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A Water Purification System, Method Of Manufacture Therefor And Method Of Purifying Water Therewith

Abstract: The invention relates to a water purification system, a method pf purifying water using the system and a method of manufacture of the water purification system. The invention particularly relates to a water purification system for packing small quantities of solid chlorine disinfectant which is stable for long period of time thereby ensuring that sufficient chlorine is available for killing of time thereby ensuring that sufficient chlorine is available for killing of harmful micro0organisms in water to make it safe for human consumption. Accordingly, the invention provides a water purification system comprising a sachet containing granules of calcium hypochlorite.

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Patent Information

Application #
Filing Date
28 March 2007
Publication Number
04/2009
Publication Type
INA
Invention Field
CHEMICAL
Status
Email
Parent Application
Patent Number
Legal Status
Grant Date
2014-06-27
Renewal Date

Applicants

HINDUSTAN UNILEVER LIMITED
HINDUSTAN LEVER HOUSE, 165/166 BACKBAY RECLAMATION, MUMBAI- 400020,

Inventors

1. KADAM MANOJ KRISHNA
R.NO.3613, BLDG.NO.106, NEHRU NAGAR, POLICE COLONY, EAST KURLA, MUMBAI- 400 024
2. NADAKATTI SURESH MURIGEPPA
A-312, FERN SAROJ APTS, LBS NAGAR, HAL POST, BANGLORE 560017
3. TENDULKAR MAHESH SUBHASH
C/311, GURUDASHAN, CO-OPERATIVE HOUSING SOCIETY, NAVGHAR VILLAGE, NEAR DUTTA MANDIR, BHAYANDER(EAST), THANE 401105

Specification

FORM - 2
THE PATENTS ACT, 1970
(39 of 1970)
&
The Patents Rules, 2006
PROVISIONAL SPECIFICATION
(See Section 10 and Rule 13)
A WATER PURIFICATION SYSTEM, METHOD OF MANUFACTURE THEREFOR AND METHOD OF PURIFYING WATER THEREWITH
HINDUSTAN LEVER LIMITED, a company incorporated under
the Indian Companies Act, 1913 and having its registered office at Hindustan Lever House, 165/166, Backbay Reclamation,
Mumbai -400 020, Maharashtra, India
The following specification describes the invention

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FIELD OF THE INVENTION
The invention relates to a water purification system, a method of purifying water using the system and a method of manufacture of the water purification system. The invention particularly relates to a water purification system for packing small quantities of solid
5 chlorine disinfectant which is stable for long period of time thereby ensuring that sufficient chlorine is available for killing of harmful micro-organisms in water to make it safe for human consumption.
BACKGROUND AND PRIOR ART
10 There are billions of people, especially in the underdeveloped and developing countries, especially in the rural areas who do not have purified water piped to their homes. Municipal water treatment systems are generally not available in these areas. They have to collect the water from sources like rivers, wells, lakes, streams and bore-wells in pots and store them in their homes for both cooking and drinking purposes. Such water is
15 often infected with harmful micro-organisms like cyst, virus and bacteria. The mortality and morbidity especially in infants and small children is high in these areas due to the consumption of such contaminated water. People are generally becoming aware that boiling of water makes the water microbiologically safe, but many people merely heat the water to about 60 to 70°C rather than boil for 20 minutes as recommended by the WHO.
20 Further boiling of water is expensive and requires availability of fuel like coal, kerosene or wood which are increasingly becoming scarce. Advanced home purification systems like UV (ultra-violet), RO (reverse-osmosis) etc require continuous flow of water and electricity which is also not available on a continuous basis in these areas. Thus, there has always been a need to provide a simple, easy to use, inexpensive and safe method to provide
2 5 the drinking water requirement for these people.
Halogen based disinfectants have traditionally been used to kill the micro-organisms in water. Such disinfectants include iodine, iodinated resins, chlorine compounds like calcium hypochlorite, sodium dichloro isocyanuric acid (NaDCCA), trichloroisocyanuric
30 acid (TCCA) etc. These disinfectants are very effective in killing micro-organisms but each one of them has their own inherent limitations and problems. The water from the above mentioned ground sources not only come contaminated with micro-organisms but

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also other contaminants like suspended dust and soil and dissolved impurities in trace amounts like organic impurities, dissolved salts, and pesticide residues. It is also important to remove these impurities in order to make the water fit for human consumption. In such situations a combination of flocculation and disinfections has been
5 suggested and used in the past.
W096/32194 (1996, Truetech) describes a water treatment composition in unit dose form e.g. a tablet capable of batch wise purification of water for drinking purposes comprising basically a disinfecting agent which is an organo chlorine compound, a coagulant-
10 precipitate agent, a primary and a secondary flocculent, a dispersion-buffer agent, an agglomeration matrix and pre-filter and a bulk ion-exchange absorbent. The present inventors have found that use of organo chlorine compound is effective in disinfection and the tablet has high stability in terms of available chlorine even when stored over long periods of time in hot and humid conditions. However, the organo chlorine componds
15 suffer from the drawback that after the chlorine is released from the compound when it is dissolved in water, the residual organic compound e.g cyanuric acid is harmful and has to be removed from the water. This necessitates the use of scavengers like activated carbon which can be cumbersome to use for the home user.
20 WO02/00557 (P&G) describes a water purification composition comprising essentially a primary coagulant, a bridging flocculent, a coagulant aid and optionally a disinfectant. This patent application also claims a method for clarifying and purifying water, which comprises several stages selected from coagulation and flocculation, disinfection, filtration, neutralisation and nutrifying.
25
EP0066421 (Buchan, 1982) describes a composition in unit dose form for a single step batch purification of relatively small amount of water using a combination of solid inorganic metal salt having trivalent cation, a solid water soluble alkali, a solid anionic polymeric hydrophilic colloid and optionally a bactericide.
30
Although both of the above publications, by P&G and by Buchan, are directed to purification of water using a combination of flocculation and disinfection (using inorganic chlorine based compounds), the disclosure therein are directed to compositions comprising a unit dose wherein the entire composition is mixed and packed for use by the

