Prabhakar Kulkarni resumes & CV records
Resumes
Prabhakar Kulkarni
Prabhakar Kulkarni
Prabhakar B Kulkarni, 881346 Lake Pointe Pkwy, Sugar Land, TX 77478
Prabhakar Kulkarni Phones & Addresses
1346 Lake Pointe Pkwy, Sugar Land, TX 77478 281-8004515
23 Du Pont Cir, Sugar Land, TX 77479 281-2770323 281-3130385 281-9800451
Mercer Island, WA
Houston, TX
23 Du Pont Cir, Sugar Land, TX 77479 915-4940994
Emails
Mentions for Prabhakar B Kulkarni
Publications & IP owners
Us Patents
Method And Apparatus For Treatment Of Hazardous Waste In Absence Of Oxygen
US Patent:
4896614, Jan 30, 1990
Filed:
Sep 15, 1988
Appl. No.:
7/244318
Inventors:
Prabhakar Kulkarni - Houston TX
International Classification:
F23G 700
US Classification:
110346
Abstract:
Hazardous waste treatment method and apparatus are disclosed in the preferred and illustrated emboldiment. A feedstock of hazardous waste material is combusted in a plasma generator in the absence of oxygen and converted into a gaseous outflow which is collected in a reactor chamber. The gaseous outflow is cooled and separated into selected constituents which are collected in storage vessels.
Method For Treatment Of Hazardous Waste In Absence Of Oxygen
US Patent:
5138959, Aug 18, 1992
Filed:
Apr 29, 1991
Appl. No.:
7/693942
Inventors:
Prabhakar Kulkarni - Houston TX
International Classification:
F23G 704
US Classification:
110346
Abstract:
Hazardous waste treatment method and apparatus are disclosed in the preferred and illustrated embodiment. A feedstock of solid or liquid hazardous waste material is combusted in a plasma generator in the absence of oxygen and converted into non-hazardous components which are collected in a reactor chamber. The non-hazardous components are further converted into a gaseous outflow which is cooled and separated into selected constituents which are collected in storage vessels.
Coal Liquefaction Process
US Patent:
4602991, Jul 29, 1986
Filed:
Oct 17, 1983
Appl. No.:
6/542276
Inventors:
Prabhakar Kulkarni - Houston TX
International Classification:
C10G 100
C10G 106
C10G 106
US Classification:
208400
Abstract:
A liquefaction process for coal or lignite is set forth. In the preferred and illustrated embodiment, coal or lignite is ground to a suitable particle size and placed in a reactor vessel. The reactor vessel is located within a pressure vessel. Pressure in the vessel is reduced to about 10. sup. -2 torr. Heat is applied. One procedure is to convert the carbon (in the coal or lignite) at an elevated temperature (600. degree. -900. degree. F. ) in the presence of hydrogen (at pressures as high as 2,000 psi) into a hydrocarbon mix; depressurization avoids making various oxides and nitrides, and also can be optionally carried out in the presence of iron or iron ore in particulate form acting as a catalyst.
Method And Apparatus For Treatment Of Hazardous Waste In Absence Of Oxygen
US Patent:
5010829, Apr 30, 1991
Filed:
Jan 29, 1990
Appl. No.:
7/471551
Inventors:
Prabhakar Kulkarni - Houston TX
International Classification:
F23G 704
US Classification:
110346
Abstract:
Hazardous waste treatment method and apparatus are disclosed in the preferred and illustrated embodiment. A feedstock of solid or liquid hazardous waste material is combusted in a plasma generator in the absence of oxygen and converted into non-hazardous components which are collected in a reactor chamber. The non-hazardous components are further converted into a gaseous outflow which is cooled and separated into selected constituents which are collected in storage vessels.
Hydrogen Generating Method
US Patent:
4729891, Mar 8, 1988
Filed:
Aug 16, 1984
Appl. No.:
6/641576
Inventors:
Prabhakar Kulkarni - Houston TX
International Classification:
C01B 1300
US Classification:
423650
Abstract:
Hydrogen generating method and apparatus are disclosed in the preferred and illustrated embodiment. A feedstock of methane from heated coal and steam or methane obtained by any other means is delivered into a furnace. The furnace (free of oxygen) heats to about 950. degree. F. in vacuum conditions, and converts the methane into elemental carbon and hydrogen gas. The preferred embodiment utilizes an inductive furnace for heating.
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