Upgrading kerosene to jet fuel with carbonaceous desorption and filtration

Patent metadata

Field	Value
Publication number	US-9976094-B2
Application number	US-201615376145-A
Country	US
Kind code	B2
Filing date	Dec 12, 2016
Priority date	Dec 18, 2014
Publication date	May 22, 2018
Grant date	May 22, 2018

Abstract

The invention relates to removing contaminants from jet fuel or kerosene using solid sorbents that are comprised primarily of carbon and preferably of coke particles. The coke particles have an affinity for contaminants in jet fuel and kerosene and are sized to be filtered from the liquid fuel without plugging. As the contaminants agglomerate onto the solid sorbent, the resulting particles form a filter cake on conventional filter materials in such a way as to allow the jet fuel or kerosene to pass on through without significant pressure drop or delay.

First claim

The invention claimed is:

1. A process for removing contaminants from jet fuel comprising:
a) adding a solid sorbent to the jet fuel wherein the solid sorbent is a mixture of green coke and recycled green coke that has been subjected to an inert heating process to liberate contaminants from a previous contaminant adsorption process;
b) agglomerating/adsorbing contaminants from the jet fuel to the solid sorbent;
c) separating the solid sorbent with agglomerated/adsorbed contaminants from the jet fuel;
d) separating undersized solid sorbent particles separated from the jet fuel prior to recycling such solid sorbent so as to maintain a desired particle size for the solid sorbent used in the contaminant removal process; and
e) heating the solid sorbent to liberate the contaminants from the solid sorbent and to prepare the solid sorbent for recycling for re-use as solid sorbent in step a).

2. The process according to claim 1 wherein the green coke has an average size of between 1 and 250 microns.

3. The process according to claim 1 wherein the green coke has an average size of between 3 and 50 microns.

4. The process according to claim 1 wherein the green coke has an average size of between 3 and 25 microns.

5. The process according to claim 1 wherein the mixture of green coke and recycled green coke has an average particle size of between 1 and 250 microns.

6. The process according to claim 1 wherein the mixture of green coke and recycled green coke has an average size of between 3 and 50 microns.

7. The process according to claim 1 wherein the mixture of green coke and recycled green coke has an average size of between 3 and 25 microns.

8. The process according to claim 1 further including a step of de-wetting the solid sorbent with contaminants agglomerated thereon so as to remove any residual jet fuel from the solid sorbent.

9. The process according to claim 1 wherein the solid sorbent is subjected to a heat treatment step of up to 500 C. in a nitrogen environment prior to the step of adding solid sorbent to the kerosene.

10. The process according to claim 1 wherein the separation of the sorbent from the jet fuel occurs in a generally vertical tank with a jet fuel feed and solid sorbent delivered to the top and mixed bay a bladed stirrer attached to a generally vertical shaft that is rotated to stir the jet fuel and solid sorbent mixture in the vessel and further wherein a filter is arranged generally horizontally such that the solid sorbent is exits adjacent the filter and the jet fuel exits below the horizontal filter.

Assignees

• Phillips 66 Co

Inventors

• Jemmett Mark R
• Mao Zhenhua
• Contreras Jesse
• Lundwall Matthew J

Classifications

• C10G2300/205

  Metal content · CPC title

• C10G25/06

  with moving sorbents or sorbents dispersed in the oil · CPC title

• C10G25/12

  Recovery of used adsorbent · CPC title

• C10G2300/1051

  Kerosene having a boiling range of about 180 - 230 °C · CPC title

• C10G25/003 Primary

  Specific sorbent material, not covered by C10G25/02 or C10G25/03 · CPC title