U.S. patent application number 14/665111 was filed with the patent office on 2015-11-26 for fuel compositions.
The applicant listed for this patent is SHELL OIL COMPANY. Invention is credited to Shannon BOUDREAUX, Michael Allen BRANCH, Ariel BRU, Tommy Louis BRUMFIELD, Cynthia DELANEY-KINSELLA, Danny F. DROUBI, Lawrence Stephen KRAUS, Dana Tatum LIPINSKY, Koen STEERNBERG, Pierre TARDIFF.
Application Number | 20150337225 14/665111 |
Document ID | / |
Family ID | 50979696 |
Filed Date | 2015-11-26 |
United States Patent
Application |
20150337225 |
Kind Code |
A1 |
DROUBI; Danny F. ; et
al. |
November 26, 2015 |
FUEL COMPOSITIONS
Abstract
Low sulphur marine fuel compositions are provided. Embodiments
comprise greater than 50 to 90 wt % of a residual hydrocarbon
component, with the remaining 10 to 50 wt % selected from a
non-hydroprocessed hydrocarbon component, a hydroprocessed
hydrocarbon component, and a combination thereof. Embodiments of
the marine fuel composition can have a sulphur content of about 0.1
wt % or less.
Inventors: |
DROUBI; Danny F.; (Houston,
TX) ; BRANCH; Michael Allen; (Spring, TX) ;
DELANEY-KINSELLA; Cynthia; (Houston, TX) ; LIPINSKY;
Dana Tatum; (Houston, TX) ; KRAUS; Lawrence
Stephen; (Dickinson, TX) ; BRUMFIELD; Tommy
Louis; (Spring, TX) ; BRU; Ariel; (Rijswijk,
NL) ; STEERNBERG; Koen; (Amsterdam, NL) ;
BOUDREAUX; Shannon; (Deer Park, TX) ; TARDIFF;
Pierre; (Houston, TX) |
|
Applicant: |
Name |
City |
State |
Country |
Type |
SHELL OIL COMPANY |
Houston |
TX |
US |
|
|
Family ID: |
50979696 |
Appl. No.: |
14/665111 |
Filed: |
March 23, 2015 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
|
62002005 |
May 22, 2014 |
|
|
|
Current U.S.
Class: |
585/13 |
Current CPC
Class: |
C10L 1/04 20130101; C10L
2200/0438 20130101; C10G 2300/302 20130101; C10G 2300/304 20130101;
C10G 2300/202 20130101; C10G 2300/203 20130101; C10L 2200/043
20130101; C10L 1/08 20130101; C10L 10/02 20130101; C10L 2200/0453
20130101; C10L 2270/026 20130101; C10L 2200/0469 20130101; C10L
2270/02 20130101; C10G 2300/308 20130101 |
International
Class: |
C10L 1/04 20060101
C10L001/04; C10L 10/02 20060101 C10L010/02 |
Foreign Application Data
Date |
Code |
Application Number |
Jun 24, 2014 |
EP |
14173748.6 |
Claims
1. A marine fuel composition comprising: greater than 50 wt % to 90
wt % of a residual hydrocarbon component comprising an atmospheric
tower bottoms (ATB) residues with a kinematic viscosity at
.about.50 degrees C. of at least 100 cSt; and wherein the marine
fuel composition has a kinematic viscosity at .about.50 degrees C.
of at least 10 cSt.
2. The marine fuel composition of claim 1 wherein the sulphur
content of the marine fuel composition is in a range of 400 to 1000
wppm.
3. The marine fuel composition of claim 1 which exhibits at least
one of the following: a hydrogen sulfide content of at most 2.0
mg/kg; an acid number of at most 2.5 mg KOH per gram; a sediment
content of at most 0.1 wt %; a water content of at most 0.5 vol %;
and an ash content of at most 0.15 wt %.
4. The marine fuel composition of claim 1 which has at least one of
the following: a density at 15 degrees C. in a range of 0.870 to
1.010 g/cm.sup.3, a pour point of .about.30 to 35 degrees C., and a
flash point of at least 60 degrees C.
5. (canceled)
6. The marine fuel composition of claim 1 wherein the residual
hydrocarbon component further comprises vacuum tower bottoms (VTB)
residues.
7. The marine fuel composition of claim 1 wherein the atmospheric
tower bottoms (ATB) residues which exhibit at least one of the
following: a pour point in a range of -19.0 to 64 degrees C., a
flash point in a range of 80 to 213 degrees C.; an acid number of
up to 8.00 mgKOH/g; and a density at .about.15 degrees C. of at
most about 1.0 g/cc.
8. The marine fuel composition of claim 1 wherein the residual
hydrocarbon component comprises a first atmospheric tower bottoms
(ATB) residues which exhibits at least one of the following a pour
point of about 45 degrees C., a flash point of about 124 degrees
C.; a density at .about.15 degrees C. of about 0.91 g/cm.sup.3, and
a kinematic viscosity at .about.50 degrees C. of at least 165
cSt.
9. The marine fuel composition of claim 8 wherein the residual
hydrocarbon component comprises a second atmospheric tower bottoms
(ATB) residues which exhibits at least one of the following a pour
point of about -2 degrees C., a flash point of about 207 degrees
C.; a density at .about.15 degrees C. of about 0.94 g/cm.sup.3, and
a kinematic viscosity at .about.50 degrees C. of at least 880
cSt.
10. The marine fuel composition of claim 9 comprising at least 20
wt % of the first atmospheric tower bottoms (ATB) residues and at
least 30 wt % of the second atmospheric tower bottoms (ATB)
residues.
11. (canceled)
12. (canceled)
13. The marine fuel composition of claim 6 wherein the vacuum tower
bottoms (VTB) residues exhibit at least one of the following: a
density at 15 degrees C. in a range of 0.8 to 1.1 g/cc; a pour
point in a range of -15.0 to 95 degrees C., a flash point in a
range of 220 to 335 degrees C.; an acid number of up to 8.00
mgKOH/g; and a kinematic viscosity at 50 degrees C. in a range of
3.75 to 15000 cSt.
14. (canceled)
15. The marine fuel composition of claim 1 further comprising a
non-hydroprocessed hydrocarbon component comprising at least one of
vacuum gas oil (VGO), coker diesel, coker gas oil, coker VGO,
thermally cracked VGO, thermally cracked diesel, thermally cracked
gas oil, Group I slack waxes, lube oil aromatic extracts, and
deasphalted oil (DAO).
16. (canceled)
17. The marine fuel composition of claim 1 further comprising a
hydroprocessed hydrocarbon component comprising at least one of
hydrotreated coker diesel, hydrotreated coker gas oil, hydrotreated
thermally cracked diesel, hydrotreated VGO, hydrotreated coker VGO,
hydrotreated residues, hydrocracker bottoms, hydrotreated thermally
cracked VGO, and hydrotreated DAO.
18. The marine fuel composition of claim 1 further comprising a
non-hydroprocessed hydrocarbon component comprising at least one of
light cycle oil (LCO), heavy cycle oil (HCO), fluid catalytic
cracking (FCC) cycle oil, FCC slurry oil, pyrolysis gas oil,
cracked light gas oil (CLGO), cracked heavy gas oil (CHGO),
pyrolysis light gas oil (PLGO), pyrolysis heavy gas oil (PHGO),
thermally cracked residue, thermally cracked heavy distillate, and
coker heavy distillates.
19. The marine fuel composition of claim 1 further comprising a
hydroprocessed hydrocarbon component comprising at least one of
low-sulfur diesel (LSD) having a sulphur content of less than 500
wppm, ultra low-sulfur diesel (ULSD) having a sulphur HL: CRC
content of less than 15 wppm; hydrotreated light cycle oil (LCO);
hydrotreated heavy cycle oil (HCO); hydrotreated pyrolysis gas oil,
hydrotreated thermally cracked heavy distillate, hydrotreated
thermally cracked gas oil, and hydrocracker diesel.
20. The marine fuel composition of claim 1 with a micro carbon
residue of greater than 0.30% m/m.
21. The marine fuel composition of claim 1 wherein at least 10 wt %
of the residual hydrocarbon component has a boiling point of at
least 435 degrees C.
22. A marine fuel composition comprising: greater than 50 wt % to
90 wt % of a residual hydrocarbon component comprising a vacuum
tower bottoms (VTB) residues with a kinematic viscosity at
.about.50 degrees C. of at least 100 cSt; and wherein the marine
fuel composition has a kinematic viscosity at .about.50 degrees C.
of at least 10 cSt.
23. The marine fuel composition of claim 22 further comprising: at
least 10 wt % of a non-hydroprocessed hydrocarbon component
comprising at least one of light cycle oil (LCO), heavy cycle oil
(HCO), fluid catalytic cracking (FCC) cycle oil, FCC slurry oil,
pyrolysis gas oil, cracked light gas oil (CLGO), cracked heavy gas
oil (CHGO), pyrolysis light gas oil (PLGO), pyrolysis heavy gas oil
(PHGO), thermally cracked residue, thermally cracked heavy
distillate, and coker heavy distillates.
24. The marine fuel composition of claim 22 further comprising: at
least 10 wt % of a hydroprocessed hydrocarbon component comprising
at least one of low-sulfur diesel (LSD) having a sulphur content of
less than 500 wppm, ultra low-sulfur diesel (ULSD) having a sulphur
content of less than 15 wppm; hydrotreated light cycle oil (LCO);
hydrotreated heavy cycle oil (HCO); hydrotreated pyrolysis gas oil,
hydrotreated thermally cracked heavy distillate, hydrotreated
thermally cracked gas oil, and hydrocracker diesel.
25. The marine fuel composition of claim 22 wherein the residual
hydrocarbon component has a sulfur content of at most 0.4 wt %.
26. The marine fuel composition of claim 22 with a micro carbon
residue of greater than 0.30% m/m.
27. The marine fuel composition of claim 22 wherein at least 10 wt
% of the residual hydrocarbon component has a boiling point of at
least 435 degrees C.
Description
[0001] This non-provisional application claims the benefit of U.S.
Provisional Application No. 62/002,005, filed May 22, 2014 and,
claims priority to European Patent Application No. 14173748.6,
filed Jun. 24, 2014, the disclosures of which are incorporated
herein by reference.
BACKGROUND
[0002] This section is intended to introduce various aspects of the
art, which may be associated with exemplary embodiments of the
present invention. This discussion is believed to assist in
providing a framework to facilitate a better understanding of
particular aspects of the present invention. Accordingly, it should
be understood that this section should be read in this light, and
not necessarily as admissions of any prior art.
[0003] The present disclosure generally relates to marine fuel
compositions, specifically marine fuel compositions comprising at
least one residual hydrocarbon component.
[0004] Marine vessels used in global shipping typically run on
marine fuels, which can also be referred to as bunker fuels. Marine
fuels include distillate-based and residues-based ("resid-based")
marine fuels. Resid-based marine fuels are usually preferred
because they tend to cost less than other fuels, but they often,
and typically, have higher sulfur levels due to the cracked and/or
residual hydrocarbon components that typically make up the
resid-based marine fuels. The International Maritime Organization
(IMO), however, imposes increasingly more stringent requirements on
sulfur content of marine fuels used globally. In addition, IMO
imposes more strict marine fuel sulfur levels in specific regions
known as Emission Control Areas, or ECAs. The regulations will
require a low-sulfur marine fuel with a maximum sulfur content of
0.1 wt % (1000 wppm) for the ECA in the near future. One
conventional way of meeting the lower sulfur requirements for
marine vessels is through the use of distillate-based fuels (e.g.,
diesel) with sulfur levels typically significantly below the sulfur
levels specified in the IMO regulations. The distillate-based
fuels, however, typically have a high cost premium and limited
flexibility in blending components. For instance, use of heavy and
highly aromatic components in a distillate-based low-sulfur marine
fuel is limited because of the density, MCR content, appearance
(color), and cetane specifications imposed on marine distillate
fuels. A distinct advantage that resid-based marine fuel oils have
over distillate-based marine fuels is that they can incorporate
heavy and aromatic components into their formulations because of
their product specifications. This allows more flexible use of
available blending components for marine fuel oil production and
results in lower cost fuels. Further, the use of heavy and highly
aromatic components possible in resid-based marine fuel blends
allows higher density fuels to be produced.
[0005] While there are some publications that disclose the
desirability of lowering the sulfur content of marine fuels, there
is still a need for low-sulfur marine fuels with at least one
residual hydrocarbon component. Exemplary publications include U.S.
Pat. Nos. 4,006,076, and 7,651,605, and WO2012135247.
SUMMARY
[0006] According to one aspect, the present disclosure provides a
marine fuel composition comprising: 50 to 90 wt % of a residual
hydrocarbon component; and 10 to 50 wt % selected from a group
consisting of a non-hydroprocessed hydrocarbon component, a
hydroprocessed hydrocarbon component, and any combination thereof.
