US3792984A - Fuel oil blending to improve pour reduction - Google Patents
Fuel oil blending to improve pour reduction Download PDFInfo
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- US3792984A US3792984A US00049991A US3792984DA US3792984A US 3792984 A US3792984 A US 3792984A US 00049991 A US00049991 A US 00049991A US 3792984D A US3792984D A US 3792984DA US 3792984 A US3792984 A US 3792984A
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- pour
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- fatty acid
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/192—Macromolecular compounds
- C10L1/195—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
- C10L1/197—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and an acyloxy group of a saturated carboxylic or carbonic acid
- C10L1/1973—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and an acyloxy group of a saturated carboxylic or carbonic acid mono-carboxylic
Definitions
- This invention is concerned with means for providing a low sulfur, low pour fuel oil blend. More particularly, the invention is concerned with a fuel oil blend containing a major amount of a high pour, low sulfur, waxy residual fuel and a minor amount of a low-waxy, low pour residual fuel oil, this blend having a reduced pour point relative to its components owing to the incorporation therein of certain high molecular weight ethylene-vinyl fatty acid ester copolymers.
- residual fuel oils contain quantities of wax and asphaltic compounds which render them viscous and which sometimes interfere with practical use thereof. Particularly serious problems can be encountered in pumping residual fuel oils to a burner and in making them flow at low temperatures. Other factors to be reckoned with in regard to these oils are the facts that they behave as non-Newtonian liquids at low temperatures; exhibit variable solidifying temperatures and manifest peculiar hysteresis phenomena all of which result in difficulties in equipment design.
- additives in lubricating oils and in so-called middle distillates in order to tie in the wax present therein and to improve flow characteristics at reduced temperatures.
- the additives in question consist either of compounds formed by alkylating benzene or naphthalene derivatives; or, of copolymers of ethylene-vinyl fatty acid ester of a molecular weight up to 3,000 containing from to 25 percent by weight of the vinyl fatty acid ester.
- An equally important object of the claimed invention is to provide a novel fuel oil blend characterized by a low sulfur content and a reduced pour point resulting from the incorporation therein of a small amount of certain ethylene-vinyl fatty acid ester copolymers.
- a further object of the claimed invention is to provide a fuel oil blend which will be stable at different blend temperatures over storage times of up to about 3 months.
- the fuel blend of the invention comprises a major amount (i.e., over 50 percent by volume) of a high pour, waxy, residual fuel oil having an API gravity of about 20.0 to about 25.0; a sulfur content of between about 0.40 wt. percent and about 0.96 wt. percent; a
- a waxy, low pour residual fuel oil which has given particularly good results as the minor constituent of the claimed blend is that known as No. 6 Fuel Oil which has an API gravity of about 12.3, a Furol viscosity of 207.0 at 122F, a pour point of about 40F and a wax content of about 3 percent.
- the pour point depressant additives suitable in the practice of the invention comprise oil soluble ethylenevinyl fatty acid ester copolymers in which the fatty component of the ester has a carbon content of from about 2 to about 6, the copolymers having an average molecular weight of about 20,000 to about 31,000 determined as the Number Average Molecular Weight by the Membrane Osmometry Analytical Method, a vinyl fatty acid ester content of from about 24 to about 34 percent and a melt index of about 5 to about 28.
- the preferred copolymers are sold under the trade name of Elvax by the E. l. Du Pont de Nemours Company, the most suitable being Elvax 250 which contains 27 to 29 percent of vinyl acetate, has an inherent viscosity at F.
- the pour depressant 1s then umformly 28 33 3 dispersed in the fuel oil by injecting it into the residuum 310 24-26 335-465 run downstream in the refinery process area.
- the comggg 2152 ponent to which the pour depressant has been added is 410 174 9 5 3 then thoroughly mixed with the other component of the 460 17-19 214-9 blend.
