GB2413124A - Glass filtration media - Google Patents
Glass filtration media Download PDFInfo
- Publication number
- GB2413124A GB2413124A GB0408196A GB0408196A GB2413124A GB 2413124 A GB2413124 A GB 2413124A GB 0408196 A GB0408196 A GB 0408196A GB 0408196 A GB0408196 A GB 0408196A GB 2413124 A GB2413124 A GB 2413124A
- Authority
- GB
- United Kingdom
- Prior art keywords
- glass
- water
- filtration media
- glass granules
- filter
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
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- 239000011521 glass Substances 0.000 title claims abstract description 72
- 238000001914 filtration Methods 0.000 title claims abstract description 44
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 40
- 238000011282 treatment Methods 0.000 claims abstract description 19
- 239000000126 substance Substances 0.000 claims abstract description 17
- 239000003864 humus Substances 0.000 claims abstract description 16
- 230000003197 catalytic effect Effects 0.000 claims abstract description 12
- 238000004062 sedimentation Methods 0.000 claims abstract description 11
- 230000003647 oxidation Effects 0.000 claims abstract description 9
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 9
- 239000002253 acid Substances 0.000 claims abstract description 5
- 238000001179 sorption measurement Methods 0.000 claims abstract description 5
- 239000002351 wastewater Substances 0.000 claims abstract description 3
- 238000006555 catalytic reaction Methods 0.000 claims abstract 2
- 238000004065 wastewater treatment Methods 0.000 claims abstract 2
- 241000894006 Bacteria Species 0.000 claims description 24
- 238000000034 method Methods 0.000 claims description 12
- 239000002245 particle Substances 0.000 claims description 9
- 230000008569 process Effects 0.000 claims description 8
- 210000003250 oocyst Anatomy 0.000 claims description 6
- 229910052751 metal Inorganic materials 0.000 claims description 4
- 239000002184 metal Substances 0.000 claims description 4
- 150000002739 metals Chemical class 0.000 claims description 4
- 239000003054 catalyst Substances 0.000 claims description 2
- 238000005336 cracking Methods 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 claims 1
- 238000009877 rendering Methods 0.000 claims 1
- 230000002195 synergetic effect Effects 0.000 claims 1
- 239000008187 granular material Substances 0.000 abstract description 41
- 239000004576 sand Substances 0.000 abstract description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 6
- 239000001301 oxygen Substances 0.000 abstract description 6
- 229910052760 oxygen Inorganic materials 0.000 abstract description 6
- 150000003254 radicals Chemical class 0.000 abstract description 5
- 238000011109 contamination Methods 0.000 abstract description 3
- 230000031018 biological processes and functions Effects 0.000 abstract 1
- 238000005406 washing Methods 0.000 abstract 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 12
- 239000010865 sewage Substances 0.000 description 12
- 239000007787 solid Substances 0.000 description 12
- 239000010410 layer Substances 0.000 description 6
- 230000008901 benefit Effects 0.000 description 5
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 4
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 4
- 239000000460 chlorine Substances 0.000 description 4
- 229910052801 chlorine Inorganic materials 0.000 description 4
- 239000000356 contaminant Substances 0.000 description 4
- OSVXSBDYLRYLIG-UHFFFAOYSA-N dioxidochlorine(.) Chemical compound O=Cl=O OSVXSBDYLRYLIG-UHFFFAOYSA-N 0.000 description 4
- 239000007800 oxidant agent Substances 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 150000007513 acids Chemical class 0.000 description 3
- 230000000274 adsorptive effect Effects 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- 229910044991 metal oxide Inorganic materials 0.000 description 3
- 150000004706 metal oxides Chemical class 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 238000009287 sand filtration Methods 0.000 description 3
- 238000012216 screening Methods 0.000 description 3
- 239000003053 toxin Substances 0.000 description 3
- 231100000765 toxin Toxicity 0.000 description 3
- 108700012359 toxins Proteins 0.000 description 3
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 description 2
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 2
- 239000004155 Chlorine dioxide Substances 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 241001148470 aerobic bacillus Species 0.000 description 2
