keskinler. Published in Filtration and Separation, April 2003 EXCERPTS FROM PUBLISHED RESEARCH: โ€œDue to the high porosity of pumice, a filter bed consisting of pumice retains more suspended solids than a sand filter bed (head loss 0~ e-4). Thus, the clogging observed in the pumice bed is smaller than a sand filter bed with a similar grain size.The increase in head loss over time for pumice progresses more slowly than with sand media.โ€(FIGURE 9) HEADLOSS(MM) TIME (MINUTE) โ–  PUMICE โ–  SAND FIGURE 9: The comparison of head loss values with time for the sand and pumice bed (750 mm bed depth, 7.64 ma/m~.h flow rate & 0.5-1.0 mm grain size). 0 40 80 120 160 200 500 400 300 200 100
  • 2. CONTINUED: The performance of pumice as a filter bed material under rapid filtration conditions โ€œSand is not a porous material and particulate material can only be retained in the spaces between the grains in the filter bed, so smaller particulate matter can more easily drain through the sand media and escape in the effluent water.โ€(FIGURE 10) โ€œWhen pumice is used as filter bed material it is possible to distinguish between two levels of porosity, one of the pumice itself and the other of the filter bed.Thus, while bigger particles are retained in the filter bed, smaller particles are retained inside the pores of the pumice. Consequently, in a pumice bed clogging progresses more slowly, and the volume of the bed is used more efficiently than in a sand bed. Backwashing effective- ly cleans the pumice.โ€ โ€œFor a pumice bed, smaller head loss and greater turbidity removal efficiency was observed in comparison to a sand bed under the same experimental conditions.โ€ โ€œA pumice bed has a greater porosity and higher deposition capacity of particulate compared to sand bed, so pumice bed filters have longer periods between backwashes.โ€ โ€œPumice is resistant to acid and base solutions. No deformation because of the water was observed during the study.โ€ TITLE: A comparison study on the removal of suspended solids from irrigation water with pumice and sandโ€“gravel media filters in the laboratory scale*. ABSTRACT: In this study, different bed materials in media filter systems were examined to determine the solids removal efficiency, total outlet flow volume, and outlet flow velocity of P U M I C E A S A F I L T R A T I O N M E D I A REMOVALRATE(%) TIME (MINUTE) โ–  PUMICE โ–  SAND FIGURE 10: The comparison of turbidity removal ratios with time for the pumice and sand bed (750 mm bed depth, 7.64 m3/m2.h flow rate & 0.5-1.0 mm grain size). 0 25 50 100 150 200 100 90 80 70 RESEARCH STUDIES (continued) pumice (with its numerous open spaces, vesicles and irregular cavities) sandโ€“gravel, and combination of pumice and sandโ€“gravel.Two different filter column diameters (150 and 200mm) and two different inlet flow pressures (100 and 150 kPa) were used.The results show that the total outlet flow volumes increased logarithmically as the filtration test period progressed, while the outlet flow velocities and the outlet concentrations of suspended solids decreased logarithmically for all filter types. Pumice media filters provided higher total outlet flow volumes and lower solid removal efficiency in comparison with sandโ€“gravel media filters. However, the highest average solid removal efficiency was determined by pumice plus a sandโ€“gravel media filter at 90.5%. *Yasemin Kuslu & Ustun Sahin (2013). Agricultural Structures and Irrigation Department, Ataturk University Faculty of Agriculture, Erzurum 25240,Turkey. Published in Desalination and Water Treatment, 51:10-12, 2047-2054, DOI: 10.1080/19443994.2013.734492 EXCERPTS FROM PUBLISHED RESEARCH: โ€œIn the beginning hours of the filtration test period, the outlet flow velocities of pumice media filters were lower than sandโ€“gravel media filters. This is because pumice is a material with very rough grains that increase resistance to flow, and after the first few hours of the test period, the outlet flow velocities of the pumice media filters were higher than sandโ€“gravel media filters because of its highly porous nature.โ€ โ€œWhen the pumice media was subjected to pressure, suspense solids retained in irregular cavities went out at higher concen- tration than the sandโ€“gravel media.โ€ โ€œ... the outlet concentration of suspended solids for pumice media filters was lower than that of sandโ€“gravel media filters without pressure flow conditions.โ€ โ€œThe average removal efficiencies of the different filter types were calculated at 74.9% for pumice in 200mm diameter column at 100 kPa inlet flow pressure, 73.0% for pumice in 200mm column at 150 kPa inlet flow pressure, and 90.5% for pumice plus sand-gravel in 200mm diameter column at 150 kPa inlet flow pressure.โ€ โ€œThe pumice media filter, due to its higher total outlet flow volumes, can be used for the filtration of waters with a high suspended solid concentration.โ€ โ€œ... both pumice and pumice plus sandโ€“gravel media filters are suitable for lower pressure micro-irrigation [systems]โ€ TABLE: The Properties of Different Filter Layers Number Layer Material Effective Diameter Uniformity PorosityValues of of Layers Depth(mm) Sizes(mm) (mm) Coefficient Granular Medium(%) Pumice Sand-Gravel Pumice Sand-Gravel Pumice Sand-Gravel 1โ€“7 64 8โ€“12.5 8.80 8.60 0.92 0.90 80.3 41.1 2โ€“6 64 4โ€“8 5.03 5.00 0.83 0.83 77.4 43.6 3โ€“5 128 2โ€“4 2.42 2.42 0.81 0.82 74.6 45.0 4 340 0.5โ€“1 0.58 0.61 0.97 0.85 71.7 46.4