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consumer. The compositions disclosed in these two publications are better than the one by Truetech in one sense, in that inorganic chlorine compounds are used as disinfectants which are effective and has a residue which is harmless to consume unlike organic chlorine compounds. The present inventors have also been working on this area for a
5 long time and one problem they have faced is that inorganic chlorine compounds like calcium hypochlorite are very unstable especially in the presence of moisture. In a single dose formulation the other ingredients of the composition like clay etc are hygroscopic and tend to pick up moisture which leads to the instability of the chlorine compound, thereby reducing the amount of available chlorine by the time the consumer uses the
10 composition. The above publication by P&G talks of achieving optimum purification wherein the disinfecting agent is preferably used in controlled, delayed, sustained or slow release form. Means for providing such slow release include blending, or coating the chlorine compound with a poorly water soluble or hydrophobic material. The present inventors have found that these kinds of compositions require a long time of stirring of the
15 compositions with the water to be purified in order to achieve the desired dissolution and efficacy and it is desirable to provide for shorter stirring times to facilitate ease of operation for the consumer. Further, in the prior art, high amount of purification compositions are needed for achieving the desired quality of purified water.
20 The present inventors have worked diligently on solving this problem and developed a water purification system for ensuring that the purified water meets the desired standards for removal of unsafe micro organisms. The system involves inorganic chlorine compound having pre-selected properties and packed in a sachet. The amount of chlorine required in water for disinfection purposes has to be in a narrow window viz. 6 to
25 10 ppm by weight. If it is too low, the desired disinfection does not happen in the desired time of less than 5 minutes. If it is too high, high levels of quencher needs to be used in subsequent treatments which may alter the taste of water. Thus, the amount of inorganic chlorine compound like calcium hypochlorite to be packed in a sachet for use by a home consumer having a vessel of water of about 10 to 50 litres is of the order of 0.05 to 0.5
30 grams. It is very difficult to pack such low amounts of material especially corrosive material, like calcium hypochlorite in a sachet. This is especially so since the technology is meant for the mass market, where billions of such sachets will have to be manufactured at low cost, high reliability and high speed. The present inventors

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searched far and wide for a packaging technology to meet this requirement and could not find any. While some available technologies could not meet the stringent requirement of accurate weighment, others had problems with the flow properties of the chlorine compound used. The present inventors then set about solving this problem. They found
5 that if the calcium hypochlorite meet certain pre-specified properties, it is possible to pack the desired low amount in a sachet, meet the high accuracy of weighment, provide reliability in high speed packaging, all while ensuring that the storage stability of the packed chlorine compound is not compromised.
JP2002136975 (Anto KK) discloses a method of metering, handling and sterilizing small
10 amount of drinking water by adding calcium sulphate to calcium hypochlorite to increase the volume of calcium hypochlorite. The present inventors found this technology unsuitable since the stringent storage stability criterion of not more then 20% loss of available chlorine in the packed composition, could not be met.
It is thus an object of the present invention to provide for a water purification system that
15 enables packing of inorganic disinfectant like calcium hypochlorite in a sachet in small amount of 0.05 to 0.5 grams.
It is another object of the present invention to provide for a water purification system with a sachet containing 0.05 to 0.5 grams of calcium hypochlorite where loss of available chlorine is not more than 20% when stored at 40°C and 85% relative humidity for three
20 months.
It is yet another object of the present invention to provide for method to form and pack sachets containing 0.05 to 0.5 grams of calcium hypochlorite in a high speed machine at high reliability of weighment while not compromising on the storage stability of the calcium hypochlorite.
25 It is yet another object of the present invention to provide for a water purification system that ensures purification of raw water to meet the stringent WHO removal criteria of log 6 of bacteria, log 4 of virus and log 3 of cysts using the flocculation-disinfection means.

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SUMMARY OF THE INVENTION
According to one aspect of the present invention there is provided a water purification system comprising a sachet containing 0.05 to 0.5 grams of granules of calcium hypochlorite having 55 to 68% available chlorine, and up to 3% moisture, at least 80% of
5 said granules having particle size between 300 to 850 microns.
According to a preferred aspect of the invention, the water purification system comprises a sachet having two compartments, a first compartment containing 0.05 to 0.5 grams of granules of calcium hypochlorite having 55 to 68% available chlorine, and up to 3%
10 moisture, at least 80% of said granules having particle size between 300 to 850 microns and a second compartment containing a flocculating composition.
It is particularly preferred that the sachet of the water purification system of the invention is made of a laminate of a polymer and a metal.
15
According to another aspect of the invention there is provided a method of purifying water using the water purification system of the invention comprising the step of mixing the contents of the sachet with the water to be purified.
20 According to yet another aspect of the invention there is provided a method of forming and filling the sachet of the water purification system of the invention comprising the steps of
(a) forming a sachet by sealing the overlapping longitudinal and bottom edges of two
superimposed laminates;
25 (b) filling the sachet thus formed with said calcium hypochlorite granules from a cup of
predetermined volume; and
(c ) heat sealing the overlapping top edges.

