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Patent
Bharat Petroleum Corporation Ltd. | Date: 2015-12-03

The present disclosure provides methods and apparatus for catalytic cracking of hydrocarbon feed. The apparatus includes a plurality of stages, wherein hydrocarbon feed is introduced into a bottom stage reactor and flows in an overall upward direction. A reaction catalyst stream is introduced into a top stage reactor and flows in an overall downward direction. In each of the stages, the hydrocarbon feed is allowed to come in contact with the reaction catalyst stream received at the particular stage for cracking of the hydrocarbon feed. The final cracked product stream is obtained at an outlet of the top stage reactor and a final spent catalyst stream is obtained at an outlet of the bottom stage reactor.


Patent
Bharat Petroleum Corporation Ltd. | Date: 2013-03-18

The present invention relates to a process for obtaining food grade hexane, comprising: fractionating a hydrocarbon feed having a boiling point in the range of 50 C. to 140 C. to obtain a hydrocarbon fraction having boiling point in the range of 63 C. to 69 C. and having 3%-15% (wt/wt) of aromatic compounds content; extracting the hydrocarbon fraction by counter current solvent extraction using sulfolane as a solvent to obtain a first raffinate phase; extracting the first raffinate phase by co-current solvent extraction using sulfolane as a solvent to obtain a second raffinate phase; and washing the second raffinate phase with water to obtain a food grade hexane containing less than 100 ppm of aromatic compounds.


Patent
Bharat Petroleum Corporation Ltd. | Date: 2012-05-07

The present invention relates to a multifunctional catalyst additive composition for reduction of carbon monoxide and nitrogen oxides in a fluid catalytic cracking process comprising an inorganic oxide; alumino silicate or a zeolite; a noble metal; a metal of Group I A; a metal of Group II A; a metal of Group III A; a metal of Group IV A; a metal of Group V A; a rare earth oxide; at least a metal of Group VIII. The composition is attrition resistant and is incorporated on a support. The present invention also discloses a process for preparing the multifunctional catalyst additive composition. The present invention also discloses a fluid cracking catalyst comprising the multifunctional catalyst additive composition.


The present invention relates to sulphur reduction catalyst additive composition comprising an inorganic porous support incorporated with metals; an alumino silicate or zeolite component; an alumina component and clay. More particularly the present invention relates to sulphur reduction catalyst additive composition comprising refinery spent catalyst as support. The primary sulphur reduction catalyst additive component of the catalyst composition contains metals of Group I, II, III, IV, V, VIII of the Periodic Table, preferably Zinc or Magnesium or combination thereof or one of the transition metals along with other metals.


Patent
Bharat Petroleum Corporation Ltd. | Date: 2014-06-23

A method for modification of pretreated acidic porous material via selective cation exchange using suitable solvent to obtain higher noble metal dispersion is described herein. The solvent system required for cation exchange should have its dielectric constant in the range of 25-45, wherein this solvent property is found to impart significant effect on cation loading and distribution, which in turn defines the stability, dispersion of the noble metals. The catalyst so obtained has higher noble metal dispersion and when used for hydroisomerization reaction, leads to higher selectivity even at significantly high conversion values.


Patent
Bharat Petroleum Corporation Ltd. | Date: 2016-01-06

Method(s) and system(s) for estimation of cold-flow properties of refinery product blends are described. The method may include receiving refinery products to be blended and ratios of the refinery products to be used for producing the refinery product blend, and determining whether the refinery products include at least one heavy product. The cold-flow property of the refinery product blend can be estimated based on a first correlation when the refinery products include the at least one heavy product, and based on a second correlation when the refinery products include no heavy product. The first correlation and the second correlation can differ in at least a sign of a coefficient.


In accordance with the present subject matter there is provided a process for producing mono-, di- and triesters of glycerol over a catalyst composition. The catalyst composition including a base catalyst and a support material based on phyllosilicates of montmorillonite structure and the process for preparing the catalyst composition is also described.


The present invention relates to a catalyst composition for conversion of vegetable oils to hydrocarbon products in the diesel boiling range, comprising a porous support; Group III A or VA element in the range of 1-10 wt%; Group VI B elements in the range of 1 to 20 wt%; Group VIII B elements in range of 0.01 to 10 wt%.. The present invention further provides the process for preparing the catalyst composition for conversion of vegetable oils to hydrocarbon products in the diesel boiling range. The present invention also provides the process for conversion of vegetable oils to hydrocarbon products in the diesel boiling range using the catalyst composition or discarded refinery spent hydrotreating catalyst.


Patent
Council Of Scientific & Industrial Research and Bharat Petroleum Corporation Ltd. | Date: 2016-08-05

The present invention discloses activated carbon-metal organic framework composite materials (AC@MOF) with enhanced gas adsorption capacity. The present invention also discloses a process for the preparation of carbon-metal organic framework composite materials (AC@MOF). The present invention involves the use of void space filling method in metal organic frameworks (MOFs), which have been accomplished by in-situ addition of selected type and appropriate amount of activated carbon during the synthesis of MOF such as Cu-BTC, in the storage of gases such as methane. The gas adsorption capacity of these AC@MOF composite materials is significantly increased through this method.


Patent
Bharat Petroleum Corporation Ltd. | Date: 2014-04-15

Methods, apparatus and processes for three phase contacting and reactions in a cross flow reactor with reduced feed vaporization, low pressure operation, higher liquid holdup, lower reactor pressure drop, low severity operation, and reduced product inhibitory effects. A cross flow reactor for three phase catalytic hydroprocessing, having at least one reactor stage is disclosed. The reactor stage has a central gas distributor with perforated lateral surface for distributing gas, a middle region accommodating a packed catalyst bed, and an outer gas space for removal of effluent gases from the middle region. The middle region receives a liquid reactant and gas from central gas distributor to carry out three phase catalytic hydroprocessing reaction.

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