Company Information

CIN
Status
Date of Incorporation
23 April 1999
State / ROC
Delhi / ROC Delhi
Last Balance Sheet
31 March 2023
Last Annual Meeting
13 September 2023
Paid Up Capital
29,509,080
Authorised Capital
75,000,000

Directors

Uday Shyamkant Prabhudesai
Uday Shyamkant Prabhudesai
Director/Designated Partner
over 2 years ago
Saket Bhattar
Saket Bhattar
Director/Designated Partner
almost 3 years ago
Amit Kumar Tantia
Amit Kumar Tantia
Director/Designated Partner
over 3 years ago
Deepak Bisht
Deepak Bisht
Director/Designated Partner
over 5 years ago

Past Directors

Bharat Tulsian
Bharat Tulsian
Director
over 6 years ago
Michael Jeffrey Banach
Michael Jeffrey Banach
Managing Director
over 7 years ago
Steven Christian Gimre
Steven Christian Gimre
Director
over 7 years ago
Soumendra Mohan Banerjee
Soumendra Mohan Banerjee
Director
about 10 years ago
Kartik Suryanarayana
Kartik Suryanarayana
Director
about 10 years ago
Glen William Davies
Glen William Davies
Director
about 24 years ago
Rajneesh Kumar Sharma
Rajneesh Kumar Sharma
Company Secretary
about 24 years ago

Patents

"A Catalytic Composition For The Conversion Of Hydrocarbons"

A catalytic composition for the conversion of hydrocarbons comprising a combination of a refractory inorganic oxide support with 0.01 to 5 mass% on an elemental basis of a Group IVA(IUPAC 14) metal component, 0.01 to 2 mass % on an elemental basis of a platinum metal component, and 0.05 mass % on an elemental basis ...

"An Aparatus For Transport Of Particulate Material"

A system for transporting particulate material uses a combination of non-mechanical valves and pneumatic and gravity transport to reduce breakage of particulate material. This system is particularly useful for the conveyance of catalyst particles where a lift conduit raises the particles from a low elevation to a re...

"A Process For The Production Of Light Olefins From A Hydrocarbon Gas Feedstream"

A process for the production of light olefins from a hydrocarbon gas feedstream, comprising methane and/or ethane, which comprises: a) passing said feedstream in combination with a water stream to a syngas production zone at a syngas temperature of 700 to 1100°C and a syngas pressure of 2 to 75 Mpa to produce a sy...

"Nitrogen Selective Zeolitic Adsorbent For Use In Air Separation Process"

In using calcium-exchanged forms of zeolite X as selective adsorbents for nitrogen in PSA air separation process, it has been discovered that, particularly under certain temperature and pressure conditions, superior performance is not, as is generally believed, obtained when the calcium content is at a maximum, but ...

"Fluid Catalytic Cracking Process For The Fluidized Catalytic Cracking Of A Hydrocarbon Feedstock"

The effective utilization of available stripping medium in an FCC process is hcreased by using a cyclonic separation method and apparatus to discharge particulate solids and gaseous fluids into a separation vessel from a discharge opening of a central conduit and to withdraw separated gaseous fluids from the separat...

"A Process For Catalytic Reforming Of A Naphtha Feedstock".

A novel catalyst and the use thereof in a hydrocarbon conversion process is disclosed. The catalyst comprises a refractory inorganic oxide, platinum-group metal, Group IVA(IUPAC 14) metal, and europium in a specified ratio. Utilization of this catalyst in the conversion of hydrocarbons, especially in reforming, resu...

"A Process For Removal Of Polynuclear Aromatic Compounds"

Trace quantities of polynuclear aromatic compounds are removed from the vapor effluent of a hydrocarbon dehydrogenation zone containing normally gaseous olefinic hydrocarbons, trace mononuclear aromatic, compounds and trace polynuclear aromatic compounds by cooling the vapor effluent to condense at least a portion t...

"Process For Shut Down Of A Membrane Separation Zone"

A process is disclosed for the shut-down of a membrane separation zone comprising a non-permeate side and a permeate side and processing a feed stream comprising a non-permeable component, a less-readily permeable, condensible component, and a readily permeable component. When the feed stream is not passed to the me...

"A Process For Catalytically Reforming A Naphtha Feedstock"

A naphtha feedstock is catalytically reformed in a combination sequence comprising a continuous-reforming zone, consisting essentially of a moving-bed catalytic reforming zone with continuous regeneration of catalyst particles, followed by a zeolitic-reforming zone containing a catalyst comprising a platinum-group m...

"A Process For The Production Of Light Olefins From A Hydrocarbon Gas Feedstream"

Light olefins are produced from a hydrocarbon gas stream by a combination of steam reforming, oxygenate production, and oxygenate conversion to olefm wherein a crude methanol stream - produced in the production of oxygenates and comprising methanol, light ends, and heavier alcohols - is passed directly to the oxygen...

"An Apparatus For Use Disengaging Particles From A Lift Riser For A Catalytic Reforming Process"

A system for transporting particulate material uses a combination of non-mechanical valves and pneumatic and gravity transport to reduce breakage of particulate material. This system is particularly useful for the conveyance of catalyst particles where a lift conduit raises the particles from a low elevation to a re...

"Process For Producing Light Olefins From An Oxygenate Feedstream"

Light olefins are produced from an oxygenate feedstream by ontacting the oxygenate feedstream in the presence of a methane diluent in a reaction zone containing a metal aluminium phosphate molecular sieve (ELAPO) catalyst at conditions selective for the conversion of at least a portion of the feedstock into light ol...

"A Process For Removing A Metal Ion Contaminant From Liquid Streams"

Contaminant metal ions are removed from a liquid stream by a process involving contacting at adsorption conditions the liquid stream with a novel crystalline molecular sieve which has a crystal structure which is an intergrowth of the pharmacosiderite and sitinakite structures. The molecular sieve has an emp...

Registered Trademarks

Define Uop

[Class : 1] Catalyst For Diolefin Hydrogenation Process.

Documents

Form DPT-3-29122020-signed
Form MSME FORM I-31102020_signed
List of share holders, debenture holders;-15092020
Copy of MGT-8-15092020
Form MGT-7-15092020_signed
Form AOC-4(XBRL)-10092020-signed
XBRL financial statements duly authenticated as per section 134 (including Board's report,auditor's report and other documents)-04092020
Form MGT-14-14082020-signed
Form DIR-12-14082020_signed
Optional Attachment-(1)-14082020
Copy(s) of resolution(s) along with copy of explanatory statement under section 173-13082020
Altered articles of association-13082020
Form ADT-1-11082020_signed
Copy of written consent given by auditor-11082020
Copy of resolution passed by the company-11082020
Form DPT-3-03082020-signed
Form MSME FORM I-30042020_signed
Form DIR-12-07012020_signed
Notice of resignation;-06012020
Optional Attachment-(1)-06012020
Evidence of cessation;-06012020
Declaration of the appointee director, Managing director, in Form No. DIR-2;-06012020
Form DIR-11-05012020_signed
Form DIR-11-02012020_signed
Acknowledgement received from company-02012020
Notice of resignation filed with the company-02012020
Proof of dispatch-02012020
Notice of resignation filed with the company-31122019
Acknowledgement received from company-31122019
Proof of dispatch-31122019