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DETAILED DESCRIPTION OF THE INVENTION
All parts herein are by weight unless otherwise specified.
The first aspect of the invention provides for a water purification system comprising a
5 sachet containing very small amount of a selective disinfectant viz. calcium hypochlorite having very selective properties. The present inventors found that in order to meet the requirement of individual consumers and their families who have a requirement of potable water in pots or buckets of about 10 to 50 litres per day, it is required to provide very small amount of a chlorine compound for disinfection of the water in the order of 0.05 to
10 0.5 grams. The weight of the chlorine compound is different depending on the compound chosen, its molecular weight and its available chlorine, but is within this weight range.
The term 'available chlorine' is widely used in water purification industry. This term was originated for comparing the potential bleaching or oxidising or disinfecting power of
15 chlorine compounds. This is accomplished by a quantitative analysis of the chlorine that is available for oxidising, by a method known as iodometric method. The term 'available chlorine' is the calculated weight of chlorine molecule (Cl2) that is required to liberate the same amount of iodine molecule (l2). As only half of the chlorine molecule is of positive valence (+1 oxidation state), when in solution, the available chlorine content of any
20 chlorine compound that has CI+ (e.g., HOCI) will always be twice the amount of this cation present.
In summary, the term 'available chlorine* refers to the oxidising power of the compound tested. More information can be found in 'Handbook of chlorine and alternative
25 disinfectants', fourth edition, Geo. Clifford White, (John Wiley & sons Inc.)
Most chlorine disinfectants are very unstable especially in the presence of moisture and air and at high temperatures like 30 to 45°C which are prevalent in tropical countries. Calcium hypochlorite is a commonly used solid inorganic chlorine disinfectant. It is
30 generally available in two forms. The more common form has the formula Ca(OCI)CI and is commonly referred to as stabilised bleaching powder (SBP). Commercially available bleaching powder generally has available chlorine in amounts in the range of 30 to 35 wt%. SBP is generally available in fine powder form and at low moisture content of

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less than 1 wt%. The other form of calcium hypochlorite is called high-strength hypochlorite and has the chemical formula Ca(OCI)2. This can be commercially procured at available chlorine in the range of 60 to 65 wt%. Commercial High strength hypochlorite is generally available at a moisture content in the range of 5 to 10 wt%.
5
When the present inventors set about finding a solution to the present problem of providing a water purification system that can disinfect the water for individual consumers and their families in the rural areas, they realised that the disinfectant to be packed will have to be in very small amounts of less than 0.5 grams and very often as less as 0.1
10 gram. They found that packing technologies of such small amounts of materials is not very accurate and reliable especially for corrosive materials like chlorine compounds. They tried adding various fillers that will increase the weight of the material to be packed. They also worked at various processing conditions, tableting options and by using various disinfectant, each one of them of various properties. They found that there were many
15 conditions that had to be met so that the product would meet all the requirements of the consumer. The product must be packed such that it is stable to enable sufficient amount of chlorine to ensure disinfection, at the same time available chlorine should not be so high that it makes the water difficult to consume. With most of the options tried, the inventors encountered many different problems like accuracy in weighment, choking and
20 lack of reliability in filling of the sachet due to flow problems of the powder/ granules, poor stability of the chlorine compound packed, slow dissolution of the granule/powder among a host of other problems. The present inventors found that only when calcium hypochlorite which met the highly selective properties of having a moisture content of less than 3% and available chlorine of 55 to 68 wt%, a particle size such that more than 80%
25 is in the size range of 300 to 850 microns, was it possible to pack it in a sachet in amounts in the range of 0.05 to 0.5 grams and yet meet all of the above contrasting requirements described above. If any of these properties were not met, one or more of the problems occurred and it was not possible to meet the objects of the invention.
30 It is preferred that at least 90% of the granules, more preferably at least 95% of granules of calcium hypochlorite are in the size range of 300 to 850 microns, said granules having less than 3% moisture and 55 to 68% available chlorine. It is preferred that the calcium hypochlorite has available chlorine in the range of 60 to 68 wt%, more preferably 60 to 65

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wt%. As per the water purification system of the invention, the sachet preferably contains 0.1 to 0.25 grams of calcium hypochlorite granules. Calcium hypochlorite having the chemical formula Ca(OCI)2 is especially preferred. It is preferred that the sachet additionally contains 2 to 10% calcium oxide with respect to weight of the calcium
5 hypochlorite granules. It has been found that such compositions comprising calcium oxide provide further enhanced stability.
The packaging material is also important in achieving optimum stability and other desired properties of the disinfectant packed. The packaging material is preferably a laminate
10 comprising a layer of aluminium and a layer of polyethylene. The polyethylene layer is generally in contact with the calcium hypochlorite granules. The aluminium layer is on the outside of the polyethylene layer. The aluminium layer may optionally be further layered with other one or more polymeric layers. Suitable polymer is polyethylene terephthalate (PET). The inner polyethylene layer is preferably at a layer thickness in the range of 30 to
15 100 microns, more preferably in the range of 35 to 75 microns. The thickness of the aluminium layer is preferably in the range of 5 to 15 microns, more preferably in the range of 8 to 12 microns.
The granules of calcium hypochlorite in the water purification system are so present that
20 when stirred in water to be purified it dissolves in less than one minute. Using the water purification system of the invention the available chlorine in said granules reduces by less than 20%, more preferably less than 10 %, when the sachet stored for three months at 40 °C and 85% relative humidity.
25 A preferred aspect of the invention provides for a water purification system wherein the sachet contains two compartments, a first compartment containing the calcium hypochlorite granules and a second compartment containing a flocculating composition. When the sachet comprises two compartments, it is especially preferred that the external surface area of said first compartment is less than the external surface area of said
30 second compartment.
The flocculating composition present in the second compartment preferably comprises a coagulating agent, which is a water soluble salt of a trivalent inorganic metal; a