- Tables IV and V below show the average pour points of dupliate samples at 0, 3 weeks, 6 weeks and i mm as in d by ASTM 1328 difi d 20 3 months. These data show that the blends produced by the invention desirably remain stable over storage The specific properties of the oils used in examples times of a least up to three months.
- Fuel Blend 1 Process for producing a low pour point, low sulfur of a low waxy, low pour, residual fuel oil, bringing one of said oils to a temperature of between about 200 and 400F.; adding to the said oil a pour depressant consisting of an oil soluble, ethylene-vinyl fatty acid ester copolymer in which the fatty acid component of the ester has a carbon content of from about two to about six, said copolymer having a molecular weight of about 20,000 to about 31,000, a vinyl fatty acid ester content of from about 24 to about 34 percent and a melt index of about 5 to about 28; uniformly dispersing said copolymer in said oil at said temperature; and mixing said oils to produce a blend having a pour point substantially lower than either of said oils.
- a pour depressant consisting of an oil soluble, ethylene-vinyl fatty acid ester copolymer in which the fatty acid component of the ester has a carbon content of from about two to about six, said copolymer
- a fuel oil blend characterized by a lowered pour point and a low sulfur content comprising a major amount of a high pour, waxy, residual fuel oil having a pour point of between about 80 and 120F. and a minor amount of a low waxy, low pour, residual fuel oil and an effective pour depressant amount of an oil soluble, ethylene-vinyl fatty acid ester copolymer in which the fatty acid component of the ester has a carbon content of from about two to about six, said copolymer having a molecular weight of between about 20,000 to about 31,000; a vinyl fatty acid ester content of from about 24 to 34 percent, and a melt index of about 5 to about 28.
- composition according to claim 2 wherein the said vinyl ester is vinyl acetate and wherein the said composition contains over percent by volume of the said high-pour fuel oil.
- composition of claim 2 containing 60 percent by volume of said high pour fuel oil and 40 percent by volume of said low pour fuel oil.
- composition of claim 2 wherein said high pour, residual fuel oil has an API gravity ranging between about 20.0 and about 25.0; a sulfur content between about 0.40 weight percent and about 0.96 weight percent; a Furol viscosity at 122F. of about 60 to about 230; a flash point of between 300 and 450F. and a wax content of between about 10 and 20 percent; said low waxy, low pour residual fuel oil having an API gravity of about 10.0 to about 15.0; a Furol viscosity at 122F. of about 150 to about 250; a flash point of about 220 to about 350F.; a pour point of about 25F.
- a wax content of about 2 to about 5 weight perfuel oil blend comprising blending a major amount of 50 cent and a sulfur content of between about 0.50 and a high pour, waxy residual fuel oil having a pour point of between about 80 and l20F.; and a minor amount about 0.90 weight percent.
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Emergency Medicine (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Liquid Carbonaceous Fuels (AREA)
Abstract
A low pour point fuel oil blend is prepared from a major amount of a high pour point, low sulfur, waxy, residual fuel and a minor amount of low-waxy, low pour, residual fuel oil by adding thereto from 0.01 to 0.5 percent by weight of an oil soluble ethylenevinyl fatty acid ester copolymer in which the fatty acid component of the ester has a carbon content of from about 2 to about 6; the copolymer having a molecular weight between about 20,000 and 31,000, a melt index of about 5 to about 28 and a vinyl fatty acid ester content of from about 24 to about 34 percent. The copolymer may be added either in a water-glycol emulsion or in a hydrocarbon to one of the blend components which has been heated to between about 200* to 400*F.
Description
United States Patent [191 v Cole et al.
[ FUEL OIL BLENDING TO IMPROVE POUR I REDUCTION p [75] Inventors: Edmund W. Cole, Poughkeepsie;
Jerzy J. Bialy, Lagrangeville; William M. Sweeney, Wappingers Falls, all of N.Y.
[73] Assignee: Texaco Inc., New York, N.Y.
[22] Filed: June 25, 1970 [21] Appl. No.: 49,991
Related US. Application Data [63] Continuation-impart of Ser. No. 878,919, Nov. 21,
. 1969, abandoned.