- 230000001580 bacterial effect Effects 0.000 description 2
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 2
- 229910052794 bromium Inorganic materials 0.000 description 2
- 210000002421 cell wall Anatomy 0.000 description 2
- 239000013626 chemical specie Substances 0.000 description 2
- 235000019398 chlorine dioxide Nutrition 0.000 description 2
- 239000000645 desinfectant Substances 0.000 description 2
- -1 hydroxyl ions Chemical class 0.000 description 2
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 229910021645 metal ion Inorganic materials 0.000 description 2
- NDLPOXTZKUMGOV-UHFFFAOYSA-N oxo(oxoferriooxy)iron hydrate Chemical compound O.O=[Fe]O[Fe]=O NDLPOXTZKUMGOV-UHFFFAOYSA-N 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- 238000005549 size reduction Methods 0.000 description 2
- 230000007704 transition Effects 0.000 description 2
- PIILXFBHQILWPS-UHFFFAOYSA-N tributyltin Chemical compound CCCC[Sn](CCCC)CCCC PIILXFBHQILWPS-UHFFFAOYSA-N 0.000 description 2
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- 241000224466 Giardia Species 0.000 description 1
- 229910020175 SiOH Inorganic materials 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 229960005070 ascorbic acid Drugs 0.000 description 1
- 235000010323 ascorbic acid Nutrition 0.000 description 1
- 239000011668 ascorbic acid Substances 0.000 description 1
- 231100000693 bioaccumulation Toxicity 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 125000003636 chemical group Chemical group 0.000 description 1
- 229940090961 chromium dioxide Drugs 0.000 description 1
- UMUXBDSQTCDPJZ-UHFFFAOYSA-N chromium titanium Chemical compound [Ti].[Cr] UMUXBDSQTCDPJZ-UHFFFAOYSA-N 0.000 description 1
- UOUJSJZBMCDAEU-UHFFFAOYSA-N chromium(3+);oxygen(2-) Chemical class [O-2].[O-2].[O-2].[Cr+3].[Cr+3] UOUJSJZBMCDAEU-UHFFFAOYSA-N 0.000 description 1
- IAQWMWUKBQPOIY-UHFFFAOYSA-N chromium(4+);oxygen(2-) Chemical compound [O-2].[O-2].[Cr+4] IAQWMWUKBQPOIY-UHFFFAOYSA-N 0.000 description 1
- AYTAKQFHWFYBMA-UHFFFAOYSA-N chromium(IV) oxide Inorganic materials O=[Cr]=O AYTAKQFHWFYBMA-UHFFFAOYSA-N 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000006735 deficit Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000005357 flat glass Substances 0.000 description 1
- 239000005308 flint glass Substances 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 229940093915 gynecological organic acid Drugs 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000003295 industrial effluent Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- SOQBVABWOPYFQZ-UHFFFAOYSA-N oxygen(2-);titanium(4+) Chemical class [O-2].[O-2].[Ti+4] SOQBVABWOPYFQZ-UHFFFAOYSA-N 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000005315 stained glass Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/02—Loose filtering material, e.g. loose fibres
- B01D39/06—Inorganic material, e.g. asbestos fibres, glass beads or fibres
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/04—Additives and treatments of the filtering material
- B01D2239/0414—Surface modifiers, e.g. comprising ion exchange groups
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2305/00—Use of specific compounds during water treatment
- C02F2305/02—Specific form of oxidant
- C02F2305/023—Reactive oxygen species, singlet oxygen, OH radical
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Geology (AREA)
- Biological Treatment Of Waste Water (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Filtering Materials (AREA)
Abstract
A glass filtration media used as an alternative to sand for the enhanced treatment of water and wastewater. The filtration media is specifically manufactured from green and brown glass bottles. The glass granules are further enhanced by exposure to an acid to increase the surface area available on the glass granules for adsorption and catalysis. In wastewater treatment glass granules are used in a filter immediately after the biological process but before humus tank sedimentation, or in place of the humus tank sedimentation stage. The glass granules will mechanically filter the water and remove prescribed substances. The glass granules may be further processed by fluidized bed washing at a high oxidation potential to remove any contamination and to the sanitize the glass granules. The presence of dissolved oxygen or oxidising chemicals will enhance the surface catalytic properties by increasing still further, the free radical concentration on oxidation potential on the surface of the glass granules.