In some embodiments, the sulphur content is in a range of 400 to
1000 wppm. Additionally or alternately, the marine fuel composition
exhibits at least one of the following characteristics: a hydrogen
sulfide content of at most 2.0 mg/kg; an acid number of at most 2.5
mg KOH per gram; a sediment content of at most 0.1 wt %; a water
content of at most 0.5 vol %; and an ash content of at most 0.15 wt
%. Additionally or alternately, the marine fuel composition has at
least one of the following: a density at 15 degrees C. in a range
of 0.870 to 1.010 g/cm.sup.3, a kinematic viscosity at 50 degrees
C. in a range of 1 to 700 cSt, a pour point of -30 to 35 degrees
C., and a flash point of at least 60 degrees C. In some
embodiments, the residual hydrocarbon component has a sulfur
content of at least 0.4 wt %, at least 0.2 wt %, at most 0.4 wt %
or at most 0.2 wt %.
[0007] In some embodiments, the residual hydrocarbon component is
selected from a group consisting of long residues (ATB), short
residues (VTB), and a combination thereof. In some embodiments, the
residual hydrocarbon component comprises long residues (ATB) which
exhibit at least one of the following: a pour point in a range of
.about.19.0 to 64 degrees C., a flash point in a range of 80 to 213
degrees C.; an acid number of up to 8.00 mgKOH/g; a density at
.about.15 degrees C. of at most about 1.1 g/cc; and a kinematic
viscosity at .about.50 degrees C. in a range of 1.75 to 15000 cSt.
In some embodiments, the residual hydrocarbon component comprises a
first long residue (ATB) which exhibits at least one of the
following a pour point of about 45 degrees C, a flash point of
about 124 degrees C.; a density at .about.15 degrees C. of about
0.91 g/cm.sup.3, and a kinematic viscosity at .about.50 degrees C.
of about 165 cSt.
[0008] In some embodiments, the marine fuel composition comprises
at least 60% of the first long residue. In some embodiments, the
residual hydrocarbon component comprises a second long residue
(ATB) which exhibits at least one of the following a pour point of
about .about.2 degrees C., a flash point of about 207 degrees C.; a
density at .about.15 degrees C. of about 0.94 g/cm.sup.3, and a
kinematic viscosity at .about.50 degrees C. of about 880 cSt. In
some embodiments, the marine fuel composition comprises at least 20
wt % of the first long residue and at least 30% of the second long
residue. In some embodiments, the marine fuel composition comprises
at least 32 wt % of the second long residue. In some embodiments,
the marine fuel composition comprises at least 32% of the first
long residue. In some embodiments, the marine fuel composition
comprises at least 60 wt % of the residual hydrocarbon component.
In some embodiments, the marine fuel composition comprises at least
70 wt % of the residual hydrocarbon component. In some embodiments,
the marine fuel composition comprises at least 80 wt % of the
residual hydrocarbon component. In some embodiments, the marine
fuel composition comprises at least 90 wt % of the residual
hydrocarbon component.
[0009] In some embodiments, the residual hydrocarbon component
comprises short residues (VTB) which exhibit at least one of the
following: a density at 15 degrees C. in a range of 0.8 to 1.1
g/cc; a pour point in a range of .about.15.0 to 95 degrees C., a
flash point in a range of 220 to 335 degrees C.; an acid number of
up to 8.00 mgKOH/g; and a kinematic viscosity at 50 degrees C. in a
range of 3.75 to 15000 cSt. In some embodiments, the
non-hydroprocessed hydrocarbon component is selected from a group
consisting of light cycle oil (LCO), heavy cycle oil (HCO), fluid
catalytic cracking (FCC) cycle oil, FCC slurry oil, pyrolysis gas
oil, cracked light gas oil (CLGO), cracked heavy gas oil (CHGO),
pyrolysis light gas oil (PLGO), pyrolysis heavy gas oil (PHGO),
thermally cracked residue, thermally cracked heavy distillate,
coker heavy distillates, and any combination thereof. In some
embodiments, the marine fuel composition wherein the
non-hydroprocessed hydrocarbon component is selected from a group
consisting of vacuum gas oil (VGO), coker diesel, coker gas oil,
coker VGO, thermally cracked VGO, thermally cracked diesel,
thermally cracked gas oil, Group I slack waxes, lube oil aromatic
extracts, deasphalted oil (DAO), and any combination thereof. In
some embodiments, the non-hydroprocessed hydrocarbon component is
selected from a group consisting of coker kerosene, thermally
cracked kerosene, gas-to-liquids (GTL) wax, GTL hydrocarbons,
straight-run diesel, straight-run kerosene, straight run gas oil
(SRGO), and any combination thereof. In some embodiments, the
hydroprocessed hydrocarbon component is selected from a group
consisting of low-sulfur diesel (LSD) having a sulphur content of
less than 500 wppm, ultra low-sulfur diesel (ULSD) having a sulphur
content of less than 15 wppm; hydrotreated LCO; hydrotreated HCO;
hydrotreated FCC cycle oil; hydrotreated pyrolysis gas oil,
hydrotreated PLGO, hydrotreated PHGO, hydrotreated CLGO,
hydrotreated CHGO, hydrotreated coker heavy distillates,
hydrotreated thermally cracked heavy distillate, hydrotreated
diesel oil, and any combination thereof.
[0010] In some embodiments, the hydroprocessed hydrocarbon
component is selected from a group consisting of hydrotreated coker
diesel, hydrotreated coker gas oil, hydrotreated thermally cracked
diesel, hydrotreated thermally cracked gas oil, hydrotreated VGO,
hydrotreated coker VGO, hydrotreated residues, hydrocracker
bottoms, hydrotreated thermally cracked VGO, and hydrotreated
hydrocracker DAO, and any combination thereof. In some embodiments,
the hydroprocessed hydrocarbon component is selected from a group
consisting of ultra low sulfur kerosene (ULSK), hydrotreated jet
fuel, hydrotreated kerosene, hydrotreated coker kerosene,
hydrocracker diesel, hydrocracker kerosene, hydrotreated thermally
cracked kerosene, and any combination thereof.
[0011] Advantages and other features of embodiments of the present
invention will become apparent from the following detailed
description. It should be understood, however, that the detailed
description and the specific examples, while indicating preferred
embodiments of the invention, are given by way of illustration
only, since various changes and modifications within the spirit and
scope of the invention will become apparent to those skilled in the
art from this detailed description.
DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS
[0012] The present disclosure generally relates to marine fuels,
specifically marine fuels with low sulfur content comprising at
least one residual hydrocarbon component. The present disclosure
provides a marine fuel that has a residual hydrocarbon component in
an amount in a range of greater than 50 wt % to 90 wt %. The fuel
compositions provided by the present disclosure are able to meet
the low-sulfur requirements as well as meet fuels standard
specifications, such as the marine fuels standard ISO 8217 (2010).
Such fuels standard specifications are part of common general
knowledge in the art. For instance, in the marine fuels field, it
is known that ISO 8217 provides standard specifications: one set of
specifications for marine distillate fuel and a separate set of
specifications for marine residual fuel. While it is part of the
common general knowledge, the ISO 8217 (2010) specifications for
various types of marine fuels are reproduced below.
TABLE-US-00001 ISO 8217 2010 FUEL STANDARD ISO 8217 2010 Fuel
Standard for marine distillate fuels MARINE DISTILLATE FUELS Limit
Parameter DMX DMA DMZ DMB Max Viscosity at 40.degree. C.
(mm.sup.2/s) 5.500 6.000 6.000 11.00 Min. Viscosity at 40.degree.C.
(mm.sup.2/s) 1.400 2.000 3.000 2.000 Max. Micro Carbon Residues at
10% Residue (% m/m) 0.30 0.30 0.30 -- Max. Density at 15.degree. C.
(kg/m3) -- 890.0 890.0 900.0 Max. Micro Carbon Residue (% m/m) --
-- -- 0.30 Max. Sulphur (% m/m) 1.00 1.50 1.50 2.00 Max. Water (%
V/V) -- -- -- 0.30 Max. Total sediment by hot filtration (% m/m) --
-- -- 0.10 Max. Ash (% m/m) 0.010 0.010 0.010 0.010 Min. Flash
point (0.degree. C.) 43.0 60.0 60.0 60.0 Max. Pour point in Summer
(0.degree. C.) -- 0 0 6 Max. Pour point in Winter (.degree. C.) --
-6 -6 0 Max. Cloud point (.degree. C.) -16 -- -- -- Min. Calculated
Cetane Index 45 40 40 35 Max. Add Number (mgKOH/g) 0.5 0.5 0.5 0.5
Max. Oxidation stability (g/m.sup.3) 25 25 25 25 Max. Lubricity
corrected wear scar diameter (wsd 1.4 at 60.degree. C.) (um) 520
520 520 520 Max. Hydrogen sulphide (mg/kg) 2.00 2.00 2.00 2.00
Appearance Clear & Bright --
[0013] In one embodiment, one property of the marine fuel
composition is a density at 15 degrees C. of greater than 830
kg/m.sup.3 as measured by a suitable standard method known to one
of ordinary skill in the art, such as ASTM D4052. The marine fuel
composition preferably meets the marine residual fuels standard of
ISO 8217 (2010).
[0014] The marine fuel preferably has a micro carbon residue of
greater than 0.30% m/m, as measured by a suitable standard method
known to one of ordinary skill in the art, such as ASTM D4530 or
ISO 10370. In particular, the marine fuel has a micro carbon
residue of at least 0.50% m/m, at least 1.00% m/m, at least 1.50%
m/m, at least 2.00% m/m, at least 2.50% m/m, at least 3.00% m/m, at
least 3.50% m/m, at least 4.00% m/m, at least 4.50% m/m, at least
5.00% m/m, at least 5.50% m/m, at least 6.00% m/m, at least 6.50%
m/m, at least 7.00% m/m, at least 7.50% m/m, at least 8.00% m/m, at
least 8.50% m/m, at least 9.00% m/m, at least 9.50% m/m, at least
10.00% m/m, at least 10.50% m/m, at least 11.00% m/m, at least
11.50% m/m, at least 12.00% m/m, at least 12.50% m/m, at least
13.00% m/m, at least 13.50% m/m, at least 14.00% m/m, at least
14.50% m/m, at least 15.00% m/m, at least 15.50% m/m, at least
16.00% m/m, at least 16.50% m/m, at least 17.00% m/m, at least
17.50% m/m, at least 18.00% m/m, at least 18.50% m/m, at least
19.00% m/m, at least 19.50% m/m, or at least 20.00% m/m. In another
instance, the marine fuel has a micro carbon residue of at most
2.50% m/m, at most 10.00% m/m, at most 14.00% m/m, at most 15.00%
m/m, at most 18.00% m/m, or at most 20.00% m/m. Preferably, the
marine fuel can have a micro carbon number in a range of greater
than 0.30% m/m and 20.00% m/m, particularly any amount or range in
between as specified here or otherwise.
[0015] Carbon residue tests, such as the Micro Carbon Residue (MCR)
Test or the ASTM test for Conradson Carbon Residue (CCR), are
primarily used on residual fuels since the distillate fuels that
are satisfactory in other respects do not have high amounts of
carbon residue. It is understood that the MCR and CCR tests are
also used for distillate fuels to confirm that they contain an
acceptable amount of carbon residue content below a specified
level. This is reflected in the ISO 8217 limiting the amount of
micro carbon residue to a maximum of 0.30% m/m for marine
distillate fuels. Because of the difference in the MCR and CCR
results between distillate and residual fuels, the MCR and CCR
tests can be used as an indication of contamination of distillate
fuel by residual fuel.
[0016] As mentioned, the marine fuel composition described herein
comprises in a range of greater than 50 to 90 wt % of a residual
hydrocarbon component and at least about 10 to less than 50 wt % of
other components selected from the group consisting of a
non-hydroprocessed hydrocarbon component, a hydroprocessed
hydrocarbon component, and a combination thereof. According to one
aspect, the amount and material of the residual hydrocarbon
component may be selected first, and the amount and material of the
non-hydroprocessed hydrocarbon component and/or hydroprocessed
hydrocarbon component can be determined based on their properties
in view of the residual hydrocarbon component selection to form a
marine fuel composition that meets the desired application, such as
to meet a particular specification or regulation requirement.
[0017] In one embodiment, the marine fuel composition includes a
residual hydrocarbon component in a range of about 50 to 90 wt %
while still maintaining the sulfur content to meet regulations. In
some embodiments, the marine fuel composition comprises about 50 to
90 wt %, of the residual hydrocarbon component. For example, the
marine fuel composition may comprise at least 50 wt %, at least 55
wt %, at least 60 wt %, at least 65 wt %, at least 70 wt %, at
least 75 wt %, at least 80 wt %, at least 85 wt %, and 90 wt %. The
marine fuel composition may comprise at most about 90 wt %, for
example, at most 85 wt %, at most 80 wt %, at most 75 wt %, at most
70 wt %, at most 65 wt %, at most 60 wt %, at most 55 wt %, or 50
wt %. In one embodiment, the marine fuel composition comprises
greater than 50 wt % of the residual hydrocarbon component. The
residual hydrocarbon component can include any suitable residual
hydrocarbon component, including long residues, short residues, or
a combination thereof. The term "residual" or "residual hydrocarbon
component" is understood to refer to residues that remain from
distillation processes; that is, materials which are not distilled
as an overhead or distillate fraction and remain behind in the
distillation tower. For instance, a residual hydrocarbon component
can include residues obtained as residues in the distillation of
crude mineral oil under atmospheric pressure, producing straight
run distillate fractions and a first residual oil, which is called
"long residue" (or atmospheric tower bottoms (ATB)). The long
residue is usually distilled at sub-atmospheric pressure to yield
one or more so called "vacuum distillates" and a second residual
oil, which is called "short residue" (or vacuum tower bottoms
(VTB)).
