NANOADSORBENT BASED USER-FRIENDLY HOUSEHOLD FILTER FOR THE PURIFICATION OF FLUORIDE AND ARSENIC CONTAMINATED DRINKING WATER

Abstract

A nanoadsorbent based filter is used for purification of fluoride and arsenic contaminated water. 140-150 g low cost (10 USD/kg) nanoparticles of gamma alumina of 20-25 mg/g fluoride and 25-30 mg/g arsenic adsorption capacity is incorporated in propylene filter without susceptibility of leaching incorporated nanoparticles in water. The cost of domestic defluoridation device containing low cost nanoalumina incorporated filters/cartridges along with housing, overhead tank, tubing and treated water storage container etc. is of very low cost of around 25 USD/device. The fluoride treatment cost would be <0.5 USD/100 lit for 4-5 mg/l fluoride water after 2-3 regenerations while, the arsenic treatment cost using domestic filtration device would be <0.25 USD/100 lit for 90-100 g/l arsenic (III) water. A method incorporates nanoadsorbent in a sediment removal filter candle and provides a household defluoridation device capable of treatment of fluoride and arsenic contaminated ground/drinking water without electricity.

Claims

1. Nanoadsorbent based user-friendly filter for the purification of fluoride and arsenic contaminated water, comprises of following steps: a. incorporating 130-150 g of gamma alumina nanoadsorbent in sediment removal filter cartridge; b. arranging cartridges in series by attaching the inlet to the overhead tank containing contaminated water and connecting the outlet in container where treated water is stored.

2. Nanoadsorbent based user-friendly filter for the purification of fluoride and arsenic contaminated water as claimed in claim 1, wherein the low cost synthesis of gamma alumina nanoparticles is done using inexpensive aluminum salt, sodium hydroxide.

3. Nanoadsorbent based user-friendly filter for the purification of fluoride and arsenic contaminated water as claimed in claim 1, wherein filter can work in the gravity force for filtration, without using electricity.

4. Nanoadsorbent based user-friendly filter for the purification of fluoride and arsenic contaminated water as claimed in claim 1, wherein filtration rate can be adjusted by increasing the height of the water head tank.

5. Nanoadsorbent based user-friendly filter for the purification of fluoride and arsenic contaminated water as claimed in claim 1, wherein the said process removes 20-30 mg/g fluoride ions and 25-30 mg/g arsenic (III).

6. Nanoadsorbent based user-friendly filter for the purification of fluoride and arsenic contaminated water as claimed in claim 1, wherein three cartridges can treat 4-5 mg/l of fluoride contaminated 3000-4000 litre water after 2-3 regenerations and 9-10 mg/l of fluoride contaminated 1500-2000 lit drinking after 2-3 regenerations.

7. Nanoadsorbent based user-friendly filter for the purification of fluoride and arsenic contaminated water as claimed in claim 1, wherein three cartridges can treat 90-100 g/l of arsenic contaminated 6000-7000 litre water after 2-3 regenerations and 240-250 g/l of arsenic contaminated 2000-3000 lit drinking water after 2-3 regenerations.

Description

BRIEF DESCRIPTION OF DRAWINGS

[0016] FIG. 1: The drawing of the purifier operating for continuous treatment. [0017] Component 1: Inlet of the contaminated water [0018] Component 2: First chamber containing only the sediment cartridge [0019] Component 3: Housing 1 [0020] Component 4: Cartridge containing the hollow perforated tube wrapped with carbon containing polypropylene cloth [0021] Component 6, 8 10: Housing containing the cartridges with the nanoalumina [0022] Component 7, 9, 11: Cartridges containing hollow perforated tube wrapped with the nanoalumina coated polypropylene cloth [0023] Component 12: Outlet for the treated water.

[0024] FIG. 2: Detailed view of component 3 of FIG. 1. [0025] Component 1: Polypropylene cloth with carbon only wrapped around the perforated hollow tube [0026] Component 2: Perforated hollow tube.