Description
1 2413124
WATER TREATMENT
The present invention relates to water treatment, and more particularly to an improved process for the treatment of wastewater, sewage effluent and drinking water, using active filtration glass granules With everincreasing levels of water consumption there is increased demand for more efficient and effective methods for treating sewage water to protect the receiving environment.
There is also an increasing problem of chemical contaminants from various sources in sewage water, which require special and costly treatment processes.
Conventional sewage water treatment generally comprises the following process steps: coarse screening . ë . primary sedimentation &-.
biological treatment :. secondary settlement (in humus tanks), and tertiary sand filtration. c. .
With such conventional treatments, the sand filtration stage if employed, is particularly susceptible to failure due to fouling by bacteria and contaminants present in the water.
It is an object of the present invention to avoid or minimize one or more of the above-mentioned problems and disadvantages.
It has now been found that a particular form of granular glass, conveniently referred to herein as active filtration glass granules, provides a particularly effective form of water filtration medium in sewage water treatment. More particularly we have found that such active filtration glass granules can effectively replace the secondary settlement stages, in a sewage water treatment system.
Thus in one aspect the present invention provides a method of and apparatus for, sewage water treatment consisting essentially of the following stages: coarse screening; . e primary sedimentation; biological treatment; and . active filtration glass granule filtration. .e
A. With the method and apparatus of the invention, not only is the apparatus substantially simplified, and the treatment process significantly enhanced, but significant further benefits are obtainable including improved chemical contaminant removal and sewage treatment works performance.
In more detail, the principal reason for sand filter failure is fouling of the sand by bacteria and contaminants present in the water. Active filtration glass granules actively resist biofouling and contamination which provides greatly improved filtration performance and allows active filtration granules to be used before secondary humus tank sedimentation.
The flow of water through a sand or active filtration glass granules filter has to be reversed for approximately 1 to 10 minutes, at intervals ranging from a few hours to several days, in order to clean the filter media. If any of the solids remain in the filter after the standard backflush period, then the solids will gradually accumulate, act as a food source for bacteria, and the filter performance will deteriorate until the filter fails. The time interval to . e . complete failure may be several days to years. The time .
interval is a function of the water quality, the filter media, filter design and operating procedures. In sewage effluent or grossly contaminated biologically active water, *.
: . sand filters cannot normally be used because the filter will rapidly fail due to biofouling. In clean water applications sand filters will also fail, but biofouling will take longer to occur.
Another significant benefit is improved solids removal efficiency. During the humus tank sedimentation phase, the oxygen content in the water will fall, and may become anaerobic. The bacteria floes being removed by the humus tank are aerobic bacteria. The bacteria floe therefore come under stress and shock from exposure to anoxic conditions. As a consequence of bacteria stress, the floes or bacterial colonies will have a tendency to break up into smaller colonies. Filtration of the water prior to the humus tanks therefore means that the bacteria floe being filtered by the active filtration glass granules filter are larger and more stable than the bacteria floe after the humus tank. Since the active filtration glass granules filter is tolerant of high solids loading, removal efficiency by active filtration glass granules filtration is better before humus tank solids separation as opposed to after the humus tanks. .e
A
A further benefit is avoidance of stressing of the bacteria . . recycled back to the beginning of the treatment system, by anoxic conditions. The bacteria will be in a better .
