Abstract: This invention relates to an improved granular formulation of herbicide glyphosate in form of ammonium salt using environmentally friendly adjuvtants, and a process for preparation thereof. The formulation minimizes the use of some inactive ingredients without compromising the effectiveness of the product.
FORM 2
THE PATENTS ACT 1970
(39 of 1970)
&
The Patents Rules, 2003
COMPLETE SPECIFICATION
(See Section 10; Rule 13)
1. TITLE OF THE INVENTION: Improved Herbicidal Formulation
2. APPLICANT(S)
(a) NAME: Excel Crop Care Limited & C. C. Shroff Researach Institute
(b) NATIONALITY: An Indian Company
(c) ADDRESS:
Excel crop Care Ltd. C. C. Shroff Researach Institute
184-87, Swami Vivekanand Road, Rom House , 2nd Floor,
Jogeshwari (West), Gaiwadi Industrial Estate
Mumbai 400 102, Goregaon (west)
Maharashtra, India. Mumbai –400 062
3. PREAMBLE TO THE DESCRIPTION:
The following COMPLETE specification particularly describes the nature of this invention and the manner in which it is to be performed.
Improved Herbicidal Formulation
FIELD OF INVENTION
This invention relates to a granular formulation comprising ammonium salt of N-phosphonomethylglycine i.e., glyphosate, a process for manufacturing the same and use of said formulation for controlling weeds.
BACKGROUND AND PRIOR ART
N-(phosphonomethyl)glycine is a broad spectrum systemic non-selective herbicide generically known as Glyphosate. It is effective for control of annual and perennial plants including grasses, sedges, broad-leaved weeds and woody plants.
Glyphosate is commonly used in salt form such as isopropylamine salt, trimethylsulfonium salt, ammonium salt etc. However, the difference in efficacy of various brands is more likely to be due to the adjuvants used in the formulation and tank-mix rather than the type of salt itself. Many adjuvants are available to improve spreading, deposition and rain-fastness of glyphosate formulation.
The effectiveness of a formulation as well as its suitability from environmental point of view, both are important. Among the available adjuvants, those which are safe to the environment are preferable.
Ammonium sulfate is added to glyphosate formulations in order to improve its performance under stressful conditions, especially when hard water is used to prepare spray solution.
Various types of formulations of Glyphosate are commercially available such as suspension concentrate, water soluble or dispersible granules etc. The granular form is more popular and preferred over other forms.
Numerous compositions and processes have been disclosed in the literature for preparation of granular formulation of ammonium glyphosate using various adjuvants. These include patents/applications viz. WO9007275, EP252897, WO2007112933, WO2006133788, JP2005112836, US2004102323, US5858921, WO9800022, EP0378985 and EP0582561. Tallow amine surfactants are most commonly used in these glyphosate formulations. European patent EP0378985 discloses a granular formulation of glyphosate salt in which the most preferred surfactant is an ethoxylated tallow amine containing 15-18 moles of ethylene oxide. WO2006133788 describes a process for preparing water-soluble ammonic glyphosate granules in which tallow amine surfactant is preferably used.
Though glyphosate itself is practically non-toxic to fish, the toxicity is due to tallow amine surfactant used in the formulation. Therefore such formulations are not suitable for use in or close to aquatic environment. Tallow amine surfactants are also irritants to eyes 8B skin. Therefore it is preferable to have a glyphosate formulation in which non-tallow amine surfactants are used.
US6248695 discloses herbicidal composition comprising glyphosate or its salt and an alkyldiamine tetraalkoxylate surfactant. It also claims the use of alkyl glycoside or alkyl polyglycoside surfactants along with alkyldiamine tetraalkoxylate in glyphosate or its salt containing composition. However, in the said patent, the surfactant requirement is as high as 21-22wt%. In the formulation described in said patent, alkyl
glycoside or alkyl polyglycoside is not used without using alkyldiamine tetraalkoxylate simultaneously. Moreover, in the said patent, the formulation of isopropylamine salt of glyphosate is in liquid form when alkyl glycoside is used.
The use of alkyl glycoside or alkyl polyglycoside surfactants in granular formulation of ammonium salt of glyphosate is not known in the art.
OBJECTS OF INVENTION
The main object of this invention is to provide a cost-effective granular formulation of glyphosate without using tallow amine surfactant.