[0018] In a particular embodiment, the residual hydrocarbon
component used has a sulfur content of less than about 0.4 wt %,
for example, less than about 0.2 wt %. The residual hydrocarbon
component with a sulfur content of less than about 0.4 wt % may be
selected from at least one of long residues (ATB) and short
residues (VTB). Preferably, at least 10.0 wt % of the residual
hydrocarbon component has a boiling point of at least 435 degrees
C., such as at least 12.5 wt %, at least 15.0 wt %, at least 17.5
wt %, or at least 20.0 wt % of the residual hydrocarbon component
has a boiling point of at least 435 degrees C.
[0019] The residual hydrocarbon component preferably has a micro
carbon residue of at least 0.10% m/m, at least 0.15% m/m, at least
0.20% m/m, at least 0.25% m/m, at least 0.30% m/m, at least 0.35%
m/m, at least 4.0% m/m, of at least 0.50% m/m, at least 1.00% m/m,
at least 1.50% m/m, at least 2.00% m/m, at least 2.50% m/m, at
least 3.00% m/m, at least 3.50% m/m, at least 4.00% m/m, at least
4.50% m/m, at least 5.00% m/m, at least 5.50% m/m, at least 6.00%
m/m, at least 6.50% m/m, at least 7.00% m/m, at least 7.50% m/m, at
least 8.00% m/m, at least 8.50% m/m, at least 9.00% m/m, at least
9.50% m/m, at least 10.00% m/m, at least 10.50% m/m, at least
11.00% m/m, at least 11.50% m/m, at least 12.00% m/m, at least
12.50% m/m, at least 13.00% m/m, at least 13.50% m/m, at least
14.00% m/m, at least 14.50% m/m, at least 15.00% m/m, at least
15.50% m/m, at least 16.00% m/m, at least 16.50% m/m, at least
17.00% m/m, at least 17.50% m/m, at least 18.00% m/m, at least
18.50% m/m, at least 19.00% m/m, at least 19.50% m/m, or at least
20.00% m/m. The residual hydrocarbon component can also have a
micro carbon residue of at most 1.5% m/m, at most 2.00% m/m, at
most 2.50% m/m, at most 5.00% m/m, at most 7.50% m/m, at most
10.00% m/m, at most 12.50% m/m, at most 15.00% m/m, at most 17.50%
m/m, or at most 20.00% m/m. Preferably, the residual hydrocarbon
component can have a micro carbon number in a range of 0.10% m/m
and 20.00% m/m, such as in a range of greater than 0.30% m/m and
20.00% m/m, including any amount or range in between as specified
here or otherwise.
[0020] The long residues (ATB) may exhibit one or more of the
following properties: a density at .about.15 degrees C. of at most
about 1.0 g/cc (or g/cm.sup.3), for example, at most 0.95 g/cc, at
most 0.90 g/cc, at most 0.85 g/cc, at most 0.80 g/cc, at most 0.75
g/cc, or at most 0.70 g/cc; a density at .about.15 degrees C. of at
least about 0.70 g/cc, for example, at least 0.75 g/cc, at least
0.80 g/cc, at least 0.85 g/cc, at least 0.90 g/cc, at least 0.95
g/cc, or at least 1.0 g/cc; a sulfur content of about at most 0.40
wt %, at most 0.35 wt %, at most 0.30 wt %, at most 0.25 wt %, at
most 0.20 wt %, at most 0.15 wt %, at most 0.10 wt %, at most 0.05
wt %, or at most 0.01 wt %; a sulfur content of about at least 0.01
wt %, at least 0.05 wt %, at least 0.10 wt %, at least 0.15 wt %,
at least 0.20 wt %, at least 0.25 wt %, at least 0.30 wt %, at
least 0.35 wt %, or at least 0.40 wt %; a pour point of at least
about -20.0 degrees C., such as -19.0 degrees C., for example, at
least -15.0 degrees C., at least -10.0 degrees C., at least -5.0
degrees C., at least 0.0 degrees C., at least 5.0 degrees C., at
least 10.0 degrees C., at least 15.0 degrees C., at least 20.0
degrees C., at least 25.0 degrees C., at least 30.0 degrees C., at
least 35.0 degrees C., at least 40.0 degrees C., at least 45.0
degrees C., at least 50.0 degrees C., at least 55.0 degrees C., or
at least 60.0 degrees C., such as 64.0 degrees C.; a pour point of
at most about 65.0 degrees C., such as 64.0 degrees C., for
example, at most 60.0 degrees C., at most 55.0 degrees C., at most
50.0 degrees C., at most 45.0 degrees C., at most 40.0 degrees C.,
at most 35.0 degrees C., at most 30.0 degrees C., at most 25.0
degrees C., at most 20.0 degrees C., at most 15.0 degrees C., at
most 10.0 degrees C., at most 5.0 degrees C., at most 0.0 degrees
C., at most -5.0 degrees C., at most -10.0 degrees C., at most
-15.0 degrees C., such as -19.0 degrees C., or at most -20.0
degrees C.; a flash point of at least about 80 degrees C., for
example, at least 85 degrees C., at least 90 degrees C., at least
95 degrees C., at least 100 degrees C., at least 105 degrees C., at
least 110 degrees C., at least 115 degrees C., at least 120 degrees
C., at least 125 degrees C., at least 130 degrees C., at least 135
degrees C., at least 140 degrees C., at least 145 degrees C., at
least 150 degrees C., at least 155 degrees C., at least 160 degrees
C., at least 165 degrees C., at least 170 degrees C., at least 175
degrees C., at least 180 degrees C., at least 185 degrees C., at
least 190 degrees C., at least 195 degrees C., at least 200 degrees
C., at least 205 degrees C., or at least 210 degrees C., such as
213 degrees C.; a flash point of at most about 213 degrees C., for
example, at most 210 degrees C., at most 205 degrees C., at most
200 degrees C., at most 195 degrees C., at most 190 degrees C., at
most 185 degrees C., at most 180 degrees C., at most 175 degrees
C., at most 170 degrees C., at most 165 degrees C., at most 160
degrees C., at most 155 degrees C., at most 150 degrees C., at most
145 degrees C., at most 140 degrees C., at most 135 degrees C., at
most 130 degrees C., at most 125 degrees C., at most 120 degrees
C., at most 115 degrees C., at most 110 degrees C., at most 105
degrees C., at most 100 degrees C., at most 95 degrees C., at most
90 degrees C., at most 85 degrees C., or at most 80 degrees C.; a
total acid number (TAN) of up to about 8.00 mgKOH/g, for example,
at most about 7.50 mgKOH/g, at most 7.00 mgKOH/g, at most 6.50
mgKOH/g, at most 6.00 mgKOH/g, at most 5.50 mgKOH/g, at most 5.00
mgKOH/g, at most 4.50 mgKOH/g, at most 4.00 mgKOH/g, at most 3.50
mgKOH/g, at most 3.00 mgKOH/g, at most 2.50 mgKOH/g, at most 2.00
mgKOH/g, at most 1.50 mgKOH/g, at most 1.00 mgKOH/g, at most 0.50
mgKOH/g, at most 0.10 mgKOH/g, or at most 0.05 mgKOH/g; a total
acid number (TAN) of at least about 0.05 mgKOH/g, for example, at
least 0.10 mgKOH/g, at least 0.50 mgKOH/g, at least 1.00 mgKOH/g,
at least 1.50 mgKOH/g, at least 2.00 mgKOH/g, at least 2.50
mgKOH/g, at least 3.00 mgKOH/g, at least 3.50 mgKOH/g, at least
4.00 mgKOH/g, at least 4.50 mgKOH/g, at least 5.00 mgKOH/g, at
least 5.50 mgKOH/g, at least 6.00 mgKOH/g, at least 6.50 mgKOH/g,
at least 7.00 mgKOH/g, at least 7.50 mgKOH/g, or at least 8.00
mgKOH/g; a kinematic viscosity at .about.50 degrees C. of at least
about 1.75 cSt, for example, at least 100 cSt, at least 500 cSt, at
least 1000 cSt, at least 1500 cSt, at least 2000 cSt, at least 2500
cSt, at least 3000 cSt, at least 3500 cSt, at least 4000 cSt, at
least 4500 cSt, at least 5000 cSt, at least 5500 cSt, at least 6000
cSt, at least 6500 cSt, at least 7000 cSt, at least 7500 cSt, at
least 8000 cSt, at least 8500 cSt, at least 9000 cSt, at least 9500
cSt, at least 10000 cSt, at least 10500 cSt, at least 11000 cSt, at
least 11500 cSt, at least 12000 cSt, at least 12500 cSt, at least
13000 cSt, at least 13500 cSt, at least 14000 cSt, at least 14500
cSt, or at least 15000 cSt; a kinematic viscosity at .about.50
degrees C. of at most about 15000 cSt, for example, at most 14500
cSt, at most 14000 cSt, at most 13500 cSt, at most 13000 cSt, at
most 12500 cSt, at most 12000 cSt, at most 11500 cSt, at most 11000
cSt, at most 10500 cSt, at most 10000 cSt, at most 9500 cSt, at
most 9000 cSt, at most 8500 cSt, at most 8000 cSt, at most 7500
cSt, at most 7000 cSt, at most 6500 cSt, at most 6000 cSt, at most
5500 cSt, at most 5000 cSt, at most 4500 cSt, at most 4000 cSt, at
most 3500 cSt, at most 3000 cSt, at most 2500 cSt, at most 2000
cSt, at most 1500 cSt, at most 1000 cSt, at most 500 cSt, at most
100 cSt, or at most 1.75 cSt.
[0021] The long residues (ATB) can have a similar micro carbon
residue number as that provided above for the residual hydrocarbon
component. For instance, the long residues (ATB) can have a micro
carbon residue number of at least 0.10% m/m, at least 0.15% m/m, at
least 0.20% m/m, at least 0.25% m/m, at least 0.30% m/m, at least
0.35% m/m, at least 4.0% m/m, of at least 0.50% m/m, at least 1.00%
m/m, at least 1.50% m/m, at least 2.00% m/m, at least 2.50% m/m, at
least 3.00% m/m, at least 3.50% m/m, at least 4.00% m/m, at least
4.50% m/m, at least 5.00% m/m, at least 5.50% m/m, at least 6.00%
m/m, at least 6.50% m/m, at least 7.00% m/m, at least 7.50% m/m, at
least 8.00% m/m, at least 8.50% m/m, at least 9.00% m/m, at least
9.50% m/m, at least 10.00% m/m, at least 10.50% m/m, at least
11.00% m/m, at least 11.50% m/m, at least 12.00% m/m, at least
12.50% m/m, at least 13.00% m/m, at least 13.50% m/m, at least
14.00% m/m, at least 14.50% m/m, at least 15.00% m/m, at least
15.50% m/m, at least 16.00% m/m, at least 16.50% m/m, at least
17.00% m/m, at least 17.50% m/m, at least 18.00% m/m, at least
18.50% m/m, at least 19.00% m/m, at least 19.50% m/m, or at least
20.00% m/m. The long residues (ATB) can also have a micro carbon
residue of at most 1.5% m/m, at most 2.00% m/m, at most 2.50% m/m,
at most 5.00% m/m, at most 7.50% m/m, at most 10.00% m/m, at most
12.50% m/m, at most 15.00% m/m, at most 17.50% m/m, or at most
20.00% m/m. Preferably, the long residues (ATB) can have a micro
carbon number in a range of 0.10% m/m and 20.00% m/m, such as in a
range of greater than 0.30% m/m and 20.00% m/m, including any
amount or range in between as specified here or otherwise. Also,
preferably, at least 10 wt % of the long residues (ATB) can also
have a boiling point of at least 435 degrees C., including at least
12.5 wt %, at least 15 wt %, at least 17.5 wt %, or at least 20 wt
% of the long residues (ATB) can also have a boiling point of at
least 435 degrees C.