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flocculating agent, which is a high molecular weight water soluble polymer; and an adsorbent clay.
The coagulating agent is a compound which is a water-soluble inorganic metal salt having
5 trivalent cation. Suitable trivalent cations are Al3+ and Fe3+. The coagulant is generally free from carbon atoms. Examples of coagulating agents are ferric sulfate, aluminium sulfate and polyaluminium chloride. Without being limited by theory, it is believed that these coagulating agents when added to water form gelatinous hydroxide compounds at pH greater than or equal to 6. The mechanism of coagulation via the formation of
10 gelatinous hydroxide is optimum when pH is adjusted between 6 and 8.5. The gelatinous precipitate entrains fine suspended particles and microbes as it settles or coagulates. The coagulating agent is preferably present in an amount in the range of from 5 to 50%, more preferably from 15 to 40% by weight of the flocculating composition.
15 The flocculating agent in the flocculating composition of this invention is a compound which is a high molecular weight water soluble polymer. Examples of flocculating agents are polysaccharides (dextane celluloses), proteins, modified celluloses (hydroxyethyl/hydroxypropyl or carboxymethyl), and polyacrylamides preferably high molecular weight polyacrylamide. It is especially preferred that the polyacrylamide is
20 either anionic or non-ionically modified, more preferably anionically modified. Suitable molecular weights of these polyacrylamides are in the range of 10s to 107. Preferred flocculating agent is Superfloc (from Cytec). Preferred amounts of the flocculating agent is from 0.5 to 15%, more preferably from 1 to 10% and most preferably from 2 to 8% by weight of the flocculating composition.
25
The adsorbent clay in the flocculating composition are those clays which are capable of adsorbing high levels of water and organic or inorganic compounds. Examples of clay which may be included are Montmorillonite clay (dioctheydral smectite clay), Laponite, Hectorite, Nontronite, Saponite, Volkonsite, Sauconite, Beidellite, Allevarlite, lllite,
30 Halloysite, Attapulgite, Mordenite, Kaolines, and Bentonite. A highly preferred clay as per this invention is Bentonite clay. When included, the adsorbent clay is present in an

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amount in the range of 5 to 75%, more preferably from about 10 to 60% by weight of the flocculating composition.
The flocculating composition preferably comprises a quencher which is capable of
5 reacting with chlorine thereby making the water suitable for human consumption. Suitable quenchers are sodium thiosulphate or ascorbic acid. The quencher is preferably present in an amount in the range of 1 to 20%, more preferably from about 2 to 12% by weight of the flocculating composition.
10 Another optional ingredient which may be present in the flocculating composition is a buffering agent capable of maintaining the pH in the range of 6 to 8.5 when the flocculating composition is dissolved/dispersed in water. Suitable buffering agents are calcium oxide, sodium carbonate or sodium bicarbonate. The buffering agent, when present, is included in an amount in the range of 0.5 to 10% by weight of the flocculating
15 composition.
The flocculating composition is preferably present in the second compartment of the sachet in amounts in the range of 0.5 to 10 grams more preferably in the range of 1 to 5 grams.
20
According to another aspect of the present invention there is provided a method of purifying water using the water purification system of the invention comprising the step of mixing the contents of the sachet with the water to be purified.
25 When the sachet is configured with two compartments the preferred method of purifying water comprises the steps of (i)mixing the contents of said first compartment with impure water, followed by; (ii)mixing the contents of said second compartment, to form floes therein; and (iii)separating said floes from said impure water to get purified water.
30 The contents of the first compartment are usually mixed for a period of time from 0.5 to 5 minutes and the water is then allowed to stand for a time period of 2 to 10 mins, after which the contents of the second compartment are added. The mixture is then mixed for

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a period of time from 0.5 to 5 minutes and again allowed to stand for 2 to 10 mins. The flocculated mass is then allowed to settle down and then separated from the mixture usually by filtration or decantation. A simple cloth may be used for filtration.
5 A batch of 10 to 50 litres of water can be purified using the water purification system of the invention. The inventive method of purification of water ensures 6-log removal of bacteria (examples 2-4), 4-log removal of viruses (examples 5 and 6) and 3-log removal of cysts (example - 7).
10 A preferred method of forming and filling the sachet comprising the steps of
(a) forming a sachet by sealing the overlapping longitudinal and bottom edges of two
superimposed laminates;
(b) providing a seal across a longitudinal section of the sachet to form two
15 compartments;
(c) filling said first compartment of the sachet with said calcium hypochlorite granules
from a cup of predetermined volume and said second compartment of the sachet
with the flocculating composition; and
(d) sealing the overlapping top edges.
20
According to yet another aspect of the invention there is provided granules of calcium hypochlorite having 55 to 68% available chlorine, and up to 3% moisture, at least 80% of said granules having particle size between 300 to 850 microns for use in packing in a sachet in an amount in the range of 0.05 to 0.5 grams.
25
The invention will now be illustrated by the following non-limiting examples.
EXAMPLES
Example 1 and Comparative Example - A to D
Example -1
30 A sample of calcium hypochlorite having chemical formula Ca(OCI)2 having 60% available chlorine was dried to about 2.8% moisture. The sample was sieved to a particle size such that about 95% of the particles were between 300 to 800 microns. A form fill seal

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packing machine was used to pack the sample in a sachet made of a laminate having polyethylene as the inner layer, polyethylene terephthalate as the outer layer and aluminium layer in between the two. The machine was run for about an hour with out any problem and about ten sachets were sampled at random and the weight of the calcium
5 hypochlorite granules in them were determined. The sachets were sought to be filled with an average target weight of 0.155 grams. The data on the weight variation is shown in Table -1
Comparative Example - A
Sachets as per Example-1 were manufactured except that the calcium hypochlorite had a
10 particle size such that 90% of the particle size were in the range of 500 to 2000 microns, 70 % was in the size range of 300 to 800 microns and 10% was in the size range of 150 to 500 microns. The data on weight variation from ten such randomly chosen sachets is summarized in Table -1.
Table-1

Example -1 Comp. Ex - A
Average weight, grams 0.155 0.165
Range in weight, grams 0.150 to 0.158 0.151 to 0.180
Standard deviation, grams 0.003 0.011
15
The data in Table- 1 indicates that very high control on the amount of calcium hypochlorite packed in a sachet can be achieved by using the calcium hypochlorite which meets the properties as per the invention (Example - 1) while the control is poor in the example outside the invention (Comparative Example - A).
20 Comparative Example - B
Sachets were packed as per Example - 1 except that the initial moisture of the calcium hypochlorite was about 5.9%. These sachets were stored in a hot and humid chamber (85% relative humidity and 40 °C) for several weeks. Samples were withdrawn every few weeks. The contents of the sachets were dissolved in 10 litres of water by stirring for one
25 minute. The available chlorine in 10 litres of water was measured. An average of two such measurements is summarized in Table - 2.