. condition as opposed to bacteria that would normally have been stressed by processing in a humus sedimentation tank.
Yet another benefit relates to the removal of prescribed substances from the sewage water. Prescribed substances are prescribed because they are concentrated by bioaccumulation in the ecosystem. These include compounds such as polychlorinated bi-phenols (PCB's). tri-butyltin (TBT) and dioxin (List 1 and List 2 prescribed substances). Bacteria in a sewage treatment works will certainly concentrate these substances. Bacteria are at the root of the ecosystem, and big-accumulation of toxins starts with the bacteria. The suspended bacteria solids removal efficiency of the active filtration glass granules filter is better before the humus tank rather than after the humus tanks. The removal of prescribed toxins is therefore improved with a solids removal process before the humus tank.
When aerobic bacteria are exposed to anoxic conditions a proportion of the bacteria will succumb and lyse in to the water thereby releasing their contents and prescribed substances back into the water. Organisms under serious . stress tend to discharge into the water, multiply or go into a dormant stage. In all cases a portion of the bacterial . cell biomass and their contents will be released back into the water. The application of active filtration glass . : granules prior to humus tank sedimentation therefore provides a mechanism for the removal of prescribed substance and bio- accumulated toxins from the discharge of sewage and industrial effluent.
The active filtration glass granules used in accordance with the present invention are obtainable from coloured glass, most conveniently from green and/or brown glass bottles. Other kinds of glass, including clear glass, plate glass, and flint glass should be avoided. The glass is in general, first reduced in size by crushing to a pellet size in the region of 3 to 10 mm, preferably around 4 to 8 mm, e.g. about 6 mm. The glass pellets are then further reduced in size by means of glass-onto-glass size reduction processing, conveniently using a vertical shaft impactor, or similar equipment, to produces sub-angular glass granules, in similar size grades to those used in sand filtration. Thus typically there would be used successive layers of the following grades: 4 to 8 mm (corresponding to 2 to 4 mesh size), 1 to 2 mm (8-16 mesh size), and 0.5 to 1.0 mm (16-32 mesh size).
-. - ., In order to avoid impairment of the valuable catalytic and e. * adsorptive properties of these active filtration glass granules, they should not be exposed to temperatures over 150 C. I.
. Active glass granules work by physically filtering the solids from the water and by adsorption of the solids onto the surface of the glass. The catalytic properties of active glass granules in the presence of oxygen, hydrogen peroxide, ozone, chlorine or other oxidizing agent, generates a high oxidation potential on the surface of the glass granules and thereby prevents bacteria from becoming established.
The adsorptive properties are due to the hydrolysed glass surface. (SiOH) on the glass surface reacts with free hydroxyl ions (OH-) in the water, forming Si(OH) 2- and leaving the glass surface negatively charged. The negative charge adsorbs positively charge particles, molecules and ions.
The catalytic properties are generated by metal ions such as ferric oxide and chromium oxides on the surface of the glass.
Other metal oxides present in the glass, or which may be bonded to the glass, if desired to further improve the properties of the active filtration glass granules, include titanium oxides, and transition element metal oxides, as discussed further herein below. The presence of metal oxides .. . on the surface of the glass granules enables the catalytic .e properties thereof. a :
The raw active filtration glass granules as described above - . may be used directly. If desired, though, they may be subjected to further processing to enhance their performance, including one or more of the following.
Fluidised bed fractionation using clean water to remove dust, small particles and flat particles, improves the particle shape and size distribution.
The fluidised water can be at a high oxidation potential using chlorine, chlorine dioxide, ozone, permanganate, bromine, or a strong oxidising agent. The oxidising agent will remove surface biological, organic and inorganic contamination and sanitize the glass granules The microstructure of the glass surface can be changed by low pH conditions using acids such as citric acid, ascorbic acid or other week organic acids. Hydrochloric acid, hydrofluoric acid and other strong acids can also be used in the process.