[0022] The short residues (VTB) may exhibit one or more of the
following properties: a density at .about.15 degrees C. of at most
about 1.1 g/cc, for example, at most 1.05 g/cc, at most 1.00 g/cc,
at most 0.95 g/cc, at most 0.90 g/cc, at most 0.85 g/cc, or at most
0.80 g/cc; a density at .about.15 degrees C. of at least about 0.80
g/cc, for example, at least 0.85 g/cc, at least 0.90 g/cc, at least
0.95 g/cc, at least 1.0 g/cc, at least 1.05 g/cc, or at least 1.10
g/cc; a sulfur content of about at most 0.40 wt %, at most 0.35 wt
%, at most 0.30 wt %, at most 0.25 wt %, at most 0.20 wt %, at most
0.15 wt %, at most 0.10 wt %, at most 0.05 wt %, or at most 0.01 wt
%; a sulfur content of about at least 0.01 wt %, at least 0.05 wt
%, at least 0.10 wt %, at least 0.15 wt %, at least 0.20 wt %, at
least 0.25 wt %, at least 0.30 wt %, at least 0.35 wt %, or at
least 0.40 wt %; a pour point in a range of at least -15.0 degrees
C., for example, at least -15.0 degrees C., at least -10 degrees
C., at least -5 degrees C., at least 0.0 degrees C., at least 5.0
degrees C., at least 10.0 degrees C., at least 15.0 degrees C., at
least 20.0 degrees C., at least 25.0 degrees C., at least 30.0
degrees C., at least 35.0 degrees C., at least 40.0 degrees C., at
least 45.0 degrees C., at least 50.0 degrees C., at least 55.0
degrees C., at least 60.0 degrees C. at least 65.0 degrees C., at
least 70.0 degrees C., at least 75.0 degrees C., at least 80.0
degrees C., at least 85.0 degrees C., at least 90.0 degrees C., or
at least 95.0 degrees C.; a pour point of at most about 95.0
degrees C., for example, at most 90.0 degrees C., at most 85.0
degrees C., at most 80.0 degrees C., at most 75.0 degrees C., at
most 70.0 degrees C., at most 65.0 degrees C., at most 60.0 degrees
C., at most 55.0 degrees C., at most 50.0 degrees C., at most 45.0
degrees C., at most 40.0 degrees C., at most 35.0 degrees C., at
most 30.0 degrees C., at most 25.0 degrees C., at most 20.0 degrees
C., at most 15.0 degrees C., at most 10.0 degrees C., at most 5.0
degrees C., at most 0.0 degrees C., at most -5.0 degrees C., at
most -10 degrees C., at most -15.0 degrees C.; a flash point of at
least about 220 degrees C., for example, at least 225 degrees C.,
at least 230 degrees C., at least 235 degrees C., at least 240
degrees C., at least 245 degrees C., at least 250 degrees C., at
least 255 degrees C., at least 260 degrees C., at least 265 degrees
C., at least 270 degrees C., at least 275 degrees C., at least 280
degrees C., at least 285 degrees C., at least 290 degrees C., at
least 295 degrees C., at least 300 degrees C., at least 305 degrees
C., at least 310 degrees C., at least 315 degrees C., at least 320
degrees C., at least 325 degrees C., at least 330 degrees C., or at
least 335 degrees C.; a flash point of at most about 335 degrees
C., for example, at most 330 degrees C., at most 325 degrees C., at
most 320 degrees C., at most 315 degrees C., at most 310 degrees
C., at most 305 degrees C., at most 300 degrees C., at most 295
degrees C., at most 290 degrees C., at most 285 degrees C., at most
280 degrees C., at most 275 degrees C., at most 270 degrees C., at
most 265 degrees C., at most 260 degrees C., at most 255 degrees
C., at most 250 degrees C., at most 245 degrees C., at most 240
degrees C., at most 235 degrees C., at most 230 degrees C., at most
225 degrees C., or at most 220 degrees C.; a total acid number
(TAN) of up to about 8.00 mgKOH/g, for example, at most about 7.50
mgKOH/g, at most 7.00 mgKOH/g, at most about 6.50 mgKOH/g, at most
6.00 mgKOH/g, at most 5.50 mgKOH/g, at most 5.00 mgKOH/g, at most
4.50 mgKOH/g, at most 4.00 mgKOH/g, at most 3.50 mgKOH/g, at most
3.00 mgKOH/g, at most 2.50 mgKOH/g, at most 2.00 mgKOH/g, at most
1.50 mgKOH/g, at most 1.00 mgKOH/g, at most 0.50 mgKOH/g, at most
0.10 mgKOH/g, or at most 0.05 mgKOH/g; a total acid number (TAN) of
at least about 0.05 mgKOH/g, for example, at least 0.10 mgKOH/g, at
least 0.50 mgKOH/g, at least 1.00 mgKOH/g, at least 1.50 mgKOH/g,
at least 2.00 mgKOH/g, at least 2.50 mgKOH/g, at least 3.00
mgKOH/g, at least 3.50 mgKOH/g, at least 4.00 mgKOH/g, at least
4.50 mgKOH/g, at least 5.00 mgKOH/g, at least 5.50 mgKOH/g, at
least 6.00 mgKOH/g, at least 6.50 mgKOH/g, at least 7.00 mgKOH/g,
at least 7.50 mgKOH/g, or at least 8.00 mgKOH/g; a kinematic
viscosity at .about.50 degrees C. of at least about 3.75 cSt, for
example, at least 100 cSt, at least 500 cSt, at least 1000 cSt, at
least 1500 cSt, at least 2000 cSt, at least 2500 cSt, at least 3000
cSt, at least 3500 cSt, at least 4000 cSt, at least 4500 cSt, at
least 5000 cSt, at least 5500 cSt, at least 6000 cSt, at least 6500
cSt, at least 7000 cSt, at least 7500 cSt, at least 8000 cSt, at
least 8500 cSt, at least 9000 cSt, at least 9500 cSt, at least
10000 cSt, at least 10500 cSt, at least 11000 cSt, at least 11500
cSt, at least 12000 cSt, at least 12500 cSt, at least 13000 cSt, at
least 13500 cSt, at least 14000 cSt, at least 14500 cSt, or at most
15000 cSt; a kinematic viscosity at .about.50 degrees C. of at most
about 15000 cSt, for example, at most 14500 cSt, at most 14000 cSt,
at most 13500 cSt, at most 13000 cSt, at most 12500 cSt, at most
12000 cSt, at most 11500 cSt, at most 11000 cSt, at most 10500 cSt,
at most 10000 cSt, at most 9500 cSt, at most 9000 cSt, at most 8500
cSt, at most 8000 cSt, at most 7500 cSt, at most 7000 cSt, at most
6500 cSt, at most 6000 cSt, at most 5500 cSt, at most 5000 cSt, at
most 4500 cSt, at most 4000 cSt, at most 3500 cSt, at most 3000
cSt, at most 2500 cSt, at most 2000 cSt, at most 1500 cSt, at most
1000 cSt, at most 500 cSt, or at most 3.75 cSt. The characteristics
can be determined using any suitable standardized test method, such
as ASTM D445 for viscosity, ASTM D4294 for sulfur content, ASTM D9
for flash point, and ASTM D97 for pour point.
[0023] The short residues (VTB) can have a similar or higher micro
carbon residue number as that provided above for the residual
hydrocarbon component. For instance, the short residues (VTB) can
further have micro carbon residue number of at least 1.5% m/m, at
least 2.00% m/m, at least 2.50% m/m, at least 5.00% m/m, at least
7.50%/m/m, at least 10.00% m/m, at least 12.50% m/m, at least
15.00% m/m, at least 17.50% m/m, at least 20.00% m/m, at least
22.50% m/m, at least 25.00% m/m, at least 27.50% m/m, at least
30.00% m/m, at least 32.50% m/m, at least 35.00% m/m, at least
37.50% m/m, at least 40.00% m/m, at least 42.50% m/m, at least
45.00% m/m, at least 47.50% m/m, at least 50% m/m, at least 52.50%
m/m, at least 55.00% m/m, or at least 60.00% m/m. The short
residues (VTB) can also have a micro carbon residue number of at
most 1.50% m/m, at most 2.00% m/m, at most 2.50% m/m, at most 5.00%
m/m, at most 7.50% m/m, at most 10.00% m/m, at most 12.50% m/m, at
most 15.00% m/m, at most 17.50% m/m, at most 22.50% m/m, at most
25.00% m/m, at most 27.50% m/m, at most 30.00% m/m, at most 32.50%
m/m, at most 35.00% m/m, at most 37.50% m/m, at most 40.00% m/m, at
most 42.50% m/m, at most 45.00% m/m, at most 47.50% m/m, at most
50% m/m, at most 52.50% m/m, at most 55.00% m/m, or at most 60/00%
m/m. Preferably, the short residues (VTB) has a micro carbon
residue number in a range of 0.10% m/m and 60.00% m/m, such as in a
range of greater than 0.30% m/m and 60.00% m/m, including any
amount or range in between as specified here or otherwise.
[0024] In a particular embodiment, the residual hydrocarbon
component may be selected from a group consisting of long residues
(ATB), short residues (VTB), and a combination thereof, where the
long residues may exhibit one or more of the following
characteristics: a density at .about.15 degrees C. in a range of
about 0.7 to 1.0 g/cc; a sulfur content in a range of about 0.01 to
0.40 wt %; a pour point in a range of about -19.0 to 64.0 degrees
C.; a flash point in a range of about 80 to 213 degrees C.; a total
acid number (TAN) of up to about 8.00 mgKOH/g; and a kinematic
viscosity at .about.50 degrees C. in a range of about 1.75 to 15000
cSt; and where the short residues (VTB) may exhibit one or more of
the following properties: a density at .about.15 degrees C. in a
range of about 0.8 to 1.1 g/cc; a sulfur content in a range of
about 0.01 to 0.40 wt %; a pour point in a range of about
.about.15.0 to 95 degrees C.; a flash point in a range of about 220
to 335 degrees C.; a total acid number (TAN) of up to about 8.00
mgKOH/g; and a kinematic viscosity at .about.50 degrees C. in a
range of about 3.75 to 15000 cSt. It is understood that there can
be different kinds of long and short residues that exhibit various
properties as described above that may be similar or different to
each other. One or more kinds of long and/or short residues
exhibiting one or more characteristics provided above may be used
to provide the residual hydrocarbon component in the desired
amount, e.g., in a range of 50 to 90 wt % of the overall marine
fuel composition.
[0025] In some embodiments, the residual hydrocarbon component
comprises two types of long residues (ATB). For example, one type
of long residues may exhibit one or more of the following
characteristics: a density at .about.15 degrees C. of about 0.910
g/cc; a sulfur content of about 1000 wppm; a pour point of about 45
degrees C.; a flash point of about 124 degrees C.; and a kinematic
viscosity at .about.50 degrees C. of about 165 cSt. The second type
of long residues may exhibit one or more of the following
characteristics: a density at .about.15 degrees C. of about 0.941
g/cc; a sulfur content of about 1130 wppm; a pour point of about
.about.2 degrees C.; a flash point of about 207 degrees C.; and a
kinematic viscosity at .about.50 degrees C. of about 880 cSt.
[0026] The remaining about 10 to 50 wt % of the marine fuel
composition can comprise one or more hydrocarbon components other
than the residual hydrocarbon component, where the one or more
hydrocarbon components is selected from a non-hydroprocessed
hydrocarbon component, a hydroprocessed hydrocarbon component, and
a combination thereof. For example, the marine fuel composition may
comprise the non-hydroprocessed hydrocarbon component in an amount
of at least 5 wt %, at least 10 wt %, at least 15 wt %, at least 20
wt %, at least 25 wt %, at least 30 wt %, at least 40 wt %, at
least 45 wt %, or 50 wt %. The marine fuel composition may comprise
the non-hydroprocessed hydrocarbon component in an amount of at
most 50 wt %, at most 45 wt %, at most 40 wt %, at most 35 wt %, at
most 30 wt %, at most 25 wt %, at most 20 wt %, at most 25 wt %, at
most 20 wt %, at most 15 wt %, at most 10 wt %, at most 5 wt %, or
none. In one embodiment, the marine fuel composition comprises
greater than about 10 wt % of the non-hydroprocessed hydrocarbon
component, such as about 11 wt %, 12 wt %, 13 wt %, 14 wt %, or 15
wt %; or greater than 15 wt %, such as about 16 wt %, 17 wt %, 18
wt %, 19 wt %, or 20 wt %; or greater than 20 wt %, such as about
21 wt %, 22 wt %, 23 wt %, 24 wt %, or 25 wt %. In some
embodiments, the non-hydroprocessed hydrocarbon includes
hydrocarbon products derived from oil cuts or cuts of a
petrochemical origin which have not been subjected to
hydrotreatment or hydroprocessing (HT). Non-limiting examples of
hydrotreatment or hydroprocessing includes hydrocracking,
hydrodeoxygenation, hydrodesulphurization, hydrodenitrogenation
and/or hydroisomerization.
[0027] In a particular embodiment, the non-hydroprocessed
hydrocarbon component is selected from the group consisting of
light cycle oil (LCO), heavy cycle oil (HCO), fluid catalytic
cracking (FCC) cycle oil, FCC slurry oil, pyrolysis gas oil,
cracked light gas oil (CLGO), cracked heavy gas oil (CHGO),
pyrolysis light gas oil (PLGO), pyrolysis heavy gas oil (PHGO),
thermally cracked residue (also called tar or thermal tar),
thermally cracked heavy distillate, coker heavy distillates, which
is heavier than diesel, and any combination thereof. In other
embodiments, in addition to or alternatively, the
non-hydroprocessed hydrocarbon component is selected from the group
consisting of vacuum gas oil (VGO), coker diesel, coker gas oil,
coker VGO, thermally cracked VGO, thermally cracked diesel,
thermally cracked gas oil, Group I slack waxes, lube oil aromatic
extracts, deasphalted oil (DAO), and any combination thereof. In
yet another embodiment, in addition to or alternatively, the
non-hydroprocessed hydrocarbon component is selected from the group
consisting of coker kerosene, thermally cracked kerosene,
gas-to-liquids (GTL) wax, GTL hydrocarbons, straight-run diesel,
straight-run kerosene, straight run gas oil (SRGO), and any
combination thereof. While preferred, a non-hydroprocessed
hydrocarbon component is not required in a marine fuel composition
described herein, particularly when a residual hydrocarbon
component and a hydroprocessed hydrocarbon component can provide
the marine fuel composition with the requisite or desired
properties. Also, one or more kinds of non-hydroprocessed
hydrocarbon component may be used to provide the marine fuel
composition with the desired characteristics.