[52] US. Cl. 44/62, 44/70 [51] Int. Cl C101 1/18 [58] Field of Search 44/62, 70; 252/56 [56 References Cited UNITED STATES PATENTS 2,664,388 12/1953 Winterhalter 208/15 X 3,567,639 3/1971 Aaron et al 252/56 Feb. 19, 1974 Primary Examiner Daniel E. Wyman Assistant ExaminerY. H.- Smith Attorney, Agent, or FinnThomas H. Whaley; Carl G. Ries 57 ABSTRACT index of about 5 to about 28 and a vinyl fatty acid' ester content of from about 24 to about 34 percent. The copolymer may beadded either in a water-glycol emulsion or in a hydrocarbon to one of the blend components which has been heated to between about 200 to 400F.
6 Claims, No Drawings 1 FUEL OIL BLENDING TO IMPROVE POUR REDUCTION CROSS-REFERENCE TO CO-PENDlNG APPLICATION This application is a continuation-in-part application of commonly assigned application Ser. No. 878,919 filed Nov. 21, 1969 now abandoned.
This invention is concerned with means for providing a low sulfur, low pour fuel oil blend. More particularly, the invention is concerned with a fuel oil blend containing a major amount of a high pour, low sulfur, waxy residual fuel and a minor amount of a low-waxy, low pour residual fuel oil, this blend having a reduced pour point relative to its components owing to the incorporation therein of certain high molecular weight ethylene-vinyl fatty acid ester copolymers.
As is well known, residual fuel oils contain quantities of wax and asphaltic compounds which render them viscous and which sometimes interfere with practical use thereof. Particularly serious problems can be encountered in pumping residual fuel oils to a burner and in making them flow at low temperatures. Other factors to be reckoned with in regard to these oils are the facts that they behave as non-Newtonian liquids at low temperatures; exhibit variable solidifying temperatures and manifest peculiar hysteresis phenomena all of which result in difficulties in equipment design.
One approach used in making these oils easier to handle has been to subject them to fairly lengthy and costly dewaxing procedures.
Another approach which has been suggested and tried in order to bring the viscosity of residual fuel oils to suitable levels has been to dilute or cut them with a major amount of lighter distillate oils. This procedure is expensive because of the considerably higher cost of the distillate oils relative to that of residual oils.
In recent years it has been recommended to incorporate additives in lubricating oils and in so-called middle distillates in order to tie in the wax present therein and to improve flow characteristics at reduced temperatures. The additives in question consist either of compounds formed by alkylating benzene or naphthalene derivatives; or, of copolymers of ethylene-vinyl fatty acid ester of a molecular weight up to 3,000 containing from to 25 percent by weight of the vinyl fatty acid ester.
ln commonly assigned, co-pending application, U. S. Ser. No. 832,856, filed June 12, 1969, now abandoned, there has been disclosed and claimed a residual fuel oil composition containing an additive comprising a middle distillate heating oil boiling from about 350 to 650F and an effective pour point depressant amount of an oil soluble ethylene-vinyl fatty acid ester copolymer or resin in which the fatty acid component of the waxy residual fuel oils with low-waxy, low pour residual fuel oils to give large increases in pour reduction without employing elaborate dewaxing procedures.
An equally important object of the claimed invention is to provide a novel fuel oil blend characterized by a low sulfur content and a reduced pour point resulting from the incorporation therein of a small amount of certain ethylene-vinyl fatty acid ester copolymers.
A further object of the claimed invention is to provide a fuel oil blend which will be stable at different blend temperatures over storage times of up to about 3 months.
Other objects of this invention will in part be obvious and in part hereinafter pointed out.