Another object of invention is to provide a formulation of ammonium glyphosate in granular form using alkyldiamine alkoxylate and alkyl glycoside or alkyl polyglycoside surfactants.
Another object of invention is to provide an environmentally safer formulation of glyphosate.
Another object of invention is to minimize the use of inactive ingredients without compromising the effectiveness of the product.
Another object of the invention is to provide a process for preparation of granular formulation of ammonium glyphosate using alkyl glycoside or alkyl polyglycoside surfactants and alkyldiamine alkoxylate surfactants.
Another object of invention is to provide a method of weed control using the formulation of this invention.
SUMMARY OF INVENTION
The present invention relates to a novel granular formulation of ammonium salt of glyphosate, method of preparation thereof and use of said formulation for controlling weeds. In the formulation of present invention, non-toxic surfactants such as alkyldiamine alkoxylate, alkyl-glycoside/polyglycoside etc. have been used.
DETAILED DESCRIPTION OF INVENTION
Though the use of alkyldiamine alkoxylate in granular formulation of ammonium glyphosate is reported in US patent 6248695, the amount of surfactant which has to be used therein is as high as 21-22wt%. On the other hand, in the formulation of present invention, only ll-12wt% of this surfactant is required and as little as 1.1 wt% of water soluble acrylate based copolymer is required. This reduces environmental load of inactive ingredients and at the same time it gives scope to add other desired ingredients. The role of each adjuvant used in the present invention is as described hereinafter.
Alkyl polyglycoside surfactant used in the present invention exhibit low
surface tension, good wettability, they are non-toxic, non-irritant,
environmentally friendly and biodegradable. Due to their safe
characteristics, they are also used in cosmetic compositions. C6-12 Alkyl polyglycosides are preferred surfactants and C8-C10 alkyl polyglycosides are most preferred surfactants. Even mixtures containing variable alkyl chain can be used such as C6 85 C8 alkyl-, C8 & CIO alkyl-, and C8 85 C12 alkyl-polyglycosides etc.
The binder(s) used in the said formulation are based on water-soluble acrylate based co-polymers. Some examples include but not limited to
acrylic acid or methacrylic acid ester - acrylic acid copolymers, wherein the ester may be selected from ethyl, butyl, isobutyl, n-hexyl, n-octyl, lauryl, 2-ethylhexyl and stearyl acrylates. In addition to these, acrylamide - acrylic acid, ethyl acrylate copolymer with methyl methacrylate, methacrylic acid polymer with butyl acrylate can also be used.
Fatty amine ethoxylate surfactant is used in a comparative example.
Ethylenediamine alkoxylate such as ethylenediamine ethoxylate or 1,2-Ethanediamine Polymer With Methyl Oxirane and Oxirane can also be used in the formulation of present invention along with water soluble acrylate based copolymer. Ethylenediamine alkoxylates are approved by EPA reassessment process and are listed on the new 40CFR 180.960 polymers and exempted from the requirement of tolerance data. Ethylenediamine alkoxylates are considered to be low risk under 40CFR 723.250 and no mammalian toxicity is anticipated from dietary, inhalation, or dermal exposure to this compound.
The process for preparation of granular formulation of ammonium glyphosate in accordance with the present invention involves the steps of taking ammonium glyphosate, ammonium sulfate and adjuvants in required quantity in the mixer, adding water to make dough, mixing for half an hour to get uniform dough, extruding the dough to get granules and drying the granules at 40-65°C. Each specific example with quantities of ingredients is described below.
EXAMPLE-1
71wt% ammonium glyphosate, 19.69wt% ammonium sulfate, 8.26wt% C8-10 alkyl polyglycoside and 1.1 wt% acrylate based copolymer were
taken in the mixer. Water was added for making dough. The contents were mixed for half an hour to get uniform dough. The dough was extruded to obtain granules which were dried at 60-65°C. The granules thus obtained were free-flowing and soluble in water.
EXAMPLE-2
71wt% ammonium glyphosate, 21.5wt% ammonium sulfate, 5.9wt% C8-10 alkyl polyglycoside and 1.6wt% acrylate based copolymer were taken in the mixer. Water was added to make dough. The contents were mixed for half an hour to get uniform dough. The dough was extruded to obtain granules which were dried at 60-65°C. The granules thus obtained were free-flowing and soluble in water.