[0028] The materials listed above have their ordinary meaning as
understood by one of ordinary skill in the art. For example, LCO is
herein preferably refers to a fraction of FCC products of which at
least 80 wt %, more preferably at least 90 wt %, boils in the range
from equal to or more than 221.degree. C. to less than 370.degree.
C. (at a pressure of 0.1 MegaPascal). HCO is herein preferably
refers to a fraction of the FCC products of which at least 80 wt %,
more preferably at least 90 wt %, boils in the range from equal to
or more than 370.degree. C. to less 425.degree. C. (at a pressure
of 0.1 MegaPascal). Slurry oil is herein preferably refers to a
fraction of the FCC products of which at least 80 wt %, more
preferably at least 90 wt %, boils at or above 425.degree. C. (at a
pressure of 0.1 MegaPascal).
[0029] Additionally or alternatively, the marine fuel composition
can comprise a hydroprocessed hydrocarbon component. For example,
the marine fuel composition may comprise the hydroprocessed
hydrocarbon component in an amount of at least 5 wt %, at least 10
wt %, at least 15 wt %, at least 20 wt %, at least 25 wt %, at
least 30 wt %, at least 40 wt %, at least 45 wt %, or 50 wt %. The
marine fuel composition may comprise the hydroprocessed hydrocarbon
component in an amount of at most 50 wt %, at most 45 wt %, at most
40 wt %, at most 35 wt %, at most 30 wt %, at most 25 wt %, at most
20 wt %, at most 15 wt %, at most 10 wt %, at most 5 wt %, or none.
The marine fuel composition can comprise greater than 20 wt % of
the hydroprocessed hydrocarbon component. The hydroprocessed
hydrocarbon component can be derived from oil cuts or cuts of a
petrochemical origin which have been subjected to hydrotreatment or
hydroprocessing, which can be referred to as hydrotreated.
Non-limiting examples of hydrotreatment or hydroprocessing includes
hydrocracking, hydrodeoxygenation, hydrodesulphurization,
hydrodenitrogenation and/or hydroisomerization.
[0030] In a particular embodiment, the hydroprocessed hydrocarbon
component can comprise at least one of low-sulfur diesel (LSD) of
less than about 500 wppm of sulfur, particularly ultra low-sulfur
diesel (ULSD) of less than 15 or 10 wppm of sulfur; hydrotreated
LCO; hydrotreated HCO; hydrotreated FCC cycle oil; hydrotreated
pyrolysis gas oil, hydrotreated PLGO, hydrotreated PHGO,
hydrotreated CLGO, hydrotreated CHGO, hydrotreated coker heavy
distillates, hydrotreated thermally cracked heavy distillate. In
another embodiment, in addition to or alternatively, the
hydroprocessed hydrocarbon component can comprise at least one of
hydrotreated coker diesel, hydrotreated coker gas oil, hydrotreated
thermally cracked diesel, hydrotreated thermally cracked gas oil,
hydrotreated VGO, hydrotreated coker VGO, hydrotreated residues,
hydrocracker bottoms (which can also be known as hydrocracker
hydrowax), hydrotreated thermally cracked VGO, and hydrotreated
hydrocracker DAO. In yet another embodiment, in addition to or
alternatively, the hydroprocessed hydrocarbon component can
comprise at least one of ultra low sulfur kerosene (ULSK),
hydrotreated jet fuel, hydrotreated kerosene, hydrotreated coker
kerosene, hydrocracker diesel, hydrocracker kerosene, hydrotreated
thermally cracked kerosene. While preferred, a hydroprocessed
hydrocarbon component is not required in a marine fuel composition
described herein, particularly when a residual hydrocarbon
component and a non-hydroprocessed hydrocarbon component can
provide the marine fuel composition with the requisite or desired
properties. Also, one or more kinds of hydroprocessed hydrocarbon
component may be used to provide the marine fuel composition with
the desired characteristics.
[0031] Additionally or alternately, in certain embodiments, the
marine fuel composition can comprise other components aside from
components (i) the residual hydrocarbon, (ii) the hydroprocessed
hydrocarbon, and (iii) the non-hydroprocessed hydrocarbon. Such
other components may typically be present in fuel additives.
Examples of such other components can include, but are not limited
to, detergents, viscosity modifiers, pour point depressants,
lubricity modifiers, dehazers, e.g. alkoxylated phenol formaldehyde
polymers; anti-foaming agents (e.g., polyether-modified
polysiloxanes); ignition improvers (cetane improvers) (e.g.
2-ethylhexyl nitrate (EHN), cyclohexyl nitrate, di-tert-butyl
peroxide and those disclosed in U.S. Pat. No. 4,208,190 at column
2, line 27 to column 3, line 21); anti-rust agents (e.g. a
propane-1,2-diol semi-ester of tetrapropenyl succinic acid, or
polyhydric alcohol esters of a succinic acid derivative, the
succinic acid derivative having on at least one of its alpha-carbon
atoms an unsubstituted or substituted aliphatic hydrocarbon group
containing from 20 to 500 carbon atoms, e.g. the pentaerythritol
diester of polyisobutylene-substituted succinic acid); corrosion
inhibitors; reodorants; anti-wear additives; anti-oxidants (e.g.
phenolics such as 2,6-di-tert-butylphenol, or phenylenediamines
such as N,N'-di-sec-butyl-p-phenylenediamine); metal deactivators;
static dissipator additives; combustion improvers; and mixtures
thereof.
[0032] Examples of detergents suitable for use in fuel additives
include polyolefin substituted succinimides or succinamides of
polyamines, for instance polyisobutylene succinimides or
polyisobutylene amine succinamides, aliphatic amines, Mannich bases
or amines and polyolefin (e.g. polyisobutylene) maleic anhydrides.
Succinimide dispersant additives are described for example in
GB-A-960493, EP-A-0147240, EP-A-0482253, EP-A-0613938, EP-A-0557516
and WO-A-98/42808.
[0033] In one embodiment, if present, a lubricity modifier enhancer
may be conveniently used at a concentration of less than 1000 ppmw,
preferably from 50 to 1000 or from 100 to 1000 ppmw, more
preferably from 50 to 500 ppmw. Suitable commercially available
lubricity enhancers include ester- and acid-based additives. It may
also be preferred for the fuel composition to contain an
anti-foaming agent, more preferably in combination with an
anti-rust agent and/or a corrosion inhibitor and/or a lubricity
modifying additive. Unless otherwise stated, the concentration of
each such additional component in the fuel composition is
preferably up to 10000 ppmw, more preferably in the range from 0.1
to 1000 ppmw, advantageously from 0.1 to 300 ppmw, such as from 0.1
to 150 ppmw (all additive concentrations quoted in this
specification refer, unless otherwise stated, to active matter
concentrations by weight). The concentration of any dehazer in the
fuel composition will preferably be in the range from 0.1 to 20
ppmw, more preferably from 1 to 15 ppmw, still more preferably from
1 to 10 ppmw, advantageously from 1 to 5 ppmw. The concentration of
any ignition improver present will preferably be 2600 ppmw or less,
more preferably 2000 ppmw or less, conveniently from 300 to 1500
ppmw.
[0034] If desired, one or more additive components, such as those
listed above, may be co-mixed--preferably together with suitable
diluent(s)--in an additive concentrate, and the additive
concentrate may then be dispersed into the base fuel, or into the
base fuel/wax blend, in order to prepare a fuel composition
according to the present invention.
[0035] In one embodiment, the marine fuel composition has a maximum
sulfur content of 1000 wppm (parts per million by weight) or 0.1%.
In some embodiments, the marine fuel composition can exhibit a
sulfur content in a range of about 850 wppm to 1000 wppm, for
example about 900 wppm, 950 wppm, or 1000 wppm. In other
embodiments, the marine fuel composition can exhibit a sulfur
content of at most 1000 wppm, for example at most 1000 wppm, at
most 950 wppm, at most 900 wppm, at most 850 wppm, at most 800
wppm, at most 750 wppm, at most 700 wppm, at most 650 wppm, at most
600 wppm, at most 550 wppm, at most 500 wppm, at most 450 wppm, at
most 400 wppm, at most 350 wppm, at most 300 wppm, or at most 250
wppm. In some embodiments, the marine fuel composition can exhibit
a sulfur content of at least 250 wppm, at least 300 wppm, at least
350 wppm, at least 400 wppm, at least 450 wppm, at least 500 wppm,
at least 550 wppm, at least 600 wppm, at least 650 wppm, at least
700 wppm, at least 750 wppm, at least 800 wppm, at least 850 wppm,
or at least 900 wppm, at least 950 wppm, at least 1000.
[0036] It is understood that the sulfur content of the residual
hydrocarbon component, the non-hydroprocessed hydrocarbon
component, and/or the hydroprocessed hydrocarbon component,
individually, can vary, as long as the marine fuel composition as a
whole meets the sulfur target content requirement for a certain
embodiment. Likewise, in one embodiment, it is understood that
other characteristics of the residual hydrocarbon component, the
non-hydroprocessed hydrocarbon component, and/or the hydroprocessed
hydrocarbon component, individually, can vary, as long as the
marine fuel composition meets the requirements of a
standardization, such as ISO 8217. As such, certain embodiments can
allow for greater use of cracked materials, for example, 25 wt % or
greater.
[0037] Still further additionally or alternately, in some
embodiments, the marine fuel composition can exhibit one or more of
the following characteristics: a kinematic viscosity at about
50.degree. C. (according to a suitable standardized test method,
e.g., ASTM D445) of at most about 700 cSt, for example at most 500
cSt, at most 380 cSt, at most 180 cSt, at most 80 cSt, at most 55
cSt, at most 50 cSt, at most 45 cSt, at most 40 cSt, at most 35
cSt, at most 30 cSt, at most 25 cSt, at most 20 cSt, at most 15
cSt, at most 10 cSt, or at most 5 cSt; for example, about 4, 5, 6,
7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, or 21 cSt; a
kinematic viscosity at about 50.degree. C. (according to a suitable
standardized test method, e.g., ASTM D445) of at least 5 cSt, for
example at least 10 cSt, at least 15 cSt, at least 20 cSt, at least
25 cSt, at least 30 cSt, at least 35 cSt, at least 40 cSt, at least
45 cSt; at least 50 cSt, at least 55 cSt, at least 80 cSt, at least
180 cSt, at least 380 cSt, at least 500 cSt, or at least 700 cSt; a
density at about 15.degree. C. (according to a suitable
standardized test method, e.g., ASTM D4052) of at most 1.010
g/cm.sup.3, for example, at most 1.005, at most 1.000, at most
0.995, such as 0.991 g/cm.sup.3, at most 0.990 g/cm.sup.3, at most
0.985 g/cm.sup.3, at most 0.980 g/cm.sup.3, at most 0.975
g/cm.sup.3, at most 0.970 g/cm.sup.3, at most 0.965 g/cm.sup.3, at
most 0.960 g/cm.sup.3, at most 0.955 g/cm.sup.3, at most 0.950
g/cm.sup.3, at most 0.945 g/cm.sup.3, at most 0.940 g/cm.sup.3, at
most 0.935 g/cm.sup.3, at most 0.930 g/cm.sup.3, at most 0.925
g/cm.sup.3, at most 0.920 g/cm.sup.3, at most 0.915 g/cm.sup.3, at
most 0.910 g/cm.sup.3, at most 0.905 g/cm.sup.3, at most 0.900
g/cm.sup.3, at most 0.895 g/cm.sup.3, at most 0.890 g/cm.sup.3, at
most 0.885 g/cm.sup.3, or at most 0.880 g/cm.sup.3; a density at
about 15.degree. C. (according to a suitable standardized test
method, e.g., ASTM D4052) of at least 0.870 g/cm.sup.3, at least
0.875 g/cm.sup.3, at least 0.880 g/cm, at least 0.885 g/cm.sup.3,
at least 0.890 g/cm.sup.3, at least 0.895 g/cm.sup.3, at least
0.900 g/cm.sup.3, at least 0.905 g/cm.sup.3, at least 0.910
g/cm.sup.3, at least 0.915 g/cm.sup.3, at least 0.920 g/cm.sup.3,
at least 0.925 g/cm.sup.3, at least 0.930 g/cm.sup.3, at least
0.935 g/cm.sup.3, at least 0.940 g/cm.sup.3, at least 0.945
g/cm.sup.3, at least 0.950 g/cm.sup.3, at least 0.955 g/cm.sup.3,
at least 0.960 g/cm.sup.3, at least 0.965 g/cm.sup.3, at least
0.970 g/cm.sup.3, at least 0.975 g/cm.sup.3, at least 0.980
g/cm.sup.3, at least 0.985 g/cm.sup.3, at least 0.990 g/cm.sup.3,
such as 0.991 g/cm.sup.3, at least 0.995 g/cm.sup.3, at least 1.000
g/cm.sup.3, at least 1.005 g/cm.sup.3, or at least 1.010
g/cm.sup.3; a pour point (according to a suitable standardized test
method, e.g., ASTM D97) of at most 35.degree. C., at most
30.degree. C., for example, at most 28.degree. C., at most
25.degree. C., at most 20.degree. C., at most 15.degree. C., at
most 10.degree. C., for example 6.degree. C., at most 5.degree. C.,
at most 0.degree. C., at most -5.degree. C., at most -10.degree.