[0027] FIG. 3: Detailed view of component 7, 9 and 11 of FIG. 1. [0028] Component 1: Polypropylene cloth coated with nanoalumina wrapped around perforated hollow tube. [0029] Component 2: Perforated hollow tube.

[0030] FIG. 4: Detailed view of perforated tube with the dimensions. [0031] Component 1: Hollow perforated tube.

DETAILED DESCRIPTION OF THE INVENTION

[0032] In an embodiment of the present invention, methodology developed for the incorporation of nanoparticles of alumina in sediment removal filter/cartridges, can be adopted for any types of adsorbent. The low cost nanoparticle of gamma alumina is synthesized to bring down fluoride treatment cost significantly low [I. B. Singh, Archana Singh, Indian patent submitted, Application No: 0056NF2016]. Firstly, sodium aluminate was prepared by pure aluminum metal in 2M sodium hydroxide solution. The prepared sodium aluminate is subjected for precipitation reaction under stirring condition and by drop by drop addition of 2M sulphuric acid solution till pH reached at around 7. White gel like precipitates formed which is mainly hydrous aluminum hydroxide Al(OH).sub.3.nH.sub.2O. This is heated at a temperature in the range of 480 to 500 C. in muffle furnace for five hours followed by their grinding in mechanized mortar pistil for 5-6 hour to get nanoparticle of gamma alumina of size in the range of 20-25 nm of surface are in the range of around 250-300 m.sup.2/g. Finally the adsorption kinetics study of fluoride and arsenic in water was carried out to see the removal potential of the synthesized nanoparticles of gamma alumina. Before incorporating in sediment removal cartridge, fluoride and arsenic adsorption capacity of the synthesized nanoparticles was estimated through adsorption studies, are found as 20-30 mg/g and 25-30 mg/g, respectively.

[0033] In another embodiment of the present invention, 130-150 g synthesized nanoparticles of gamma alumina has been incorporated in conventional sediment removal cartridge made of polypropylene cloth sheet. For making cartridge, one end closed perforated polymer make cylindrical tube (dia 30 mm, length 230 mm, thickness 1 mm) is used whose another end was threaded and can be fixed properly in the housing. In making of filter candle, firstly one layer polypropylene make thread is wrapped over the perorated tube (FIG. 1-5). Incorporation of the nanoalumina particle in the cartridges is made through nanocoating methodology (thickness in the range of 400-500 m) over polypropylene sheet/cloth layer by layer coating.

[0034] In this way 140-150 g synthesized nanoparticles of gamma alumina were incorporated in each filter cartridges/candle.

[0035] In yet another embodiment of the present invention, household filtration device was made (FIG. 1-5) where two or three number of nanoparticle incorporated filter cartridges were fitted in housing in series in which out let of first is connected to inlet of second one. Similarly outlet of second connected to inlet of third one and outlet of third cartridges open in the storage container where treated water gets stored. The inlet of first housing is connected separately to the outlet of standard sediment removal cartridges containing carbon whereas inlet of standard sediment removal filter is connected to 20-50 lit capacity overhead tank from where fluoride or arsenic contaminated water enter in to the standard sediment removal filter and then nanoadsorbent containing cartridges. In addition of removal of turbidity, physical impurities, sediment etc, standard sediment removal also removes odors, smell, and color of the contaminated water. 50-100 g/l arsenic or 2-5 mg/l fluoride is mixed accordingly in water of overhead tank which contain the cation from the group consisting of sodium, potassium, calcium, magnesium etc. and anions from the group consisting of chloride, nitrate, sulphate, carbonate, bicarbonate etc which are generally present in ground water. The height of the overhead tank from the candle housing can be kept 3-4 feet above and adjustable in order to maintain flow rate of around 1-5 lit/h. Every after 100 liter of filtration residual arsenic or fluoride present in the treated water was analyzed.