EXAMPLE-3
71wt% ammonium glyphosate, 20.9wt% ammonium sulfate, 7.0wt% 1,2-Ethanediamine Polymer With Methyl Oxirane & Oxirane and 1.1 wt% acrylate based copolymer were taken in the mixer. Water was added to make dough. The contents were mixed for half an hour to get uniform dough. The dough was extruded to obtain granules which were dried at 40°C. The granules thus obtained were free-flowing and soluble in water.
EXAMPLE-4
71wt% ammonium glyphosate, 16.1wt% ammonium sulfate, 11.8wt% 1,2-Ethanediamine, Polymer With Methyl Oxirane and Oxirane and 1.1 wt% acrylate based copolymer were taken in the mixer. Water was added to make dough. The contents were mixed for half an hour to get uniform dough. The dough was extruded to obtain granules which were
dried at 40°C. The granules thus obtained were free-flowing and soluble in water.
EXAMPLE-5 (Comparative Example)
71wt% ammonium glyphosate, 16.1wt% ammonium sulfate, 11.8wt% fatty amine ethoxylate and 1.1 wt% acrylate based copolymer were taken in the mixer. Water was added to make dough. The contents were mixed for half an hour to get uniform dough. The dough was extruded to obtain granules which were dried at 60-65°C. The granules thus obtained were free-flowing and soluble in water.
EXAMPLE - 6
71wt% ammonium glyphosate, 17wt% ammonium sulfate, 10.5wt% C8-10 alkyl polyglycoside and 1.5wt% acrylate based copolymer were taken in the mixer. Water was added to make dough. The contents were mixed for half an hour to get uniform dough. The dough was extruded to obtain granules which were dried at 60-65°C. The granules thus obtained were free-flowing and soluble in water.
EXAMPLE - 7
71wt% ammonium glyphosate, 20wt% ammonium sulfate, 7.5wt% C8-10 alkyl polyglycoside and 1.5wt% acrylate based copolymer were taken in the mixer. Water was added to make dough. The contents were mixed for half an hour to get uniform dough. The dough was extruded to obtain granules which were dried at 60-65°C. The granules thus obtained were free-flowing and soluble in water.
EXAMPLE - 8
71wt% ammonium glyphosate, 12.5wt% ammonium sulfate, 15wt% 1,2-Ethanediamine, Polymer With Methyl Oxirane and Oxirane and 1.5wt% acrylate based copolymer were taken in the mixer. Water was added to make dough. The contents were mixed for half an hour to get uniform dough. The dough was extruded to obtain granules which were dried at 60-65°C. The granules thus obtained were free-flowing and soluble in water.
EXAMPLE - 9
71wt% ammonium glyphosate, 12.5wt% ammonium sulfate, 15wt% fatty amine ethoxylate and 1.5wt% acrylate based copolymer were taken in the mixer. Water was added to make dough. The contents were mixed for half an hour to get uniform dough. The dough was extruded to obtain granules which were dried at 60-65°C. The granules thus obtained were free-flowing and soluble in water.
EXAMPLE - 10
71wt% ammonium glyphosate, 15.5wt% ammonium sulfate, 10.5wt% C8-10 alkyl polyglycoside and 3.0wt% acrylate based copolymer were taken in the mixer. Water was added to make dough. The contents were mixed for half an hour to get uniform dough. The dough was extruded to obtain granules which were dried at 60-65°C. The granules thus obtained were free-flowing but hard in nature and soluble in water.
EXAMPLE - 11
71wt% ammonium glyphosate, 18.5wt% ammonium sulfate, 7.5wt%
C8-10 alkyl polyglycoside and 3.0wt% acrylate based copolymer were
taken in the mixer. Water was added to make dough. The contents were mixed for half an hour to get uniform dough. The dough was extruded to obtain granules which were dried at 60-65°C. The granules thus obtained were free-flowing but hard in nature and soluble in water.
EXAMPLE- 12
71wt% ammonium glyphosate, llwt% ammonium sulfate, 15wt% 1,2-Ethanediamine, Polymer With Methyl Oxirane and Oxirane, and 3.0wt% acrylate based copolymer were taken in the mixer. Water was added to make dough. The contents were mixed for half an hour to get uniform dough. The dough was extruded to obtain granules which were dried at 60-65°C. The granules thus obtained were free-flowing but hard in nature and soluble in water.