C., at most -15.degree. C., at most -20.degree. C., at most
-25.degree. C., such as -27.degree. C., or at most -30.degree. C.;
a pour point (according to a suitable standardized test method,
e.g., ASTM D97) of at least -30.degree. C., such as -27.degree. C.,
for example, at least -25.degree. C., at least -20.degree. C., at
least -15.degree. C., at least -10.degree. C., at least -5.degree.
C., at least 0.degree. C., at least 5.degree. C., at least
7.degree. C., at least 10.degree. C., at least 15.degree. C., at
least 20.degree. C., at least 25.degree. C., at least 30.degree.
C., or at least 35.degree. C., and a flash point (according to a
suitable standardized testing method, e.g., ASTM D93 Proc. 9
(Automatic)) of at least about 60.degree. C., for example, at least
65.degree. C., at least 70.degree. C., at least 75.degree. C., at
least 80.degree. C., at least 85.degree. C., at least 90.degree.
C., at least 95.degree. C., at least 100.degree. C., at least
105.degree. C., at least 110.degree. C., at least 115.degree. C.,
at least 120.degree. C., at least 125.degree. C., or at least
130.degree. C.; an acid number (also known as Total Acid Number or
TAN) of at most 2.5 mgKOH/g, for example, at most 2.0 mgKOH/g, at
most 1.5 mgKOH/g, at most 1.0 mgKOH/g, or at most 0.5 mgKOH/g; an
acid number of at least 0.5 mgKOH/g, at least 1.0 mgKOH/g, at least
1.5 mgKOH/g, at least 2.0 mgKOH/g, or at least 2.5 mgKOH/g.
[0038] In one embodiment, the marine fuel composition may exhibit
one or more of the following characteristics: a kinematic viscosity
at about 50.degree. C. (according to a suitable standardized test
method, e.g., ASTM D445) in a range of about 0 to 700 cSt, for
example, at most 700.0 cSt, at most 500.0 cSt, at most 380.0 cSt,
at most 180.0 cSt, at most 80.00 cSt, at most 30.00 cSt, or at most
10.00 cSt; a density at about 15.degree. C. (according to a
suitable standardized test method, e.g., ASTM D4052) in a range of
about 0.870 to 1.010 g/cm.sup.3, for example, at most 0.920
g/cm.sup.3, at most 0.960 g/cm.sup.3, at most 0.975 g/cm.sup.3, at
most 0.991 g/cm.sup.3, or at most 1.010 g/cm.sup.3, particularly,
at least 0.890 g/cm.sup.3; a pour point (according to a suitable
standardized test method, e.g., ASTM D97) in a range of about -30
to 35.degree. C., such as -27 to 30.degree. C., for example, at
most 6 to 30 degrees C. or at most 0 to 30 degrees C.; a flash
point (according to a suitable standardized testing method, e.g.,
ASTM D93 Proc. 9 (Automatic)) in a range of about 60 to 130.degree.
C., for example, at least 60 degrees C.; an acid number in a range
of about 0.0 to 2.5 mgKOH/g, for example, at most about 2.5
mgKOH/g.
[0039] Yet still further additionally or alternately, the low
sulfur marine and/or bunker fuels, e.g., made according to the
methods disclosed herein, can exhibit at least one of the following
characteristics: a hydrogen sulfide content (according to a
suitable standardized test method, e.g., IP 570) of at most about
2.0 mg/kg; an acid number (according to a suitable standardized
test method, e.g., ASTM D-664) of at most about 2.5 mg KOH per
gram; a sediment content (according to according to a suitable
standardized test method, e.g., ASTM D4870 Proc. B) of at most
about 0.1 wt %; a water content (according to according to
according to a suitable standardized test method, e.g., ASTM D95)
of at most about 0.5 vol %, for example about 0.3 vol %; an ash
content (according to a suitable standardized testing method, e.g.,
ASTM D482) of at most about 0.15 wt %, for example, about 0.10 wt
%, 0.07 wt %, or 0.04 wt %, and a Calculated Carbon Aromaticity
Index (CCAI) number of at most 870, such as at most 850 or 860.
[0040] According to a yet further aspect, there is provided a
process for the preparation of a marine fuel composition comprising
at least about 50 and up to 90 wt % of a residual hydrocarbon
component and at least about 10 and up to 50 wt % of other
components selected from a non-hydroprocessed hydrocarbon
component, a hydroprocessed hydrocarbon component, and a
combination thereof, wherein the marine fuel composition has a
sulfur content of about 0.1 wt % (1000 wppm) or less. The process
involves selecting a relative composition amount and material of
the residual hydrocarbon component; selecting a relative
composition amount and material of the non-hydroprocessed
hydrocarbon component and/or hydroprocessed hydrocarbon component
based on the residual hydrocarbon component selection to provide
the composition sulfur content of about 0.1 wt % or less; and
blending the selected components to form the marine fuel
composition. In one embodiment, the selected residual hydrocarbon
component has a sulfur content of 0.4 wt % or less. In another
embodiment, the residual hydrocarbon component, non-hydroprocessed
hydrocarbon component and/or hydroprocessed hydrocarbon component
are selected to provide the marine fuel composition with
characteristics that meet a standard specification, such as, but
not limited to ISO 8217.
[0041] To facilitate a better understanding of the present
invention, the following examples of preferred or representative
embodiments are given. In no way should the following examples be
read to limit, or to define, the scope of the invention.
EXAMPLES
[0042] The following are non-limiting Examples 1-107 of exemplary
embodiments of the marine fuel composition described herein. The
residual hydrocarbon component can comprise at least one of two
types of long residues: ATB(1) and ATB(2). The non-hydroprocessed
hydrocarbon component, if present, can be selected from a group
consisting of slurry oil, pyrolysis gas oil ("Pygas oil"), LCO,
thermally cracked residue (which can also be known as thermal tar),
and Group I slack waxes. The hydroprocessed hydrocarbon component,
if present, can be selected from a group consisting of
hydroprocessed LCO that contains up to 400 wppm of sulfur ("400
LCO"), hydroprocessed LCO that contains up to 15 wppm of sulfur
("15 LCO"), ULSD, and hydrocracker bottoms (which can also be known
as hydrowax). Examples 1-101 are prophetic examples, and the
characteristics of these materials in Examples 1-101 are provided
in Table 1 below.
TABLE-US-00002 TABLE 1 Characteristics of respective components in
Examples 1-101 Density Flash Viscosity @ @ ~15.degree. C. Sulfur
Pour Point Point ~50.degree. C. (kg/m.sup.3) (wppm) (.degree. C.)
(.degree. C.) (CSt) ATB (1) ~0.910 ~1000 ~45 ~124 ~165 ATB (2)
~0.941 ~1130 ~-2 ~207 ~880 Slurry Oil ~1.093 ~4000 ~0 ~100 ~800
Pygas Oil ~0.960 ~1000 ~0 ~80 ~10 LCO ~0.989 ~1590 ~-15 ~80 ~10
Thermal Tar ~1.026 ~5000 ~6 ~66 ~1213 Slack Wax ~0.814 ~32 ~35 ~60
~10 400 LCO ~0.880 ~400 ~-15 ~88 ~2 15 LCO ~0.959 ~15 ~-18 ~61 ~2
ULSD ~0.860 ~15 ~0 ~60 ~2 Hydrowax ~0.838 ~100 ~39 ~210 ~18
Examples 1-11
[0043] In prophetic Examples 1-11, each of the marine fuel
composition can include about 55 wt % of a residual hydrocarbon
component. In Examples 1-6, the residual hydrocarbon component can
comprise 20 wt % of long residues ATB(1) and 35 wt % of long
residues ATB(2). In Examples 7-11, the residual hydrocarbon
component can comprise 35 wt % of long residues ATB(1) and 20 wt %
of long residues ATB(2). The remaining about 45 wt % of the
respective marine fuel composition can be selected from a
non-hydroprocessed hydrocarbon component, a hydroprocessed
hydrocarbon component, and a combination thereof. Table 2 below
summarizes the blend content of the marine fuel composition in
Examples 1-11.
TABLE-US-00003 TABLE 2 Blend content of Examples 1-11 Blend content
(wt %) Residual Non-hydroprocessed Hydroprocessed component
component component ATB ATB Slurry Pygas Thermal Slack 400 15 Hydro
(1) (2) Oil Oil LCO tar Wax LCO LCO ULSD wax Ex. 1 20 35 0 0 18 0 0
27 0 0 0 Ex. 2 20 35 5 0 10 0 0 0 0 30 0 Ex. 3 20 35 0 0 25 0 20 0
0 0 0 Ex. 4 20 35 0 0 20 0 0 0 10 0 15 Ex. 5 20 35 0 25 0 0 0 0 20
0 0 Ex. 6 20 35 0 0 20 1 0 0 24 0 0 Ex. 7 35 20 0 0 20 0 0 25 0 0 0
Ex. 8 35 20 5 0 10 0 0 0 0 30 0 Ex. 9 35 20 0 0 25 0 20 0 0 0 0 Ex.
10 35 20 0 0 20 0 0 0 10 0 15 Ex. 11 35 20 0 25 0 0 0 0 20 0 0
[0044] Table 3 below provides certain characteristics that the
marine fuel composition of Examples 1-11 would be expected to have,
as measured by a respective standard testing method.
TABLE-US-00004 TABLE 3 Expected characteristics of the marine fuel
composition in Examples 1-11 Pour Density @ Sulfur Point Flash
Point Viscosity @ ~15.degree. C. (g/cc) (wppm) (.degree. C.)
(.degree. C.) ~50.degree. C. (cSt) Ex. 1 0.925 990 14.2 100.2 23.8
Ex. 2 0.919 959 16.3 81.2 26.1 Ex. 3 0.917 999 22.5 108.0 54.0 Ex.
4 0.928 930 21.7 95.8 44.1 Ex. 5 0.943 849 15.5 85.2 29.0 Ex. 6
0.949 967 14.1 83.4 26.9 Ex. 7 0.923 994 23.1 98.7 21.9 Ex. 8 0.915
940 24.6 80.8 22.7 Ex. 9 0.913 980 29.2 106.4 45.6 Ex. 10 0.924 911
28.6 94.9 37.5 Ex. 11 0.938 829 24.0 84.7 25.1
Examples 12-30
[0045] In prophetic Examples 12-30, each of the marine fuel
composition can include about 60 wt % of a residual hydrocarbon
component. In Examples 12 to 18, the residual hydrocarbon component
can comprise 20 wt % of long residues ATB(1) and 40 wt % of long
residues ATB(2). In Examples 19 to 30, the residual hydrocarbon
component can comprise 30 wt % of long residues ATB(1) and 30 wt %
of long residues ATB(2). The remaining about 40 wt % of the
respective marine fuel composition can be selected from a
non-hydroprocessed hydrocarbon component, a hydroprocessed
hydrocarbon component, and a combination thereof. Table 4 below
summarizes the blend content of the marine fuel composition in
Examples 12-30.
TABLE-US-00005 TABLE 4 Blend content of Examples 12-30 Blend
content (wt %) Residual Non-hydroprocessed Hydroprocessed component
component component ATB ATB Slurry Pygas Thermal Slack 400 15 Hydro
(1) (2) Oil Oil LCO tar Wax LCO LCO ULSD wax Ex. 12 20 40 0 0 20 0
0 0 0 0 20 Ex. 13 20 40 0 0 20 0 20 0 0 0 0 Ex. 14 20 40 0 0 20 0 0
0 0 20 0 Ex. 15 20 40 0 0 15 0 0 25 0 0 0 Ex. 16 20 40 0 0 21 0 0 0
19 0 0 Ex. 17 20 40 0 25 0 0 0 0 15 0 0 Ex. 18 20 40 0 0 17 1 0 0
22 0 0 Ex. 19 30 30 0 0 22 0 0 0 18 0 0 Ex. 20 30 30 5 0 0 0 0 35 0
0 0 Ex. 21 30 30 0 0 17 1 0 0 22 0 0 Ex. 22 30 30 0 0 15 0 0 25 0 0
0 Ex. 23 30 30 0 30 0 0 0 10 0 0 0 Ex. 24 30 30 8 0 0 0 0 0 0 32 0
Ex. 25 30 30 0 0 20 0 20 0 0 0 0 Ex. 26 30 30 0 0 20 0 0 0 0 0 20
Ex. 27 30 30 0 20 0 0 0 20 0 0 0 Ex. 28 30 30 0 0 0 0 0 40 0 0 0
Ex. 29 30 30 0 30 0 0 0 0 10 0 0 Ex. 30 30 30 0 20 10 0 0 0 10 0
0
[0046] Table 5 below provides certain characteristics that the
marine fuel composition of Examples 12-30 would be expected to
have, as measured by a respective standard testing method.