The fuel blend of the invention comprises a major amount (i.e., over 50 percent by volume) of a high pour, waxy, residual fuel oil having an API gravity of about 20.0 to about 25.0; a sulfur content of between about 0.40 wt. percent and about 0.96 wt. percent; a
Furol viscosity at 122F of about 60 to about 230; a
flash point of between about 300 and 450F, with a wax content of between about 10 and 20 percent; and a minor amount (i.e., less than 50 percent by volume) of a low-waxy, low pour residual fuel oil having an API gravity of about 10.0 to about 15.0; a Furol viscosity at 122F of about 150 to about 250; a flash point of about 220 to about 350F; a pour point of between about 25F and about 45F; a wax content of between about 2 and 5 weight per cent with a sulfur content of between about 0.50 and about 0.90 weight percent. A waxy, low pour residual fuel oil which has given particularly good results as the minor constituent of the claimed blend is that known as No. 6 Fuel Oil which has an API gravity of about 12.3, a Furol viscosity of 207.0 at 122F, a pour point of about 40F and a wax content of about 3 percent.
The pour point depressant additives suitable in the practice of the invention comprise oil soluble ethylenevinyl fatty acid ester copolymers in which the fatty component of the ester has a carbon content of from about 2 to about 6, the copolymers having an average molecular weight of about 20,000 to about 31,000 determined as the Number Average Molecular Weight by the Membrane Osmometry Analytical Method, a vinyl fatty acid ester content of from about 24 to about 34 percent and a melt index of about 5 to about 28. The preferred copolymers are sold under the trade name of Elvax by the E. l. Du Pont de Nemours Company, the most suitable being Elvax 250 which contains 27 to 29 percent of vinyl acetate, has an inherent viscosity at F. of 0.78 dcl./gm. in toluene; a softening point as d m ne y A-S-Ll L E Z Q llwfiftas d point in paraffin wax of F, a Melt Index of 12-18 and a molecular weight of 23,000 to 27,000. The material is supplied by its manufacturer for use in blends containing wax to provide toughness, flexibility, adhesion and barrier properties properties having nothing common with pour point reduction in fuel oil blends.
basic aliphatic carboxylic acid. The characterization of.
the various Elvax additives is given in Table A below:
TABLE A TABLE 111 Vinyl Acetate 100% Stocks Elvax 250, ELVAX" in Copolymer M lt I d Blended at 350 F .125 .094 .062 .031 F/18 1 93 94 94 97 F/18 2 94 94 98 99 F/18 3 97 90 94 94 Louisiana No. 6 37 33 36 40 40 3942 I 4540 10 In practice the claimed fuel blends suitably are pre- 150 32-34 22-23 pared 1n the following manner. Either of the fuel oil 210 27-29 335-465 220 2749 25475 components is brought up to a temperature of between 240 v 27-29 I 22-28 200 and 400F. The pour depressant 1s then umformly 28 33 3 dispersed in the fuel oil by injecting it into the residuum 310 24-26 335-465 run downstream in the refinery process area. The comggg 2152 ponent to which the pour depressant has been added is 410 174 9 5 3 then thoroughly mixed with the other component of the 460 17-19 214-9 blend. Tables IV and V below show the average pour points of dupliate samples at 0, 3 weeks, 6 weeks and i mm as in d by ASTM 1328 difi d 20 3 months. These data show that the blends produced by the invention desirably remain stable over storage The specific properties of the oils used in examples times of a least up to three months. The data show also of the practice of the invention appear in Table I below: that lesser quantities of the additives lower the pour TABLE I BASE STOCKS INSPECTION TESTS F/18 F/18 F/18 No.6 Base Stock Fuel Oil (1) Fuel Oil (2) Fuel Oil (3) Fuel Oil TESTS (iravity, API 22.3 23.5 22.6 12.3 Flash Point 425 395 330 270 (COC), "F Viscosity. SUS
at 122F 1043 1971 701 1968 at 15()F 435 404 315 748 ASTM Four 100 100 90 Point, F 1 Carbon Residue. 6.8 6.99 6.78 13.61 WTf/v Wax Content, 16.80 15.99 12.36 3.05 WTf/r Sulfur. WT/Vr 0.96 0.54 0.84 0.74