EXAMPLE - 13
71wt% ammonium glyphosate, llwt% ammonium sulfate, 15wt% fatty amine ethoxylate and 3.0wt% acrylate based copolymer were taken in the mixer. Water was added to make dough. The contents were mixed for half an hour to get uniform dough. The dough was extruded to obtain granules which were dried at 60-65°C. The granules thus obtained were free-flowing but hard in nature and soluble in water.
EXAMPLE - 14
71wt% ammonium glyphosate, 15.4wt% ammonium sulfate, 12.5wt% C8-10 alkyl polyglycoside and 1.1 wt% acrylate based copolymer were taken in the mixer. Water was added to make dough. The contents were mixed for half an hour to get uniform dough. The dough was extruded to
obtain granules which were dried at 60-65°C. The granules thus obtained were free-flowing and soluble in water.
EXAMPLE- 15
60wt% ammonium glyphosate, 31.1wt% ammonium sulfate, 5.9wt% C8-10 alkyl polyglycoside and 3.0wt% acrylate based copolymer were taken in the mixer. Water was added to make dough. The contents were mixed for half an hour to get uniform dough. The dough was extruded to obtain granules which were dried at 60-65°C. The granules thus obtained were free-flowing and soluble in water.
EXAMPLE - 16
85wt% ammonium glyphosate, 1.5wt% ammonium sulfate, 10.5wt% C8-10 alkyl polyglycoside and 3.0wt% acrylate based copolymer were taken in the mixer. Water was added to make dough. The contents were mixed for half an hour to get uniform dough. The dough was extruded to obtain granules which were dried at 60-65°C. The granules thus obtained were free-flowing and soluble in water.
EXAMPLE-17
71wt% ammonium glyphosate, 15.4wt% ammonium sulfate and 12.5wt% C8-10 alkyl polyglycoside were taken in the mixer. Water was added to make dough. The contents were mixed for half an hour to get uniform dough. The dough was extruded to obtain granules which were dried at 60-65°C. The granules thus obtained were soft and brittle in nature.
The formulation of this invention as described in Examples 1-14 can be used for controlling weeds by spraying aqueous solution of 2-4 Kg formulation per Ha. The optimum dose depends on the weed density. A dose rate of 3 Kg/Ha is generally sufficient. The formulation is more effective if sprayed after weeds develop some leaves. Formulation as described in other Examples can be used in an identical manner, by taking the quantity equivalent to that in Examples 1-14 in terms of the active ingredient.
CLAIMS
1. A granular formulation comprising 70-72 wt% of ammonium glyphosate, 11-22 wt% ammonium sulfate, 5-12.5 wt% alkyl (poly)glycoside and 1-3 wt% acrylate based copolymer.
2. A granular formulation comprising 70-72 wt% of ammonium glyphosate, 11-22 wt% ammonium sulfate, 7-12.5 wt% ethylenediamine alkoxylate and 1-3 wt% acrylate based copolymer.
3. A process for preparing granular formulation comprising the steps of adding 70-72 wt% ammonium glyphosate, 11-22 wt% ammonium sulfate, 7-12.5 wt% ethylenediamine alkoxylate and 1-3 wt% acrylate based copolymer, adding water and mixing for half an hour to obtain a uniform dough, extruding the dough to get granules and drying the granules at 38 - 65°C.
4. A process for preparing granular formulation comprising the steps of adding 70-72 wt% ammonium glyphosate, 11-22 wt% ammonium sulfate, 5-12.5 wt% alkyl (poly)glycoside and 1-3 wt% acrylate based copolymer, adding water and mixing for half an hour to obtain a uniform dough, extruding the dough to get granules and drying the granules at 38 - 65°C.
5. A method of controlling weeds by spraying aqueous solution of
granular formulation as claimed in claim 1 or 2.
6. A method of controlling weeds as claimed in claim 5, wherein the dose
of said formulation is 2-4 Kg/Ha.
7. A method of controlling weeds by spraying aqueous solution of granular formulation which is prepared as per the process claimed in any of the claims claims 3, 4 or 12.
8. A granular formulation as claimed in claim 1 or prepared in accordance with the process as claimed in claim 4, wherein said alkyl polyglycoside is selected from C6-C12 alkyl polyglycoside or a mixture thereof.