The acids dissolve the carbonates and salts in the glass to make a rough or porous structure, which has a high surface - . area. The higher the surface area the better the catalytic, ecce adsorptive and absorptive properties of the active filtration . glass granules. c
ate. Exposure to strong bases and high pH using, for example, sodium hydroxide, removes surface layers of the glass granules, exposing surface active sites.
Surface coatings can be bonded onto the glass to change the chemical characteristics of the active filtration glass granules. Chemical groups may include silicones and metals such as titanium dioxide can be added to increase catalytic and selective adsorption properties.
The active filtration glass granules are used in essentially the same manner as a conventional filter sand, with successive layers of progressively smaller mesh size. Thus generally there is provided a coarse base support layer with a thickness of the order of 100 to 200 mm, e.g. 150 mm; an intermediate layer (usually with a mesh size of 8-16) with a thickness of the order of 100 to 200 mm, e.g. 150 mm; and a finer filter layer (usually with a mesh size of 16-32) with a thickness of the order of 300 to 1500 mm, preferably 400 to 1000 mm, e.g. 750 mm.
In accordance with conventional practice, the active .
filtration glass granules filter stage of the invention, may ate also be periodically cleared of accumulated solids by . reversing the water flow, and returning the flushed out solids to the primary sedimentation stage or biological a. stage. .
The active filtration glass granules used in accordance with the present invention have the particular benefits of acting both as a mechanical filtration media and physically removing solids from the water, and also adsorbing charged particles, molecules and ions, as well as acting as a surface catalytic filter media.
In more detail, during the size reduction process, the molecular bonds holding the glass together are broken at the surface. This leaves on the surface of the glass, ions of oxygen, aluminium, silica, ferric oxide, chromium dioxide and other elements or compounds making up the composition of the glass. The breakage of the surface bonds results in an electrical in-balance at the glass surface. In an aqueous solution the glass develops a hydrolyzed negatively charged surface with a high zeta potential. This active surface attracts and adsorbs positively charged particles, positively charged and dipolar organic molecules, and metal ions. Also adsorbed are dipolar organic molecules, including proteins, hydrocarbons, as well as small particles such as viri, . . . bacteria, protozoa, crytosporidia and giardia oocysts. e ë.e
A. Certain chemical species present on the surfaces of the active filtration glass granules exhibit catalytic activity, - -e . such as oxides of iron, chromium titanium and most of the . transition elements. The catalyst works by dissociating molecules such as water and dissolved oxygen to form highly reactive free radicals. The free radicals are generated on the surface of the active filtration glass granules. The radicals can react with any chemical species that can be oxidised such metals and organic compounds. Metals are chelated and oxidised, whilst organic molecules are cracked into smaller, and generally less harmful, compounds.
Organic molecules present on the surface and in the cell wall of bacteria, viri, and protozoa are oxidised. The surface of active filtration glass granules is therefore rendered self- sterilising, and as a result is largely free of biofouling.
Cryptosporidian oocysts are rendered more susceptible to oxidation after they have passed through a sand filter media.
It is believed that the oocyst experiences physical damage to its cell wall, which gives a route by which the disinfectant (chlorine, ozone, Ultra Violet light or oxidising agents) is more effective. In sand filters, the sand normally becomes progressively coated with a layer of bacteria and the polysaccharide gelatinous material excreted by the bacteria. ce. .
The surface of the sand particles thereby becomes cushioned A. at a microscopic level and as a result, less damaging to the oocysts. The active filtration glass granules used in accordance with the present invention tend to be much more ..
free of bacteria, and as a result impact damage to oocysts will be more severe, thereby improving the effectiveness of the disinfectants used, and the safety of the water.