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Example-1
Similar storage studies were conducted with samples prepared as per Example -1. The data on available chlorine as an average of two measurements is summarized in Table -2. Available chlorine of more than 6 ppm in the water to be purified is considered
5 acceptable after storage under these hot and humid conditions for three months.
Table-2

Example-1: Initial moisture = 2.94% Comp Ex - B: Initial moisture = 5.87%
Week Available Chlorine (ppm) Week Available Chlorine (ppm)
0 10.2 0 10.0
12 8.2 5 3.9
The data in Table- 2 indicates that calcium hypochlorite having properties outside the invention (Comparative Example - B) is unstable in less than 5 weeks of storage while
10 sample as per the invention (Example-1) meets the desired stability criteria.
Comparative Example -C and D: Calcium hypochlorite with available chlorine and particle size outside the inventive range
Comparative Example -C: A sample of calcium hypochlorite having chemical formula
15 Ca(OCI)CI having about 30% available chlorine and a moisture content of 1 % available commercially as stabilised bleaching powder, was used to fill sachets of 0.15 grams in a form-fill-seal packing machine. The particle size of the calcium hypochlorite was such that 90% of the particles were less than 250 microns in size. The observation during packing is summarized in Table -3.
20
Comparative Example - D: A sample as per Comparative Example -C was granulated to a particle size such that 90% of the particles were in the size range of 500 to 1500 microns. The observation on using sachets packed with this sample when dissolved in 10 litres of water is summarized in Table - 3.
25

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Table-3

ComparativeExample Observation
C The filling operation was difficult. The calcium hypochlorite particles stuck to the machine parts, the flow of the particles was poor and desired uniformity in filling could not be achieved.
D Does not dissolve fully in water even after stirring for five minutes.
The data in Table- 3 indicates that it is very difficult to sachet pack low amount of calcium hypochlorite having properties outside the selective range in terms of %available chlorine
5 and particle size.
Examples 2 to 7: Microbiological efficacy of system of the invention
Sachets as per Example - 1 were prepared. Test water with various levels of bacteria, polio virus and cyst were prepared and purified using the contents of the sachets. The amount of log removal of the various micro-organisms was measured. Methods to
10 measure micro-organisms/ surrogates are using the method described in detail in the publication "Tropical Medicine and International Health, volume 11 no 9 pp 1399-1405 September '2006, in article titled '"Microbiological performance of a water treatment unit designed for household use in developing countries", by Thomas Clasen, Suresh Nadakatti and Shashikala Menon.
15
The data is summarized in Table - 4.
Table - 4

Microbes Example Input Cone. Output Cone. Log reduction
Bacteria (E-Coif) 2 2x108/100mL <10 8.30
3 2x106/100mL <10 6.30
4 7x106/100mL <10 6.80
Polio Virus (Sabintype 1) 5 10425pfu/50µL <10 4.25
6 10410pfu/100µl_ <10 4.10
Cyst(irradiated) 7 5x104/L 50/L 3.00

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The data in Table - 4 indicates that water of very high microbiological purity meeting the log 6 reduction for bacteria, log 4 reduction for virus and log 3 reduction for cyst can be attained using the system of the present invention.
5 Example 8 and 9: Effect of inclusion of Calcium oxide:
Example-8:
A sample similar to Example - 1 was prepared except that the amount of moisture at point of packing was 2.32%.
Example - 9:
10 A sample similar to Example - 8 was prepared except that calcium oxide at 5 wt% of calcium hypochlorite included in the sachets.
In Example 8 and 9 the target weight was 0.17 grams. The sachets were made from a laminate having 70 micron polyethylene on the inside, overlayed by 12 micron of poly ethylene terephthalate (PET), overlayed by 9 micron of aluminium, overlayed by 12
15 micron of PET. The sachet samples were stored at HH condition (40 °C and 85% humidity) for several weeks. The samples were withdrawn every few weeks and contents of a sachet dissolved in 10 litres of water. The available chlorine in the 10 litre water was measured. The data is summarized in Table - 5.
Table - 5

20

The data in Table - 5 indicates that sample as per the invention (Example -8) meets the desired storage stability criterion of available chlorine greater than 6 ppm on storage at HH condition for 12 weeks. Inclusion of calcium oxide gives enhanced stability of more than 40 weeks of storage at HH condition.

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Examples 10 to 19 :
Two compartment sachets were manufactured in a form-fill-seal packing machine. The first compartment was packed with 0.15 grams of calcium hypochlorite granules of the invention and the second compartment was packed with 1.85 grams of a flocculating
5 composition as shown in Table - 6 below.
Table-6

First compartment Wt, grams
Calcium hypochlorite* 0.15
Second compartment Wt, grams
Poly aluminium chloride 0.40
Poly acrylamide 0.08
Bentonite clay 1.25
Anhydrous Sodium thiosulphate 0.10
Calcium oxide 0.03
* Calcium hypochlorite granules as per the invention was used.
About 3000 such sachets were prepared with out any stoppage of the packing machine. About ten randomly selected samples were used for purifying water having a turbidity of
10 about 80-90 NTU. The method used to purify water is given below:
Method of purifying water:
A test water having the indicated amount of turbidity was prepared. Contents of the first compartment were added to 10 litres of test water and stirred for one minute and allowed
15 to stay for five minutes. The contents of the second compartment was then added and stirred for one minute and allowed to stay for five minutes. The water was then filtered through a coarse clean cloth. The chlorine content of the water before addition of the contents of the second compartment and after filtration was determined. The turbidity of the water before addition of the contents of the first compartment and after filtration was
20 also measured. A turbidity value less than 1 NTU is generally considered acceptable. The data is summarized in Table - 7.