9. A granular formulation as claimed in claim 1 or prepared in accordance with the process as claimed in claim 4, wherein said alkyl polyglycoside is selected from C8-C10 alkyl polyglycoside.
10. A granular formulation described 85 prepared in accordance with any of the examples disclosed in this specification except example-5.
11. A granular formulation comprising 60-85 wt% of ammonium
glyphosate, 1.5-32 wt% ammonium sulfate, 5-12.5 wt% alkyl
(poly)glycoside and 1-3 wt% acrylate based copolymer.
12. A process for preparing granular formulation comprising the steps of
adding 60-85 wt% ammonium glyphosate, 1.5-32 wt% ammonium
sulfate, 5-12.5 wt% alkyl (poly)glycoside and 1-3 wt% acrylate based
copolymer, adding water and mixing for half an hour to obtain a uniform
dough, extruding the dough to get granules and drying the granules at
38 - 65°C.
ABSTRACT
This invention relates to an improved granular formulation of herbicide glyphosate in form of ammonium salt using environmentally friendly adjuvants, and a process for preparation thereof. The formulation minimizes the use of some inactive ingredients without compromising the effectiveness of the product.
| Section | Controller | Decision Date |
|---|---|---|
| # | Name | Date |
|---|---|---|
| 1 | 253-MUM-2008-FORM 4 [05-08-2024(online)].pdf | 2024-08-05 |
| 1 | 253-MUM-2008-PETITION UNDER RULE-138(17-11-2011).pdf | 2011-11-17 |
| 2 | 253-MUM-2008-Correspondence (Renewal)-130223.pdf | 2023-02-15 |
| 2 | 253-MUM-2008-FORM 3(17-11-2011).pdf | 2011-11-17 |
| 3 | 283968-CORRESPONDENCE(RENEWAL)-240222.pdf | 2022-02-28 |
| 3 | 253-MUM-2008-FORM 18(17-11-2011).pdf | 2011-11-17 |
| 4 | 283968-Correspondence (Renewal)-120220.pdf | 2020-02-14 |
| 4 | 253-MUM-2008-CORRESPONDENCE(17-11-2011).pdf | 2011-11-17 |
| 5 | 283968-Correspondence (Renewal)-301019.pdf | 2019-11-01 |
| 5 | 253-MUM-2008-CORRESPONDENCE (17-11-2011).pdf | 2011-11-17 |
| 6 | 283968-ANNEXURE-1 & 2-101019.pdf | 2019-10-12 |
| 6 | 253-MUM-2008-ANNEXURE 1(17-11-2011).pdf | 2011-11-17 |
| 7 | 283968-Correspondence-101019.pdf | 2019-10-12 |
| 7 | 253-MUM-2008-REPLY TO EXAMINATION REPORT-(20-06-2016).pdf | 2016-06-20 |
| 8 | 253-MUM-2008-OTHERS (E.P. DOCU.)-(20-06-2016).pdf | 2016-06-20 |
| 8 | 283968-Form 16-101019.pdf | 2019-10-12 |
| 9 | 253-MUM-2008-CLAIMS(MARKED COPY)-(20-06-2016).pdf | 2016-06-20 |
| 10 | 253-MUM-2008-ABSTRACT.pdf | 2018-08-09 |
| 10 | 253-MUM-2008-CLAIMS(AMENDED)-(20-06-2016).pdf | 2016-06-20 |
| 11 | 253-MUM-2008-Claims-280115.pdf | 2018-08-09 |
| 11 | 253-MUM-2008-MARKED COPY-19-04-2017.pdf | 2017-04-19 |