Active filtration glass granules can exert its catalytic action in any water type, however the presence of dissolved oxygen, or oxidising chemicals such as ozone, peroxide, chlorine, chlorine dioxide and bromine, will enhance the surface catalytic properties by increasing still further, the free radical concentration and oxidation potential on the surface of the glass granules.
It will be appreciated that in relation to the coarse screening; primary sedimentation; and biological treatment, stages, any form of these known in the art, may in general be used in the apparatus and process of the present invention.
Thus, for example, in the case of the biological treatment stage, there may be used trickle down flow biofiltration, fluidised bed biofiltration, or activated sludge systems. ë ë ë ë :. a sea. ae . .
Claims (8)
1. A water filtration media manufactured from green or brown glass bottles and used in a filter for the treatment of water and wastewater that actively resists colonization by bacteria.
2. A water filtration media as in claim 1 that when used in a filter may replace or precede the humus tank sedimentation stage in a wastewater treatment process.
3. A glass filtration media as in claim 2 that prevents the release of chemicals and prescribed substances back into the water by not subjecting the bacteria to anoxic stress.
4. A glass filtration media as in the preceding claims with an active surface for the adsorption of chemicals, prescribed substances and small particles.
5. A glass filtration media as in the preceding claims with an active catalytic surface, which generates a zone of high oxidation potential on the surface of the media for the cracking of organic molecules and oxidation of metals.
6. A glass filtration media as in claim 5 that can by further enhanced by the synergistic action of oxidising chemicals and catalysts injected into the water before the glass filtration media. ë ace ë a e
as
7. The filter media as in the proceeding claims that provides an effective means of removing oocysts of protozoa such as *. cryptosporidia from water, or rendering them susceptible to oxidation. :.
8. A filtration media as in the preceding claims that has ,. enhanced surface active properties of catalysis and adsorption by exposure of the glass to an acid as part of the manufacturing process.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB0408196A GB2413124A (en) | 2004-04-13 | 2004-04-13 | Glass filtration media |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB0408196A GB2413124A (en) | 2004-04-13 | 2004-04-13 | Glass filtration media |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| GB0408196D0 GB0408196D0 (en) | 2004-05-19 |
| GB2413124A true GB2413124A (en) | 2005-10-19 |
Family
ID=32320730
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB0408196A Withdrawn GB2413124A (en) | 2004-04-13 | 2004-04-13 | Glass filtration media |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB2413124A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006130052A1 (en) * | 2005-05-30 | 2006-12-07 | Lennart Olausson | Method and device for purification of water |
| WO2011038468A1 (en) * | 2009-10-02 | 2011-04-07 | Poolrite Research Pty Ltd | Filtration medium |
| EP2322262A1 (en) * | 2009-11-16 | 2011-05-18 | Bräutigam Kunststoffsysteme GmbH | Filter material for filters in water treatment and processing facilities |
| GB2521667A (en) * | 2013-12-30 | 2015-07-01 | Howard Thomas Dryden | Activation of glass as a molecular sieve adsorber for water filtration and desalination |
| WO2015113575A1 (en) | 2014-01-29 | 2015-08-06 | Dennis Mason | Treatment device and method for destructing micro-organisms in gaseous or liquid media |
| US20190023587A1 (en) * | 2017-07-24 | 2019-01-24 | Notes Intellectual Properties, LLC | Produced water filtration |
| CN110548339A (en) * | 2018-06-01 | 2019-12-10 | 天津华清环宇环保科技有限公司 | Preparation method of novel glass residue filtering material with modified negatively charged surface |