[0036] In still another embodiment of the present invention, residual fluoride was analyzed by spectrophotometer (Hack39000, method no) using alizarin red visual method and Spand solution whereas arsenic was analyzed using Hack arsenic kit. Alizarin red indicator was prepared using zirconyl chloride octahydrate (ZrOCl.sub.2) and mg alizarin red dye (3-alizarin sulphonic acid sodium salt). In the presence of fluoride ions, zirconium ions get replaced by fluoride ion from the complexes resulting in re-appearance of original yellow color of zirconium. Concentration of residual fluoride was determined by comparing color of standard solution of fluoride in water. The intensity of yellow color depends on the concentration of residual fluoride present in the working solution. In preparation of standard solution, blank (0.0), 0.2, 0.4, 0.6, 0.8, 1.0 and 1.2 mg/L fluoride bearing water solutions were prepared in 50 ml volume containing nessler tube. 5 mL of prepared alizarin red indicator was added in each solution which showed different shades of color from dark red (blank) to faded yellow (fluoride bearing). Solutions were also prepared from the filtrates obtained after batch adsorption in identical condition.

[0037] In another embodiment of the present invention, the experimental design was customer specified and was modified to understand the performance of candle filter for testing bacteria removal efficiency of the developed cartridges. The removal studies in treated water are done as per U.S. Environmental Protection Agency (USEPA) and NSF International standard using test bacteriaKlebsiella terrigen (1-3103 CFU/100 ml); VirusMS2 Bacteriophage (1-3103 CFU/L); Cyst of Giardia (1-3103 CFU/L) in 20 liter water which passed through the filter at 1-2 lit/h filtration rate. Bacteria removal studies are done by membrane filtration and standard plate count using selective media method. Virus removal studies are carried out using agar overlay method while cyst removal studies are done by microscopy technique.

EXAMPLES

Example 1

[0038] 130-140 g nanoparticles incorporated both filters candle shown more than 95% fluoride removal (treated water contains 0.5-0.8 ppm) of 5 ppp fluoride containing initial 200 liter of water with filtration rate nearly in the range of 0.8 lit-1 lit/h (20-4 lit in 24 h). Even single filter candle shown more than 90% fluoride removal (treated water contains 1 ppm fluoride) of 5-5 pp fluoride containing water with filtration rate of 1 lit/h (24 liter in 24 h). Both filters have also shown fluoride removal capability for 10 mg/l fluoride containing water as more than 90% fluoride removal (treated water contains 0.8-1.0 ppm) was obtained for 10 mg/l fluoride containing water.

Example 2

[0039] As given in example 1, both filters shown more than 90% fluoride removal (treated water contain 0.8-1.0 ppml fluoride) of 5.5 ppm fluoride containing another 200 liter of water (total 400 liter) with filtration rate of 0.8 lit/h (20 lit in 24 h). Single filter candle shown nearly 70 fluoride removal (treated water contain around 1.2-1.4 mg/l fluoride) of 5 ppm fluoride containing water after 400 liter of treatment. Both filter have shown fluoride removal capability of 10 mg/l fluoride containing water as more than 80% fluoride removal (treated water contains 1.3-1.5 ppm fluoride) is obtained after treatment of 400 liter 10 mg/l fluoride water. This indicate that both filter can also treat maximum 350-400 liter water containing more than 10 mg/l fluoride.

Example 3

[0040] As given in example 1, both filters have shown more than 80% fluoride removal (treated water contain 1.1-1.4 ppml fluoride) of 5.5 mg/l fluoride containing another 200 liter of water (total 600 liter). Fluoride removal capability of single filter candle decreases substantially after 500 liter of 5 ppml fluoride containing water as 2.5-3.0 mg/l residual fluoride was obtained in treated water using single filter after treatment of 500 lit Of 5.5 ppm fluoride water. The fluoride removal capability of both filter reduces significantly for treatment of 10 mg/l fluoride water as around 3.0-3.5 ppm residual fluoride was found in treated water of 10 mg/l fluoride containing water.

Example 4

[0041] As given in example 1, both filter shown more than 70% fluoride removal (treated water contain around 1.3-1.5 ppml fluoride) of 5.5 ppml fluoride containing another 200 liter of water (total 800 liter). Occurrence of 1.3-1.5 mg/l in treated water is almost within the WHO prescribed limit of 1.5 mg/l fluoride in drinking water.