| 12 | 253-MUM-2008-CORRESPONDENCE-19-04-2017.pdf | 2017-04-19 |
| 13 | 253-MUM-2008-CLAIMS.pdf | 2018-08-09 |
| 13 | 253-MUM-2008-REPLY TO HEARING-26-04-2017.pdf | 2017-04-26 |
| 14 | 253-MUM-2008-CLAIMS(MARKED COPY)-26-04-2017.pdf | 2017-04-26 |
| 14 | 253-MUM-2008-CORRESPONDENCE(28-3-2014).pdf | 2018-08-09 |
| 15 | 253-MUM-2008-CLAIMS(AMENDED)-26-04-2017.pdf | 2017-04-26 |
| 15 | 253-MUM-2008-CORRESPONDENCE(IPO)-(6-6-2017).pdf | 2018-08-09 |
| 16 | 253-MUM-2008-CORRESPONDENCE(IPO)-(DECISION)-(6-6-2017).pdf | 2018-08-09 |
| 16 | 253-MUM-2008-FORM 3-19-05-2017.pdf | 2017-05-19 |
| 17 | 253-MUM-2008-EP DOCUMENT-19-05-2017.pdf | 2017-05-19 |
| 17 | 253-MUM-2008-CORRESPONDENCE(IPO)-(FER)-(29-9-2014).pdf | 2018-08-09 |
| 18 | 253-MUM-2008-CORRESPONDENCE(IPO)-(HEARING NOTICE)-(7-4-2017).pdf | 2018-08-09 |
| 18 | 253-MUM-2008-CORRESPONDENCE-19-05-2017.pdf | 2017-05-19 |
| 19 | 253-MUM-2008-Correspondence-190215.pdf | 2018-08-09 |
| 19 | 283968-CORRESPONDENCE(RENEWAL PAYMENT LETTER)-11-07-2017.pdf | 2017-07-11 |
| 20 | 253-MUM-2008-DESCRIPTION(COMPLETE).pdf | 2018-08-09 |
| 20 | 283968-CORRESPONDENCE(RENEWAL PAYMENT LETTER)-02-04-2018.pdf | 2018-04-02 |
| 21 | 253-MUM-2008-Examination Report Reply Recieved-280115.pdf | 2018-08-09 |
| 21 | 253-MUM-2008_EXAMREPORT.pdf | 2018-08-09 |
| 22 | 253-MUM-2008-FORM 1.pdf | 2018-08-09 |
| 22 | 253-MUM-2008-PETITION UNDER RULE 137-120815.pdf | 2018-08-09 |
| 23 | 253-MUM-2008-PatentCertificateCoverLetter.pdf | 2018-08-09 |
| 23 | 253-MUM-2008-FORM 2(GRANTED)-(6-6-2017).pdf | 2018-08-09 |
| 24 | 253-MUM-2008-OTHERS-280115.pdf | 2018-08-09 |
| 24 | 253-MUM-2008-FORM 2(TITLE PAGE).pdf | 2018-08-09 |
| 25 | 253-mum-2008-form 2.pdf | 2018-08-09 |
| 25 | 253-MUM-2008-Other Patent Document-120815.pdf | 2018-08-09 |
| 26 | 253-MUM-2008-FORM 3(28-3-2014).pdf | 2018-08-09 |
| 26 | 253-MUM-2008-OTHER DOCUMENTS-280115.pdf | 2018-08-09 |
| 27 | 253-MUM-2008-FORM 3.pdf | 2018-08-09 |
| 28 | 253-MUM-2008-FORM 3.pdf | 2018-08-09 |
| 29 | 253-MUM-2008-FORM 3(28-3-2014).pdf | 2018-08-09 |
| 29 | 253-MUM-2008-OTHER DOCUMENTS-280115.pdf | 2018-08-09 |
| 30 | 253-mum-2008-form 2.pdf | 2018-08-09 |
| 30 | 253-MUM-2008-Other Patent Document-120815.pdf | 2018-08-09 |
| 31 | 253-MUM-2008-FORM 2(TITLE PAGE).pdf | 2018-08-09 |
| 31 | 253-MUM-2008-OTHERS-280115.pdf | 2018-08-09 |
| 32 | 253-MUM-2008-FORM 2(GRANTED)-(6-6-2017).pdf | 2018-08-09 |
| 32 | 253-MUM-2008-PatentCertificateCoverLetter.pdf | 2018-08-09 |
| 33 | 253-MUM-2008-FORM 1.pdf | 2018-08-09 |
| 33 | 253-MUM-2008-PETITION UNDER RULE 137-120815.pdf | 2018-08-09 |