It was observed in experimental work leading to the points to a lesser degree. The data moreover show that present invention that the copolymer additives did not blending the fuel and additives at 350F. gives a slightly significantly lower the pour points of either of the comsmaller reduction than those blending at 200F. ponents of the blends themselves. Thus addition of TABLE IV 0.125 percent by weight of Elvax 250 to 100 percent of the F/18 1 oil) lowers the average pour point Averages of Duplicate Samples thereof by only 1F. Similarly 0.125 percent by we1ght F I 3 Weeks. 6 Weeks. 3 Months U8 IXIUTC of the same add1t1ve lowers the pour pomt of the No. 60 (V) F/]8 4o% (v) 6 011 only by about 6 F. Unexpectedly th1s last men- N0. 6 Blended at Elvax 250, tioned amount of Elvax 250 lowers the pour point of a 200 O 60/40 percent by volume mixture of these two oils by (l) N05 80 53 53 76 27. This will be seen in Tables 2 and 3 below. W18 No. 6 a 82 52 57 67 81 F/18 3 N6. 6 79 44 47 49 69 TABLE 11 TABLE \1 Averages of Duplicate Samples at 0, 3 weeks, 6 weeks, 3 months Fuel Mixture 100% SIOCkH Elvax 250, 60 (v FMS-40% v Blended at 200F 0 .125 .094 .062 .031 No. 6 Blended at Elvax 250,
F/18(1) 92 91 92 94 F/18(2) 98 96 91 91 F/1s 1 -N6.6 83 6O 74 81 F/18(3) 96 88 89 91 F/l8(2)-No.6 84 71 73 76 Louisiana No. 6 32 26 29 2s H18 3 NO. 6 77 62 70 blend, it will be preferred to dissolve them in a hydrocarbon such as toluene, kerosene, and the like and to emuls'ify with a mixture of ethylene glycol, water and detergent to form an oil in water emulsion. The pour point of the resultant emulsion will be essentially that of the water-glycol phase. A practical example of this approach is the use of a water-glycol emulsion which contain 22.3 percent of the polymer.
On the contrary, where it is desired to use a temperature of around 250C. for incorporating the copolymers, it will be preferred to add the copolymers to the oil at the said temperature in the form of a hydrocarbon solution in, for example, toluene. This can be done by making a 12 /2 percent Udex extract hydrocarbon blend incorporating the polymer.
The unexpected and unobvious nature of the present invention can best be appreciated from the comparison tabulated below in Table VI of the pour points obtained with various additives differing in vinyl acetate content and melt index. It will be apparent from Table VI that only certain additives reduce the pour point while certain others have little effect or even increase it. Thus the copolymer Elvax 40 having a percent of vinyl acetate in excess of 34 gave a po'ur point of 80F, a reduction of only 5F from the control and Elvax 460 appeared to increase it by 5F.
TABLE VI Pour Point (F) Elvax No. (0.1% in Blend) FIB/No. 6 Fuel Blend 1. Process for producing a low pour point, low sulfur of a low waxy, low pour, residual fuel oil, bringing one of said oils to a temperature of between about 200 and 400F.; adding to the said oil a pour depressant consisting of an oil soluble, ethylene-vinyl fatty acid ester copolymer in which the fatty acid component of the ester has a carbon content of from about two to about six, said copolymer having a molecular weight of about 20,000 to about 31,000, a vinyl fatty acid ester content of from about 24 to about 34 percent and a melt index of about 5 to about 28; uniformly dispersing said copolymer in said oil at said temperature; and mixing said oils to produce a blend having a pour point substantially lower than either of said oils.
2. A fuel oil blend characterized by a lowered pour point and a low sulfur content comprising a major amount of a high pour, waxy, residual fuel oil having a pour point of between about 80 and 120F. and a minor amount of a low waxy, low pour, residual fuel oil and an effective pour depressant amount of an oil soluble, ethylene-vinyl fatty acid ester copolymer in which the fatty acid component of the ester has a carbon content of from about two to about six, said copolymer having a molecular weight of between about 20,000 to about 31,000; a vinyl fatty acid ester content of from about 24 to 34 percent, and a melt index of about 5 to about 28.