| US11001518B1 (en) * | 2020-02-12 | 2021-05-11 | Rio Resources Llc | Methods for treatment and purification of oil and gas produced water |
| US20240308884A1 (en) * | 2021-02-10 | 2024-09-19 | Inovaya | Water Treatment Unit Comprising a Plurality of Filtration Devices |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN119793072B (en) * | 2025-02-11 | 2025-12-30 | 北京中科康仑能源科技有限公司 | An oil removal filter material, its preparation method and application |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4225443A (en) * | 1978-03-22 | 1980-09-30 | The Taulman Company | Sintered-glass-granule filter medium |
| WO1996023587A1 (en) * | 1995-01-30 | 1996-08-08 | R & J Hansen, L.L.C. | Method for recycling glass and its uses |
| JP2000246282A (en) * | 1999-02-26 | 2000-09-12 | Sato Benec Co Ltd | Sewage treatment apparatus |
| JP2001048556A (en) * | 1999-08-02 | 2001-02-20 | Toshio Hoshino | Continuously porous sintered glass to which inorganic material powder is fused and the production process therefor |
| JP2003055064A (en) * | 2001-08-13 | 2003-02-26 | Takenobu Shiga | Vitreous foamed body and its production method |
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2004
- 2004-04-13 GB GB0408196A patent/GB2413124A/en not_active Withdrawn
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4225443A (en) * | 1978-03-22 | 1980-09-30 | The Taulman Company | Sintered-glass-granule filter medium |
| WO1996023587A1 (en) * | 1995-01-30 | 1996-08-08 | R & J Hansen, L.L.C. | Method for recycling glass and its uses |
| JP2000246282A (en) * | 1999-02-26 | 2000-09-12 | Sato Benec Co Ltd | Sewage treatment apparatus |
| JP2001048556A (en) * | 1999-08-02 | 2001-02-20 | Toshio Hoshino | Continuously porous sintered glass to which inorganic material powder is fused and the production process therefor |
| JP2003055064A (en) * | 2001-08-13 | 2003-02-26 | Takenobu Shiga | Vitreous foamed body and its production method |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006130052A1 (en) * | 2005-05-30 | 2006-12-07 | Lennart Olausson | Method and device for purification of water |
| WO2011038468A1 (en) * | 2009-10-02 | 2011-04-07 | Poolrite Research Pty Ltd | Filtration medium |
| CN102655923A (en) * | 2009-10-02 | 2012-09-05 | 泳池水处理设备研究有限公司 | Filtration medium |
| EP2322262A1 (en) * | 2009-11-16 | 2011-05-18 | Bräutigam Kunststoffsysteme GmbH | Filter material for filters in water treatment and processing facilities |
| GB2521667A (en) * | 2013-12-30 | 2015-07-01 | Howard Thomas Dryden | Activation of glass as a molecular sieve adsorber for water filtration and desalination |
| RU2689997C2 (en) * | 2014-01-29 | 2019-05-30 | Де-Ма Ас | Treatment device and method for destruction of microorganisms in gaseous or liquid media |
| WO2015113575A1 (en) | 2014-01-29 | 2015-08-06 | Dennis Mason | Treatment device and method for destructing micro-organisms in gaseous or liquid media |
| US20190023587A1 (en) * | 2017-07-24 | 2019-01-24 | Notes Intellectual Properties, LLC | Produced water filtration |
| CN110548339A (en) * | 2018-06-01 | 2019-12-10 | 天津华清环宇环保科技有限公司 | Preparation method of novel glass residue filtering material with modified negatively charged surface |
| US11001518B1 (en) * | 2020-02-12 | 2021-05-11 | Rio Resources Llc | Methods for treatment and purification of oil and gas produced water |
| US11739017B2 (en) | 2020-02-12 | 2023-08-29 | Rio Resources Llc | Methods and apparatus for treatment and purification of oil and gas produced water |
| US12410084B2 (en) | 2020-02-12 | 2025-09-09 | Rio Resources Llc | Methods and apparatus for treatment and purification of wastewater |
| US20240308884A1 (en) * | 2021-02-10 | 2024-09-19 | Inovaya | Water Treatment Unit Comprising a Plurality of Filtration Devices |
Also Published As
| Publication number | Publication date |
|---|---|
| GB0408196D0 (en) | 2004-05-19 |
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| WAP | Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1) |