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Table-7

Ex. After addition of contents offirst compartment After addition of contents of second compartment Residualchlorinequenched?
% Moisture AvailableChlorine intreated water Turbidity, NTU**
Test Water Treated Water
10 2.04 8.15 81 0.69 Yes
11 1.92 8.72 81 0.50 Yes
12 1.71 8.33 81 0.8 Yes
13 1.52 8.54 81 0.85 Yes
14 1.76' 8.36 81 0.94 Yes
15 3.01 8.93 81 0.82 Yes
16 1.75 8.10 81 0.76 Yes
17 1.35 8.21 87 0.80 Yes
18 2.03. 8.57 87 0.93 Yes
19 2.28 8.82 87 0.99 Yes
The data in Table- 7 indicates that highly pure water can be prepared in a very consistent manner in a high speed packing machine using a two compartment sachet with the first
5 compartment packed with calcium hypochlorite in very small amounts and the second compartment packed with a flocculating composition.
Comparative Example E and F: Effect of type of packing material:
Comparative Example - E:
10 Calcium hypochlorite granules as used in Example - 1 were packed in sachet made of a laminate of low density polyethylene (LDPE) on the inside overlayed by a layer of high density poly ethylene (HDPE).
Comparative Example - F:
15 Calcium hypochlorite granules as used in Example - 1 were packed in sachet made of a laminate of polypropylene (PP) on the inside overlayed by a layer of high density poly ethylene (HDPE).

C2154(V)
- 18 -
Sachets of Comparative Example E and F and those from Example - 1 were stored in a chamber maintained at 40 °C and 85% humidity. The samples were checked to see if it could meet the criterion of available chlorine of at least 6 ppm when the granules were dissolved in 10 litres of water after 12 weeks of such storage. The results are
5 summarised in Table - 8.
Table-8

Examples Stability
Example -1 Comp Ex -E Yes No
Comp Ex - F No
The invention thus provides for a water purification system that enables packing of
10 calcium hypochlorite in a sachet in small amount of 0.05 to 0.5 grams which is stable to ensure sufficient available chlorine till used by the consumer to purify drinking water. The invention ensures high reliability of weighment of such small amounts. The flocculation-disinfection system of the invention is able to meet the stringent WHO criteria of log 6 removal of bacteria, log 4 removal of virus and log 3 removal of cysts from impure water.
15
Dated this 28th day of March 2007.
HINDUSTAN LEVER LIMITED
20