TABLE-US-00006 TABLE 5 Expected characteristics of the marine fuel
composition in Examples 12-30 Pour Density @ Sulfur Point Flash
Point Viscosity @ ~15.degree. C. (g/cc) (wppm) (.degree. C.)
(.degree. C.) ~50.degree. C. (cSt) Ex. 12 0.921 990 24.0 112.4 80.5
Ex. 13 0.915 976 22.7 112.5 67.1 Ex. 14 0.926 973 15.6 85.9 35.0
Ex. 15 0.925 991 14.4 102.8 30.2 Ex. 16 0.947 989 14.3 87.1 36.1
Ex. 17 0.942 904 15.8 89.0 40.8 Ex. 18 0.947 976 14.4 85.5 34.3 Ex.
19 0.944 992 20.5 87.1 33.5 Ex. 20 0.916 979 20.9 106.1 24.6 Ex. 21
0.944 963 21.7 85.2 32.8 Ex. 22 0.922 978 20.7 101.9 27.3 Ex. 23
0.930 979 22.0 99.2 42.9 Ex. 24 0.914 964 22.5 81.7 29.8 Ex. 25
0.912 963 27.3 111.1 59.6 Ex. 26 0.918 977 28.4 111.1 71.1 Ex. 27
0.922 919 21.6 101.0 31.6 Ex. 28 0.906 799 20.7 105.0 18.3 Ex. 29
0.939 941 22.0 91.2 42.9 Ex. 30 0.941 1000 21.5 91.2 42.9
Examples 31-61
[0047] In prophetic Examples 31-61, each of the marine fuel
composition can include about 70 wt % of a residual hydrocarbon
component. In Examples 31-42, the residual hydrocarbon component
can comprise 30 wt % of long residues ATB(1) and 40 wt % of long
residues ATB(2). In Examples 43-55, the residual hydrocarbon
component can comprise 40 wt % of long residues ATB(1) and 30 wt %
of long residues ATB(2). In Examples 56-61, the residual
hydrocarbon component can comprise 50 wt % of long residues ATB(1)
and 20 wt % of long residues ATB(2). The remaining about 30 wt % of
the respective marine fuel composition can be selected from a
non-hydroprocessed hydrocarbon component, a hydroprocessed
hydrocarbon component, and a combination thereof. Table 6 below
summarizes the blend content of the marine fuel composition in
Examples 31-61.
TABLE-US-00007 TABLE 6 Blend content of Examples 31-61 Blend
content (wt %) Residual Non-hydroprocessed Hydroprocessed component
component component ATB ATB Slurry Pygas Thermal Slack 400 15 Hydro
(1) (2) Oil Oil LCO tar Wax LCO LCO ULSD wax Ex. 31 30 40 0 0 15 0
0 0 0 15 0 Ex. 32 30 40 5 0 0 0 0 10 0 15 0 Ex. 33 30 40 0 0 15 0
15 0 0 0 0 Ex. 34 30 40 0 20 0 0 0 10 0 0 0 Ex. 35 30 40 0 24 0 0 0
0 6 0 0 Ex. 36 30 40 0 24 0 0 0 0 0 6 0 Ex. 37 30 40 0 0 11 1 0 0
18 0 Ex. 38 30 40 0 0 15 0 0 0 5 0 10 Ex. 39 30 40 0 0 10 0 0 0 0 0
20 Ex. 40 30 40 0 0 10 0 0 20 0 0 0 Ex. 41 30 40 0 0 15 0 0 0 15 0
0 Ex. 42 30 40 0 0 15 0 0 0 0 15 0 Ex. 43 40 30 0 10 10 0 0 0 10 0
0 Ex. 44 40 30 0 0 15 0 0 0 5 0 10 Ex. 45 40 30 0 0 16 0 14 0 0 0 0
Ex. 46 40 30 0 0 16 0 0 0 0 14 0 Ex. 47 40 30 0 0 11 0 0 19 0 0 0
Ex. 48 40 30 0 20 0 0 0 10 0 0 0 Ex. 49 40 30 0 0 10 0 0 10 0 0 10
Ex. 50 40 30 5 0 0 0 0 0 25 0 0 Ex. 51 40 30 0 0 0 0 0 20 0 10 0
Ex. 52 40 30 0 0 0 0 0 19 0 0 11 Ex. 53 40 30 0 0 13 0 12 5 0 0 0
Ex. 54 40 30 0 0 13 0 0 7 0 0 10 Ex. 55 40 30 0 0 15 0 0 0 0 15 0
Ex. 56 50 20 0 0 12 0 0 18 0 0 0 Ex. 57 50 20 0 0 15 0 0 0 15 0 0
Ex. 58 50 20 0 0 0 0 0 30 0 0 0 Ex. 59 50 20 0 0 0 0 0 0 30 0 0 Ex.
60 50 20 0 5 0 0 0 0 25 0 0 Ex. 61 50 20 5 0 0 0 0 0 25 0 0
[0048] Table 7 below provides certain characteristics that the
marine fuel composition of Examples 31-61 would be expected to
have, as measured by a respective standard testing method.
TABLE-US-00008 TABLE 7 Expected characteristics of the marine fuel
composition in Examples 31-61 Pour Density @ Sulfur Point Flash
Point Viscosity @ ~15.degree. C. (g/cc) (wppm) (.degree. C.)
(.degree. C.) ~50.degree. C. (cSt) Ex. 31 0.925 993 21.7 91.3 55.1
Ex. 32 0.918 994 22.0 93.7 48.7 Ex. 33 0.917 995 26.1 116.4 94.1
Ex. 34 0.929 992 22.0 105.4 65.4 Ex. 35 0.937 993 22.1 98.1 75.4
Ex. 36 0.930 993 22.4 97.7 75.4 Ex. 37 0.940 980 21.0 90.0 52.1 Ex.
38 0.928 1001 25.1 104.9 85.8 Ex. 39 0.913 931 28.7 123.2 114.4 Ex.
40 0.923 991 21.0 107.8 46.7 Ex. 41 0.941 993 20.9 92.0 55.1 Ex. 42
0.925 993 21.7 91.3 55.1 Ex. 43 0.936 1000 26.3 94.6 58.1 Ex. 44
0.924 988 29.4 104.0 75.7 Ex. 45 0.915 998 30.0 113.7 82.8 Ex. 46
0.923 996 26.5 91.4 50.8 Ex. 47 0.921 990 26.0 106.5 43.2 Ex. 48
0.925 979 26.7 104.5 58.1 Ex. 49 0.915 948 29.4 112.8 63.4 Ex. 50
0.939 943 26.0 87.4 43.6 Ex. 51 0.907 821 26.3 96.8 30.9 Ex. 52
0.904 826 29.7 117.0 47.3 Ex. 53 0.914 970 29.4 113.3 69.1 Ex. 54
0.918 984 29.4 111.9 70.4 Ex. 55 0.922 980 26.5 90.8 49.2 Ex. 56
0.919 989 30.1 105.3 40.0 Ex. 57 0.934 967 30.0 91.0 44.0 Ex. 58
0.907 846 30.1 108.2 28.0 Ex. 59 0.930 731 30.0 84.1 28.0 Ex. 60
0.930 780 30.1 86.1 32.4 Ex. 61 0.936 930 30.1 87.0 39.1
Examples 62-71
[0049] In prophetic Examples 62-71, each of the marine fuel
composition can include about 75 wt % of a residual hydrocarbon
component, which can comprise 45 wt % of long residues ATB(1) and
30 wt % of long residues ATB(2). The remaining about 25 wt % of the
respective marine fuel composition can be selected from a
non-hydroprocessed hydrocarbon component, a hydroprocessed
hydrocarbon component, and a combination thereof. Table 8 below
summarizes the blend content of the marine fuel composition in
Examples 62-71.
TABLE-US-00009 TABLE 8 Blend content of Examples 62-71 Blend
content (wt %) Residual Non-hydroprocessed Hydroprocessed component
component component ATB ATB Slurry Pygas Thermal Slack 400 15 Hydro
(1) (2) Oil Oil LCO tar Wax LCO LCO ULSD wax Ex. 62 45 30 0 0 13 0
0 0 12 0 0 Ex. 63 45 30 0 20 0 0 0 0 5 0 0 Ex. 64 45 30 0 20 0 0 0
0 0 5 0 Ex. 65 45 30 0 0 0 0 0 25 0 0 0 Ex. 66 45 30 0 0 13 0 0 0 0
12 0 Ex. 67 45 30 0 0 0 0 0 20 0 0 5 Ex. 68 45 30 0 17 0 0 0 8 0 0
0 Ex. 69 45 30 0 0 0 0 5 20 0 0 0 Ex. 70 45 30 0 0 9 0 0 16 0 0 0
Ex. 71 45 30 0 0 10 0 5 10 0 0 0
[0050] Table 9 below provides certain characteristics that the
marine fuel composition of Examples 62-71 would be expected to
have, as measured by a respective standard testing method.
TABLE-US-00010 TABLE 9 Characteristics of the marine fuel
composition in Examples 62-71 Pour Density @ Sulfur Point Flash
Point Viscosity @ ~15.degree. C. (g/cc) (wppm) (.degree. C.)
(.degree. C.) ~50.degree. C. (cSt) Ex. 62 0.935 998 28.2 95.1 63.6
Ex. 63 0.931 990 28.9 100.5 81.7 Ex. 64 0.926 990 29.1 100.1 81.7
Ex. 65 0.911 889 28.3 111.8 41.4 Ex. 66 0.922 998 28.7 94.5 63.6
Ex. 67 0.909 874 29.9 115.4 50.6 Ex. 68 0.925 991 28.9 107.2 73.2
Ex. 69 0.907 871 29.6 115.4 48.6 Ex. 70 0.921 996 28.3 109.2 55.5
Ex. 71 0.918 990 29.6 112.1 68.2
Examples 72-91
[0051] In prophetic Examples 72-91, each of the marine fuel
composition can include about 80 wt % of a residual hydrocarbon
component. In Examples 72 to 83, the residual hydrocarbon component
can comprise 30 wt % of long residues ATB(1) and 50 wt % of long
residues ATB(2). In Examples 84 to 91, the residual hydrocarbon
component can comprise 40 wt % of long residues ATB(1) and 40 wt %
of long residues ATB(2). The remaining about 20 wt % of the
respective marine fuel composition can be selected from a
non-hydroprocessed hydrocarbon component, a hydroprocessed
hydrocarbon component, and a combination thereof. Table 10 below
summarizes the blend content of the marine fuel composition in
Examples 72-91.
TABLE-US-00011 TABLE 10 Blend content of Examples 72-91 Blend
content (wt %) Residual Non-Hydroprocessed Hydroprocessed component
component component ATB ATB Slurry Pygas Thermal Slack 400 15 Hydro
(1) (2) Oil Oil LCO tar Wax LCO LCO ULSD wax Ex. 72 30 50 0 0 0 0 0
0 20 0 0 Ex. 73 30 50 0 0 0 0 0 0 0 20 0 Ex. 74 30 50 0 0 0 0 0 20
0 0 0 Ex. 75 30 50 0 0 8 0 0 0 12 0 0 Ex. 76 30 50 0 0 8 0 0 0 0 12
0 Ex. 77 30 50 0 9 0 0 0 11 0 0 0 Ex. 78 30 50 0 13 0 0 0 0 7 0 0
Ex. 79 30 50 0 13 0 0 0 0 0 7 0 Ex. 80 30 50 0 13 0 0 7 0 0 0 0 Ex.
81 30 50 0 12 0 0 0 0 0 0 8 Ex. 82 30 50 0 0 7 0 0 0 0 0 13 Ex. 83
30 50 0 0 8 0 12 0 0 0 0 Ex. 84 40 40 0 0 9 0 0 0 11 0 0 Ex. 85 40
40 0 11 0 0 0 9 0 0 0 Ex. 86 40 40 0 14 0 0 6 0 0 0 0 Ex. 87 40 40
0 14 0 0 0 0 6 0 0 Ex. 88 40 40 0 14 0 0 0 0 0 0 6 Ex. 89 40 40 0
14 0 0 0 0 0 6 0 Ex. 90 40 40 0 0 9 0 11 0 0 0 0 Ex. 91 40 40 0 0 5
0 0 15 0 0 0
[0052] Table 11 below provides certain characteristics that the
marine fuel composition of Examples 72-91 would be expected to
have, as measured by a respective standard testing method.
TABLE-US-00012 TABLE 11 Characteristics of the marine fuel
composition in Examples 72-91 Pour Density @ Sulfur Point Flash
Point Viscosity @ ~15.degree. C. (g/cc) (wppm) (.degree. C.)
