The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Mar. 31, 2015

Filed:

Jun. 27, 2011
Applicants:

Krista Marie Prentice, Bethlehem, NJ (US);

Michel Daage, Hellertown, PA (US);

Ajit Bhaskar Dandekar, Bridgewater, NJ (US);

Christopher Gordon Oliveri, Stewartsville, NJ (US);

Rohit Vijay, Annandale, NJ (US);

Stephen J. Mccarthy, Center Valley, PA (US);

Wenyih F. Lai, Bridgewater, NJ (US);

Bradley R. Fingland, Annandale, NJ (US);

Inventors:

Krista Marie Prentice, Bethlehem, NJ (US);

Michel Daage, Hellertown, PA (US);

Ajit Bhaskar Dandekar, Bridgewater, NJ (US);

Christopher Gordon Oliveri, Stewartsville, NJ (US);

Rohit Vijay, Annandale, NJ (US);

Stephen J. McCarthy, Center Valley, PA (US);

Wenyih F. Lai, Bridgewater, NJ (US);

Bradley R. Fingland, Annandale, NJ (US);

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 73/38 (2006.01); C10G 73/44 (2006.01); C10G 45/02 (2006.01); C10G 45/64 (2006.01); C10G 47/16 (2006.01); C10G 7/00 (2006.01); C10G 49/22 (2006.01); C10G 65/12 (2006.01); C10G 65/04 (2006.01); B01J 29/74 (2006.01); B01J 35/02 (2006.01);
U.S. Cl.
CPC ...
C10G 65/12 (2013.01); C10G 45/64 (2013.01); C10G 65/043 (2013.01); C10G 2300/302 (2013.01); C10G 2300/4081 (2013.01); C10G 2400/02 (2013.01); C10G 2400/04 (2013.01); C10G 2400/10 (2013.01); C10G 2300/4018 (2013.01); C10G 2300/202 (2013.01); B01J 29/7461 (2013.01); B01J 35/026 (2013.01); B01J 2229/36 (2013.01); B01J 2229/42 (2013.01);
Abstract

An integrated process for producing naphtha fuel, diesel fuel and/or lubricant base oils from feedstocks under sour conditions is provided. The ability to process feedstocks under higher sulfur and/or nitrogen conditions allows for reduced cost processing and increases the flexibility in selecting a suitable feedstock. The sour feed can be delivered to a catalytic dewaxing step without any separation of sulfur and nitrogen contaminants. The integrated process includes an initial dewaxing of a feed under sour conditions, optional hydrocracking of the dewaxed feed, and a separation to form a first diesel product and a bottoms fraction. The bottoms fraction is then exposed to additional hydrocracking and dewaxing to form a second diesel product and optionally a lubricant base oil product. Alternatively, a feedstock can be hydrotreated, fractionated, dewaxed, and then hydrocracked to form a diesel fuel and a dewaxed, hydrocracked bottoms fraction that is optionally suitable for use as a lubricant base oil.


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