Documents

Orders

Section Controller Decision Date

Application Documents

# Name Date
1 570-mum-2007-abstract(25-3-2008).pdf 2018-08-09
1 570-MUM-2007-FORM 26(09-11-2009).pdf 2009-11-09
2 570-MUM-2007-ABSTRACT(GRANTED)-(27-6-2014).pdf 2018-08-09
2 570-MUM-2007-CORRESPONDENCE(09-11-2009).pdf 2009-11-09
3 570-MUM-2007-FORM 3(12-08-2011).pdf 2011-08-12
3 570-MUM-2007-ANNEXURE TO FORM 3(11-7-2012).pdf 2018-08-09
4 570-MUM-2007-FORM 3(10-12-2013).pdf 2013-12-10
4 570-MUM-2007-CHINA DOCUMENT(11-7-2012).pdf 2018-08-09
5 570-MUM-2007_EXAMREPORT.pdf 2018-08-09
5 570-mum-2007-claims(25-3-2008).pdf 2018-08-09
6 570-MUM-2007-REPLY TO HEARING(6-6-2013).pdf 2018-08-09
6 570-MUM-2007-CLAIMS(3-11-2009).pdf 2018-08-09
7 570-MUM-2007-REPLY TO HEARING(5-6-2013).pdf 2018-08-09
7 570-MUM-2007-CLAIMS(AMENDED)-(11-7-2012).pdf 2018-08-09
8 570-MUM-2007-REPLY TO EXAMINATION REPORT(17-8-2012).pdf 2018-08-09
8 570-MUM-2007-CLAIMS(AMENDED)-(16-3-2012).pdf 2018-08-09
9 570-MUM-2007-CLAIMS(AMENDED)-(17-8-2012).pdf 2018-08-09
9 570-MUM-2007-REPLY TO EXAMINATION REPORT(16-3-2012).pdf 2018-08-09
10 570-MUM-2007-CLAIMS(GRANTED)-(27-6-2014).pdf 2018-08-09
10 570-MUM-2007-REPLY TO EXAMINATION REPORT(11-7-2012).pdf 2018-08-09
11 570-MUM-2007-CLAIMS(MARKED COPY)-(11-7-2012).pdf 2018-08-09
11 570-MUM-2007-PETITION UNDER RULE-137(16-3-2012).pdf 2018-08-09
12 570-MUM-2007-CLAIMS(MARKED COPY)-(16-3-2012).pdf 2018-08-09
12 570-MUM-2007-PCT-IPEA-416(3-11-2009).pdf 2018-08-09
13 570-MUM-2007-CLAIMS(MARKED COPY)-(17-8-2012).pdf 2018-08-09
13 570-MUM-2007-OTHER DOCUMENT(6-6-2013).pdf 2018-08-09
14 570-mum-2007-correspondence 1(24-9-2007).pdf 2018-08-09
14 570-MUM-2007-OTHER DOCUMENT(11-7-2012).pdf 2018-08-09
15 570-mum-2007-correspondence 2(24-3-2007).pdf 2018-08-09
15 570-MUM-2007-MEXICAN DOCUMENT(11-7-2012).pdf 2018-08-09
16 570-mum-2007-correspondence 3(28-3-2007).pdf 2018-08-09
16 570-MUM-2007-GENERAL POWER OF ATTORNEY(19-2-2014).pdf 2018-08-09
17 570-mum-2007-form-3.pdf 2018-08-09
17 570-mum-2007-correspondence 4(24-9-2007).pdf 2018-08-09
18 570-MUM-2007-CORRESPONDENCE(10-2-2010).pdf 2018-08-09
18 570-mum-2007-form-2.pdf 2018-08-09
19 570-MUM-2007-CORRESPONDENCE(10-6-2013).pdf 2018-08-09
20 570-MUM-2007-CORRESPONDENCE(15-7-2013).pdf 2018-08-09
20 570-mum-2007-form-1.pdf 2018-08-09
21 570-MUM-2007-CORRESPONDENCE(18-6-2009).pdf 2018-08-09
21 570-mum-2007-form 5(25-3-2008).pdf 2018-08-09
22 570-MUM-2007-CORRESPONDENCE(19-2-2014).pdf 2018-08-09
22 570-MUM-2007-FORM 3(8-8-2012).pdf 2018-08-09
23 570-MUM-2007-CORRESPONDENCE(20-9-2012).pdf 2018-08-09
23 570-MUM-2007-FORM 3(4-8-2010).pdf 2018-08-09
24 570-mum-2007-form 3(28-3-2007).pdf 2018-08-09
24 570-mum-2007-correspondence(25-3-2008).pdf 2018-08-09
25 570-mum-2007-form 3(25-3-2008).pdf 2018-08-09
25 570-MUM-2007-CORRESPONDENCE(27-8-2010).pdf 2018-08-09
26 570-MUM-2007-CORRESPONDENCE(3-11-2009).pdf 2018-08-09
26 570-MUM-2007-FORM 3(24-2-2010).pdf 2018-08-09
27 570-MUM-2007-CORRESPONDENCE(IPO)-(27-6-2014).pdf 2018-08-09
27 570-MUM-2007-FORM 3(23-1-2013).pdf 2018-08-09
28 570-mum-2007-correspondence-received.pdf 2018-08-09
28 570-MUM-2007-FORM 3(22-6-2013).pdf 2018-08-09
29 570-mum-2007-description (complete).pdf 2018-08-09
29 570-MUM-2007-FORM 3(21-5-2014).pdf 2018-08-09
30 570-mum-2007-description(complete)-(25-3-2008).pdf 2018-08-09
30 570-MUM-2007-FORM 3(15-2-2012).pdf 2018-08-09
31 570-MUM-2007-DESCRIPTION(GRANTED)-(27-6-2014).pdf 2018-08-09
31 570-MUM-2007-FORM 3(15-2-2011).pdf 2018-08-09
32 570-mum-2007-description(provisional)-(28-3-2007).pdf 2018-08-09
32 570-mum-2007-form 2(title page)-(provisional)-(28-3-2007).pdf 2018-08-09
33 570-MUM-2007-EP DOCUMENT(11-7-2012).pdf 2018-08-09
33 570-MUM-2007-FORM 2(TITLE PAGE)-(GRANTED)-(27-6-2014).pdf 2018-08-09
34 570-MUM-2007-EP DOCUMENT(16-3-2012).pdf 2018-08-09
34 570-mum-2007-form 2(title page)-(complete)-(25-3-2008).pdf 2018-08-09
35 570-mum-2007-form 13(3-10-2007).pdf 2018-08-09
35 570-MUM-2007-FORM 2(GRANTED)-(27-6-2014).pdf 2018-08-09
36 570-mum-2007-form 2(complete)-(25-3-2008).pdf 2018-08-09
36 570-MUM-2007-FORM 13(8-2-2012).pdf 2018-08-09
37 570-MUM-2007-FORM 18(18-6-2009).pdf 2018-08-09
38 570-MUM-2007-FORM 13(8-2-2012).pdf 2018-08-09
38 570-mum-2007-form 2(complete)-(25-3-2008).pdf 2018-08-09
39 570-mum-2007-form 13(3-10-2007).pdf 2018-08-09