(.degree. C.) ~50.degree. C. (cSt) Ex. 72 0.935 868 21.3 93.0 72.0
Ex. 73 0.914 868 22.3 92.0 72.0 Ex. 74 0.919 945 21.4 117.9 72.0
Ex. 75 0.937 994 21.3 98.5 96.7 Ex. 76 0.924 994 22.0 97.7 96.7 Ex.
77 0.926 999 21.8 114.5 100.4 Ex. 78 0.935 996 22.0 102.9 117.3 Ex.
79 0.928 996 22.3 102.3 117.3 Ex. 80 0.924 997 24.4 118.9 156.0 Ex.
81 0.924 993 25.2 120.2 169.9 Ex. 82 0.920 989 26.6 128.7 179.3 Ex.
83 0.918 996 25.5 126.8 156.0 Ex. 84 0.934 997 26.2 98.6 88.2 Ex.
85 0.924 998 26.7 112.5 95.1 Ex. 86 0.922 994 28.5 115.9 135.3 Ex.
87 0.932 993 26.8 103.0 106.6 Ex. 88 0.924 998 28.9 115.9 144.0 Ex.
89 0.926 993 27.0 102.5 106.6 Ex. 90 0.917 999 29.4 122.7 135.3 Ex.
91 0.921 992 26.3 114.4 76.1
Examples 92-101
[0053] In prophetic Examples 92-101, each of the marine fuel
composition can include about 90 wt % of a residual hydrocarbon
component. In Examples 92 to 95, the residual hydrocarbon component
can comprise 40 wt % of long residues ATB(1) and 50 wt % of long
residues ATB(2). In Examples 96 to 99, the residual hydrocarbon
component can comprise 45 wt % of long residues ATB(1) and 45 wt %
of long residues ATB(2). In Examples 100 to 101, the residual
hydrocarbon component can comprise 48 wt % of long residues ATB(1)
and 42 wt % of long residues ATB(2). The remaining about 10 wt % of
the respective marine fuel composition can be selected from a
non-hydroprocessed hydrocarbon component, a hydroprocessed
hydrocarbon component, and a combination thereof. Table 12 below
summarizes the blend content of the marine fuel composition in
Examples 92-101.
TABLE-US-00013 TABLE 12 Blend content of Examples 92-101 Blend
content (wt %) Residual Non-hydroprocessed Hydroprocessed component
component component ATB ATB Slurry Pygas Thermal Slack 400 15 Hydro
(1) (2) Oil Oil LCO tar Wax LCO LCO ULSD wax Ex. 92 40 50 0 0 0 0 0
0 10 0 0 Ex. 93 40 50 0 0 0 0 10 0 0 0 0 Ex. 94 40 50 0 0 0 0 0 0 0
0 10 Ex. 95 40 50 0 0 0 0 0 0 0 10 0 Ex. 96 45 45 0 0 0 0 0 10 0 0
0 Ex. 97 45 45 0 0 0 0 0 10 0 0 0 Ex. 98 45 45 0 0 0 0 0 0 10 0 0
Ex. 99 45 45 0 0 0 0 0 0 0 10 0 Ex. 100 48 42 0 0 0 0 0 0 10 0 0
Ex. 101 48 42 0 0 0 0 0 10 0 0 0
[0054] Table 13 below provides certain characteristics that the
marine fuel composition of Examples 92-101 would be expected to
have, as measured by a respective standard testing method.
TABLE-US-00014 TABLE 13 Characteristics of the marine fuel
composition in Examples 92-101 Pour Density @ Sulfur Point Flash
Point Viscosity @ ~15.degree. C. (g/cc) (wppm) (.degree. C.)
(.degree. C.) ~50.degree. C. (cSt) Ex. 92 0.930 967 26.5 105.6
151.3 Ex. 93 0.914 968 29.4 145.1 233.3 Ex. 94 0.917 975 30.0 144.9
261.7 Ex. 95 0.920 967 27.0 104.7 151.3 Ex. 96 0.920 999 28.7 125.1
140.9 Ex. 97 0.920 999 28.7 125.1 140.9 Ex. 98 0.928 960 28.6 105.2
140.9 Ex. 99 0.918 960 29.0 104.3 140.9 Ex. 100 0.927 956 29.8
104.9 135.1 Ex. 101 0.919 995 29.9 124.4 135.1
Examples 102-106
[0055] The following are non-limiting Examples 102-106 of exemplary
embodiments of the marine fuel composition described herein. The
residual hydrocarbon component included at least one of two types
of long residues: ATB(1) and ATB(2). The non-hydroprocessed
hydrocarbon component, if used, was slurry oil. The hydroprocessed
hydrocarbon component was ULSD. The characteristics of these
materials are provided in Table 14 below.
TABLE-US-00015 TABLE 14 Characteristics of blending components in
Examples 102-106 Long Long residues residues Characteristic (ATB
(1)) (ATB (2)) Slurry Oil ULSD Density @ ~15.degree. C. (g/cc)
~0.91 ~0.94 ~1.09 ~0.83 Kinematic Viscosity @ ~180 ~880 ~800 ~2
~50.degree. C. or ~122.degree. F. (cSt) Sulfur (wppm) ~1250 ~1130
~4000 ~7 Pour Point (.degree. C.) ~42 ~-2 ~0 ~0 Flash Point
(.degree. C.) ~>110 ~207 ~100 ~60
[0056] Table 15 below summarizes the blend content of the marine
fuel composition in Examples 102-106.
TABLE-US-00016 TABLE 15 Blend content of Examples 102-106 Blend
content Residual Component Non-hydroprocessed Hydroprocessed (wt %)
ATB (1) ATB (2) Slurry Oil ULSD Ex. 102 20 32 5 43 Ex. 103 32 32 2
34 Ex. 104 30 40 0 30 Ex. 105 30 50 0 20 Ex. 106 30 55 0 15
[0057] Table 16 below provides certain characteristics of the
marine fuel composition of Examples 102-106, as measured by the
respective ASTM method. As can be seen below, the marine fuel
composition of Examples 102-106 exhibited a sulfur content that is
less than 0.1 wt %, which would allow these compositions to be used
in geographical locations that are or will be under more stringent
regulations government the sulfur content of marine fuels. In
addition, the marine fuel composition of Examples 102-106 exhibited
characteristics that allow them, if necessary or desired, to meet
specifications that govern residual-based marine fuels,
particularly ISO 8217.
TABLE-US-00017 TABLE 16 Characteristics of the marine fuel
composition of Examples 102-106 Test Method Characteristic Ex. 102
Ex. 103 Ex. 104 Ex. 105 Ex. 106 ASTM API Gravity 27.5 27.3 27.0
25.1 24.5 D4052 @ ~60.degree. F. Density @ 889.3 890.6 892.3 903.2
907.0 ~15.degree. C. (kg/m.sup.3) ASTM Viscosity @ 21.16 13.77
27.03 52.88 62.65 D445 ~122.degree. F. (cSt) ASTM Sulfur 0.094
0.092 0.082 0.089 0.100 D4294 Content (mass %) ASTM Water by
<0.05 <0.05 <0.05 <0.05 <0.05 D95 Distillation (%
(v/v)) ASTM Flash Point 64.5 69.5 71.5 80.5 85.0 D93 ( .degree. C.)
Proc. B Flash Point 148 157 161 177 185 (Automatic) (.degree. F.)
ASTM Pour Point -21 -6 12 6 12 D97 ( .degree. C.) Pour Point -6 21
54 43 54 (.degree. F.) ASTM Accelerated 0.02 0.01 0.02 0.01
<0.01 D4870 Total Proc. B Sediment (% (m/m)) ASTM Ash Content
0.030 0.03 0.033 0.049 0.041 D482 (mass %) IP 501 Vanadium <1 1
1 1 1 (ppm (mg/kg)) Sodium 8 11 12 11 14 (ppm (mg/kg)) Aluminum 6 6
1 <1 1 (ppm (mg/kg)) Silicon 12 15 13 27 10 (ppm (mg/kg))
Calcium 73 69 85 116 114 (ppm (mg/kg)) Zinc 1 1 2 3 2 (ppm (mg/kg))
Phosphorus <1 <1 1 2 1 (ppm (mg/kg)) ASTM Micro 2.58 2.70
2.75 3.57 3.78 D4530 Carbon Residue (% (m/m)) ASTM Total Acid 1.16
1.22 1.49 1.88 2.19 D664 Number (mg KOH/g) IP 570 H.sub.2S Content
0.00 0.00 0.00 <0.01 <0.4 ( ppm (mg/kg)) ISO-FDIS Calculated
790.3 800.3 788.7 788.6 789.9 8217 Carbon Aromaticity Index
(CCAI)
Example 107
[0058] Example 107 is a non-limiting exemplary embodiment of the
marine fuel composition described herein. The relative fuel
composition of the marine fuel composition was about 60 wt % of a
residual hydrocarbon component, about 12 wt % of a
non-hydroprocessed hydrocarbon component, and about 28 wt % of a
hydroprocessed hydrocarbon component. In particular, the residual
hydrocarbon component was long residues or ATB; the
non-hydroprocessed hydrocarbon component included about 4 wt % of a
first type of slurry oil (Slurry Oil (1), about 8 wt % of a second
type of slurry oil (Slurry Oil (2)); and the hydroprocessed
hydrocarbon component was hydrotreated diesel oil. The properties
of these components are listed in Table 17 below.
TABLE-US-00018 TABLE 17 Blend content and characteristics of
blending components in Example 107 Long residues Slurry Oil Slurry
Oil Hydrotreated Characteristic (ATB) (1) (2) Diesel Blend content
(wt %) ~60 ~4 ~8 ~28 Density @ ~15.degree. C. ~0.91 ~0.95 ~1.09
~0.8450 (g/cc) Viscosity @ ~50.degree. C. ~159 ~42 ~220 ~3 (cSt)
Sulfur (wppm) ~1200 ~2700 ~2200 ~50 Pour Point (.degree. C.) ~45
~30 ~3 ~-8 Flash Point (.degree. C.) ~110 ~110 ~155 ~80
[0059] Table 18 below provides certain characteristics, as measured
by the respective ISO method, of the marine fuel composition of
Example 107. As can be seen below, the marine fuel composition of
Example 107 had a sulfur content that is less than 0.1 wt %, which
would allow it to be used in geographical locations that are or
will be under more stringent regulations government the sulfur
content of marine fuels. In addition, the marine fuel composition
of Example 112 exhibited characteristics that allow it, if
necessary or desired, to meet specifications that govern
residual-based marine fuels, particularly ISO 8217.
TABLE-US-00019 TABLE 18 Characteristics of the marine fuel
composition of Example 107 Characteristic Test Method Unit Value
Density at 15.degree. C. ISO 12185 kg/m.sup.3 903.7 Kinematic
Viscosity at 50.degree. C. ISO 3104 mm.sup.2/s 26.78 Total Sulphur
ISO 8754 % m/m 0.097 Flash Point ISO 2719 B .degree. C. 81.0 Water
ISO 3733 % m/m <0.1 Pour Point ISO 3016 .degree. C. 30
(Automatic) Total Sediment Accelerated ISO 10307-2 B % m/m <0.01
Carbon Residue ISO 10370 % m/m 3.03 Ash Content ISO 6245 % m/m
<0.001 Total Acid Number ASTM D 664 mg KOH/g 0.08 Aluminum IP
501 mg/kg <5 Silicon IP 501 mg/kg <10 Aluminum plus Silicon
IP 501 mg/kg <15 Vanadium IP 501 mg/kg 2 Sodium IP 501 mg/kg 15
Calcium IP 501 mg/kg 3 Phosphorus IP 501 mg/kg 1 Zinc IP 501 mg/kg
1 CCAI ISO 8217 800 Hydrogen Sulphide IP 570 A mg/kg <0.60
[0060] Therefore, embodiments of the present invention are well
adapted to attain the ends and advantages mentioned as well as
those that are inherent therein. The particular embodiments
disclosed above are illustrative only, as the present invention may
be modified and practiced in different but equivalent manners
apparent to those skilled in the art having the benefit of the
teachings herein. Furthermore, no limitations are intended to the
details of construction or design herein shown, other than as
described in the claims below. It is therefore evident that the
particular illustrative embodiments disclosed above may be altered,
combined, substituted, or modified and all such variations are
considered within the scope and spirit of the present invention.
The invention illustratively disclosed herein suitably may be
practiced in the absence of any element that is not specifically
disclosed herein and/or any optional element disclosed herein.
While compositions and methods are described in terms of
"comprising," "containing," or "including" various components or
steps, the compositions and methods can also "consist essentially
of" or "consist of" the various components and steps. All numbers
and ranges disclosed above may vary by some amount whether
accompanied by the term "about" or not. In particular, the phrase
"from about a to about b" is equivalent to the phrase "from
approximately a to b," or a similar form thereof. Also, the terms
in the claims have their plain, ordinary meaning unless otherwise
explicitly and clearly defined by the patentee. Moreover, the
indefinite articles "a" or "an," as used in the claims, are defined
herein to mean one or more than one of the element that it
introduces. If there is any conflict in the usages of a word or
term in this specification and one or more patent or other
documents that may be incorporated herein by reference, the
definitions that are consistent with this specification should be
adopted.
* * * * *