| 34 | 253-MUM-2008-Examination Report Reply Recieved-280115.pdf | 2018-08-09 |
| 34 | 253-MUM-2008_EXAMREPORT.pdf | 2018-08-09 |
| 35 | 283968-CORRESPONDENCE(RENEWAL PAYMENT LETTER)-02-04-2018.pdf | 2018-04-02 |
| 35 | 253-MUM-2008-DESCRIPTION(COMPLETE).pdf | 2018-08-09 |
| 36 | 253-MUM-2008-Correspondence-190215.pdf | 2018-08-09 |
| 36 | 283968-CORRESPONDENCE(RENEWAL PAYMENT LETTER)-11-07-2017.pdf | 2017-07-11 |
| 37 | 253-MUM-2008-CORRESPONDENCE(IPO)-(HEARING NOTICE)-(7-4-2017).pdf | 2018-08-09 |
| 37 | 253-MUM-2008-CORRESPONDENCE-19-05-2017.pdf | 2017-05-19 |
| 38 | 253-MUM-2008-CORRESPONDENCE(IPO)-(FER)-(29-9-2014).pdf | 2018-08-09 |
| 38 | 253-MUM-2008-EP DOCUMENT-19-05-2017.pdf | 2017-05-19 |
| 39 | 253-MUM-2008-CORRESPONDENCE(IPO)-(DECISION)-(6-6-2017).pdf | 2018-08-09 |
| 39 | 253-MUM-2008-FORM 3-19-05-2017.pdf | 2017-05-19 |
| 40 | 253-MUM-2008-CORRESPONDENCE(IPO)-(6-6-2017).pdf | 2018-08-09 |
| 40 | 253-MUM-2008-CLAIMS(AMENDED)-26-04-2017.pdf | 2017-04-26 |
| 41 | 253-MUM-2008-CLAIMS(MARKED COPY)-26-04-2017.pdf | 2017-04-26 |
| 41 | 253-MUM-2008-CORRESPONDENCE(28-3-2014).pdf | 2018-08-09 |
| 42 | 253-MUM-2008-CLAIMS.pdf | 2018-08-09 |
| 42 | 253-MUM-2008-REPLY TO HEARING-26-04-2017.pdf | 2017-04-26 |
| 43 | 253-MUM-2008-CORRESPONDENCE-19-04-2017.pdf | 2017-04-19 |
| 44 | 253-MUM-2008-Claims-280115.pdf | 2018-08-09 |
| 44 | 253-MUM-2008-MARKED COPY-19-04-2017.pdf | 2017-04-19 |
| 45 | 253-MUM-2008-ABSTRACT.pdf | 2018-08-09 |
| 45 | 253-MUM-2008-CLAIMS(AMENDED)-(20-06-2016).pdf | 2016-06-20 |
| 46 | 253-MUM-2008-CLAIMS(MARKED COPY)-(20-06-2016).pdf | 2016-06-20 |
| 47 | 253-MUM-2008-OTHERS (E.P. DOCU.)-(20-06-2016).pdf | 2016-06-20 |
| 47 | 283968-Form 16-101019.pdf | 2019-10-12 |
| 48 | 253-MUM-2008-REPLY TO EXAMINATION REPORT-(20-06-2016).pdf | 2016-06-20 |
| 48 | 283968-Correspondence-101019.pdf | 2019-10-12 |
| 49 | 253-MUM-2008-ANNEXURE 1(17-11-2011).pdf | 2011-11-17 |
| 49 | 283968-ANNEXURE-1 & 2-101019.pdf | 2019-10-12 |
| 50 | 283968-Correspondence (Renewal)-301019.pdf | 2019-11-01 |
| 50 | 253-MUM-2008-CORRESPONDENCE (17-11-2011).pdf | 2011-11-17 |
| 51 | 283968-Correspondence (Renewal)-120220.pdf | 2020-02-14 |
| 51 | 253-MUM-2008-CORRESPONDENCE(17-11-2011).pdf | 2011-11-17 |
| 52 | 283968-CORRESPONDENCE(RENEWAL)-240222.pdf | 2022-02-28 |
| 52 | 253-MUM-2008-FORM 18(17-11-2011).pdf | 2011-11-17 |
| 53 | 253-MUM-2008-Correspondence (Renewal)-130223.pdf | 2023-02-15 |
| 53 | 253-MUM-2008-FORM 3(17-11-2011).pdf | 2011-11-17 |
| 54 | 253-MUM-2008-FORM 4 [05-08-2024(online)].pdf | 2024-08-05 |
| 54 | 253-MUM-2008-PETITION UNDER RULE-138(17-11-2011).pdf | 2011-11-17 |