39 570-MUM-2007-FORM 2(GRANTED)-(27-6-2014).pdf 2018-08-09
40 570-MUM-2007-EP DOCUMENT(16-3-2012).pdf 2018-08-09
40 570-mum-2007-form 2(title page)-(complete)-(25-3-2008).pdf 2018-08-09
41 570-MUM-2007-EP DOCUMENT(11-7-2012).pdf 2018-08-09
41 570-MUM-2007-FORM 2(TITLE PAGE)-(GRANTED)-(27-6-2014).pdf 2018-08-09
42 570-mum-2007-form 2(title page)-(provisional)-(28-3-2007).pdf 2018-08-09
42 570-mum-2007-description(provisional)-(28-3-2007).pdf 2018-08-09
43 570-MUM-2007-DESCRIPTION(GRANTED)-(27-6-2014).pdf 2018-08-09
43 570-MUM-2007-FORM 3(15-2-2011).pdf 2018-08-09
44 570-mum-2007-description(complete)-(25-3-2008).pdf 2018-08-09
44 570-MUM-2007-FORM 3(15-2-2012).pdf 2018-08-09
45 570-mum-2007-description (complete).pdf 2018-08-09
45 570-MUM-2007-FORM 3(21-5-2014).pdf 2018-08-09
46 570-MUM-2007-FORM 3(22-6-2013).pdf 2018-08-09
46 570-mum-2007-correspondence-received.pdf 2018-08-09
47 570-MUM-2007-CORRESPONDENCE(IPO)-(27-6-2014).pdf 2018-08-09
47 570-MUM-2007-FORM 3(23-1-2013).pdf 2018-08-09
48 570-MUM-2007-CORRESPONDENCE(3-11-2009).pdf 2018-08-09
48 570-MUM-2007-FORM 3(24-2-2010).pdf 2018-08-09
49 570-MUM-2007-CORRESPONDENCE(27-8-2010).pdf 2018-08-09
49 570-mum-2007-form 3(25-3-2008).pdf 2018-08-09
50 570-mum-2007-correspondence(25-3-2008).pdf 2018-08-09
50 570-mum-2007-form 3(28-3-2007).pdf 2018-08-09
51 570-MUM-2007-CORRESPONDENCE(20-9-2012).pdf 2018-08-09
51 570-MUM-2007-FORM 3(4-8-2010).pdf 2018-08-09
52 570-MUM-2007-CORRESPONDENCE(19-2-2014).pdf 2018-08-09
52 570-MUM-2007-FORM 3(8-8-2012).pdf 2018-08-09
53 570-MUM-2007-CORRESPONDENCE(18-6-2009).pdf 2018-08-09
53 570-mum-2007-form 5(25-3-2008).pdf 2018-08-09
54 570-MUM-2007-CORRESPONDENCE(15-7-2013).pdf 2018-08-09
54 570-mum-2007-form-1.pdf 2018-08-09
55 570-MUM-2007-CORRESPONDENCE(10-6-2013).pdf 2018-08-09
56 570-MUM-2007-CORRESPONDENCE(10-2-2010).pdf 2018-08-09
56 570-mum-2007-form-2.pdf 2018-08-09
57 570-mum-2007-correspondence 4(24-9-2007).pdf 2018-08-09
57 570-mum-2007-form-3.pdf 2018-08-09
58 570-MUM-2007-GENERAL POWER OF ATTORNEY(19-2-2014).pdf 2018-08-09
58 570-mum-2007-correspondence 3(28-3-2007).pdf 2018-08-09
59 570-MUM-2007-MEXICAN DOCUMENT(11-7-2012).pdf 2018-08-09
59 570-mum-2007-correspondence 2(24-3-2007).pdf 2018-08-09
60 570-mum-2007-correspondence 1(24-9-2007).pdf 2018-08-09
60 570-MUM-2007-OTHER DOCUMENT(11-7-2012).pdf 2018-08-09
61 570-MUM-2007-CLAIMS(MARKED COPY)-(17-8-2012).pdf 2018-08-09
61 570-MUM-2007-OTHER DOCUMENT(6-6-2013).pdf 2018-08-09
62 570-MUM-2007-CLAIMS(MARKED COPY)-(16-3-2012).pdf 2018-08-09
62 570-MUM-2007-PCT-IPEA-416(3-11-2009).pdf 2018-08-09
63 570-MUM-2007-CLAIMS(MARKED COPY)-(11-7-2012).pdf 2018-08-09
63 570-MUM-2007-PETITION UNDER RULE-137(16-3-2012).pdf 2018-08-09
64 570-MUM-2007-CLAIMS(GRANTED)-(27-6-2014).pdf 2018-08-09
64 570-MUM-2007-REPLY TO EXAMINATION REPORT(11-7-2012).pdf 2018-08-09
65 570-MUM-2007-CLAIMS(AMENDED)-(17-8-2012).pdf 2018-08-09
65 570-MUM-2007-REPLY TO EXAMINATION REPORT(16-3-2012).pdf 2018-08-09
66 570-MUM-2007-CLAIMS(AMENDED)-(16-3-2012).pdf 2018-08-09
66 570-MUM-2007-REPLY TO EXAMINATION REPORT(17-8-2012).pdf 2018-08-09
67 570-MUM-2007-REPLY TO HEARING(5-6-2013).pdf 2018-08-09
67 570-MUM-2007-CLAIMS(AMENDED)-(11-7-2012).pdf 2018-08-09
68 570-MUM-2007-REPLY TO HEARING(6-6-2013).pdf 2018-08-09
68 570-MUM-2007-CLAIMS(3-11-2009).pdf 2018-08-09
69 570-MUM-2007_EXAMREPORT.pdf 2018-08-09
69 570-mum-2007-claims(25-3-2008).pdf 2018-08-09
70 570-MUM-2007-CHINA DOCUMENT(11-7-2012).pdf 2018-08-09
70 570-MUM-2007-FORM 3(10-12-2013).pdf 2013-12-10
71 570-MUM-2007-ANNEXURE TO FORM 3(11-7-2012).pdf 2018-08-09
71 570-MUM-2007-FORM 3(12-08-2011).pdf 2011-08-12
72 570-MUM-2007-ABSTRACT(GRANTED)-(27-6-2014).pdf 2018-08-09
72 570-MUM-2007-CORRESPONDENCE(09-11-2009).pdf 2009-11-09
73 570-mum-2007-abstract(25-3-2008).pdf 2018-08-09
73 570-MUM-2007-FORM 26(09-11-2009).pdf 2009-11-09

ERegister / Renewals

3rd: 22 Aug 2014

From 28/03/2009 - To 28/03/2010

4th: 22 Aug 2014

From 28/03/2010 - To 28/03/2011

5th: 22 Aug 2014

From 28/03/2011 - To 28/03/2012

6th: 22 Aug 2014

From 28/03/2012 - To 28/03/2013

7th: 22 Aug 2014

From 28/03/2013 - To 28/03/2014

8th: 22 Aug 2014

From 28/03/2014 - To 28/03/2015

9th: 27 Feb 2015

From 28/03/2015 - To 28/03/2016

10th: 26 Feb 2016

From 28/03/2016 - To 28/03/2017

11th: 23 Feb 2017

From 28/03/2017 - To 28/03/2018