Example 5

[0042] As given in example 1, both filter shown more than 60% fluoride removal (treated water contain around 1.6-1.90 ppm fluoride of 5.5 ppml fluoride containing another 200 liter of water (total 1000 liter). Presence of more than 1.5 ppm fluoride in treated water exceeded the WHO guidelines of maximum permissible level of fluoride (1.5 mg/l) in drinking water. Therefore both filters can treat maximum 700-800 lit of 5.5 ppm fluoride water.

Example 6

[0043] As given in example 1-5, concentration the different cations and anions present in the tape water, is found almost same after fluoride removal. This indicates that present synthesized nanolaumina particles shows their ability of fluoride adsorption without affecting concentration of other mineral constituents of water.

Example 7

[0044] As given in example 1-5, a slight turbidity of treated water is observed for initial 2-3 lit of filtration. Afterward filtered water was observed crystal clear without any turbidity. This indicates that incorporated nanoparticles do not diffuse from the nanoparticles incorporated polypropylene cloth in the treated water.

Example 8

[0045] 140-150 g nanoparticles incorporated three cartridges containing filtration device shown more than 90% fluoride removal, (treated water contains 0.2-0.7 mg/l fluoride) of 5 mg/l fluoride containing 500 liter of tap water (pH 6.5-8.3, TDS 310-350 mg/l) with filtration rate of 3-5 lit/h. Above device has also shown fluoride removal capability for 10 mg/l fluoride containing water as more than 85% fluoride removal (treated water contains 0.5-1.5 mg/l) was obtained for 10 mg/l fluoride containing water up to 500 liter volume.

Example 9

[0046] 140-150 g nanoparticles incorporated three cartridges containing filtration device shown more than 90% arsenic removal (0-6 g/l) of 100 g/l arsenic containing initial 1000 liter tap water (pH 8.1-8.3, TDS 310-350 mg/l) with filtration rate of 3-5 l/h. Above device have also shown arsenic removal capability for 250 g/l arsenic containing water as 500 liter of 250 ppb arsenic containing water can be treated that contains 5-20 g/l arsenic as residual arsenic in treated water.

Example 10

[0047] As given in example 1, above filtration device has shown more than 85% fluoride removal (treated water contain 0.7-1.0 mg/l fluoride) of 5 mg/l fluoride containing another 500 liter of water (total 1000 liter). The fluoride removal capability of the filtration devices reduces slightly for treatment of 10 mg/l fluoride water as around 1.2-1.6 mg/l fluoride occurred in treated water after treatment of next 500 liter of 10 mg/l fluoride containing water.

Example 11

[0048] As given in example 2, above filtration device has shown more than 90% arsenic removal (treated water contain 6-9 g/l arsenic) of 100 g/l ppb arsenic containing another 1000 liter tap water (total 2000 liter).

Example 12

[0049] As given in example 1, developed filter device shown more than 80% fluoride removal (treated water contain around 1.0-1.4 mg/l fluoride) of 5 mg/l fluoride containing another 500 liter of water (total 1500 liter). Occurrence of 1.1-1.4 mg/l in treated water is within the WHO prescribed limit of 1.5 mg/l fluoride in drinking water.

Example 13

[0050] As given in example 2, developed filter device has shown more than 85% arsenic removal (treated water contain around 9-15 g/l arsenic) of 100 g/l arsenic containing another 1000 liter of water (total 3000 liter). This concentration of arsenic in treated water is almost nearby in the range of WHO prescribed limit of 10 g/l arsenic in drinking water.

Example 14

[0051] As given in example 1, developed filter device shown more than 70% fluoride removal (treated water contain around 1.4-1.8 mg/l fluoride) of 5 mg/l fluoride containing another 500 liter of water (total 2000 liter). Presence of this range of fluoride in the treated water is almost equal to the permissible limit of fluoride in drinking water as per WHO guidelines. Therefore developed filter device can treat maximum 1500-2000 lit of 5 mg/l fluoride water before saturation.

Example 15

[0052] As given in example 2, developed filter device remove more than 80% arsenic removal (treated water contain around 10-20 g/l arsenic) of 100 g/l arsenic containing another 1000 liter of water (total 4000 liter). Presence of 10 g/l arsenic fluoride in treated water is around the permissible limit of arsenic in drinking water as per WHO guidelines. Therefore developed filter can treat maximum 3000-3500 lit of 100 g/l arsenic containing water.

Example 16

[0053] Based on example 7, it is estimated that developed filter device can treat more than 3000-4000 liter of 2-3.0 mg/l fluoride containing water before saturation.

Example 17

[0054] Based on example 8, it is estimated that developed filter device can treat 6000-7000 liter of 50-60 g/l arsenic containing water before saturation.

Example 18

[0055] As given in example 1-10, concentration of the different cations and anions present in the tap water, is found almost same after arsenic or fluoride removal. This indicates that present synthesized nanolaumina particles shows their strong affinity for arsenic or fluoride of water without affecting concentration of other mineral constituent of water.

Example 19

[0056] As given in example 1-10, a slight turbidity of treated water is observed for initial 5-10 lit of filtration. Afterward filtered water becomes clear without any turbidity. This indicates that incorporated nanoparticles do not diffuse from the polypropylene cloth in the treated water.

Example 20

[0057] As given in example 9, the saturated nanoadsorbent of the filter can be regenerated by use of 1.5-2.0% sodium hydroxide solution and 1.5-2% sulphuric acid or 4-5% aluminum sulphate solution.

Example 21

[0058] As given in example 7 and 13, the regenerated nanoadsorbent of the developed device can further treat another 1000-1500 liter 5 mg/l containing tap water of TDS <300 mg/l and pH 6.5-8.3 range.

Example 22

[0059] As given in example 8 and 13, the regenerated nanoadsorbent of the developed device can further treat another 1200-1800 liter of 100 g/l arsenic containing tap water of TDS <300 mg/l and pH 6.5-8.5 range.

Example 23

[0060] As given in example 7 and 8, the saturated nanoadsorbent can be regenerated and reused for the fluoride and arsenic removal after three regenerations.

Example 24

[0061] As given in example 1 and 2, nearly 90% removal of bacteria and more than 99% removal of viruses and cyst are observed.

Advantages of the Present Invention

[0062] Methodology developed for the incorporation of nanoparticles of alumina in conventional sediment removal cartridges/candle is simple and feasible in making at large scale. [0063] Developed household water treatment device is very simple that contains nanoalumina incorporated cartridges/candle, housing, overhead tank, tubing and treated water storage container. [0064] The developed filtration device work on gravity force, hence no electricity requires. [0065] The developed filtration device can provide safe drinking water at very low treatment cost of 0.5 USD/100 lit for 1-5 mg/l fluoride and 0.15 USD/100 lit for 90-100 g/l arsenic contaminated water. [0066] Present synthesized nanoparticles of gamma alumina that possess an excellent fluoride removal capacity, is of very low cost (10 USD) and can be synthesized in bulk scale using inexpensive raw materials like aluminum salt, sodium hydroxide, etc. [0067] 140-150 g nanoalumina incorporated cartridges is of very low cost (<5 USD/cartridge) including cost of synthesized nanoalumina particles using present low cost synthesis method. [0068] The cost of filtration device containing low cost synthesized nanoalumina incorporated filters/cartridge as claim in 1 & 2, along with housing, overhead tank, tubing and treated water storage container etc is of very low cost of around 25 USD. [0069] Besides removal of arsenic and fluoride, developed nanoalumina incorporated filtration device can also remove chromium. Lead, cadmium etc of drinking water. [0070] Present synthesized nanoadsorbent also acts as antiviral and antibacterial and thus destroys these microorganisms up to maximum level. [0071] The fluoride treatment cost using domestic defluoridation device as claimed in claim 1, would be <0.5 USD/100 lit for 4-5 mg/l fluoride water after 2-3 regenerations. [0072] The arsenic treatment cost using domestic filtration device as claimed in claim 1, would be <0.25 USD/100 lit for 90-100 g/l arsenic (III) water.