3. The composition according to claim 2 wherein the said vinyl ester is vinyl acetate and wherein the said composition contains over percent by volume of the said high-pour fuel oil.
4. The composition according to claim 2 wherein said copolymer is present in a concentration ranging from about 0.01 to about 0.5 percent by weight.
5. The composition of claim 2 containing 60 percent by volume of said high pour fuel oil and 40 percent by volume of said low pour fuel oil.
6. The composition of claim 2, wherein said high pour, residual fuel oil has an API gravity ranging between about 20.0 and about 25.0; a sulfur content between about 0.40 weight percent and about 0.96 weight percent; a Furol viscosity at 122F. of about 60 to about 230; a flash point of between 300 and 450F. and a wax content of between about 10 and 20 percent; said low waxy, low pour residual fuel oil having an API gravity of about 10.0 to about 15.0; a Furol viscosity at 122F. of about 150 to about 250; a flash point of about 220 to about 350F.; a pour point of about 25F. and 45F a wax content of about 2 to about 5 weight perfuel oil blend comprising blending a major amount of 50 cent and a sulfur content of between about 0.50 and a high pour, waxy residual fuel oil having a pour point of between about 80 and l20F.; and a minor amount about 0.90 weight percent.
Claims (5)
- 2. A fuel oil blend characterized by a lowered pour point and a low sulfur content comprising a major amount of a high pour, waxy, residual fuel oil having a pour point of between about 80* and 120*F. and a minor amount of a low waxy, low pour, residual fuel oil and an effective pour depressant amount of an oil soluble, ethylene-vinyl fatty acid ester copolymer in which the fatty acid component of the ester has a carbon content of from about two to about six, said copolymer having a molecular weight of between about 20,000 to about 31,000; a vinyl fatty acid ester content of from about 24 to 34 percent, and a melt index of about 5 to about 28.
- 3. The composition according to claim 2 wherein the said vinyl ester is vinyl acetate and wherein the said composition contains over 50 percent by volume of the said high-pour fuel oil.
- 4. The composition according to claim 2 wherein said copolymer is present in a concentration ranging from about 0.01 to about 0.5 percent by weight.
- 5. The composition of claim 2 containing 60 percent by volume of said high pour fuel oil and 40 percent by volume of said low pour fuel oil.
- 6. The composition of claim 2, wherein said high pour, residual fuel oil has an API gravity ranging between about 20.0 and about 25.0; a sulfur content between about 0.40 weight percent and about 0.96 weight percent; a Furol viscosity at 122*F. of about 60 to about 230; a flash point of between 300* and 450*F. and a wax content of between about 10 and 20 percent; said low waxy, low pour residual fuel oil having an API gravity of about 10.0 to about 15.0; a Furol viscosity at 122*F. of about 150 to about 250; a flash point of about 220 to about 350*F.; a pour point of about 25*F. and 45*F.; a wax content of about 2 to about 5 weight percent and a sulfur content of between about 0.50 and about 0.90 weight percent.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US4999170A | 1970-06-25 | 1970-06-25 |
Publications (1)
Publication Number | Publication Date |
---|---|
US3792984A true US3792984A (en) | 1974-02-19 |
Family
ID=21962813
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US00049991A Expired - Lifetime US3792984A (en) | 1970-06-25 | 1970-06-25 | Fuel oil blending to improve pour reduction |
Country Status (6)
Country | Link |
---|---|
US (1) | US3792984A (en) |
AT (1) | AT309645B (en) |
BR (1) | BR7105237D0 (en) |
CA (1) | CA934549A (en) |
CH (1) | CH557869A (en) |
DE (1) | DE2130816A1 (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4074978A (en) * | 1973-10-12 | 1978-02-21 | Exxon Research & Engineering Co. | Combination of asphaltenes with flow improver polymers to improve the flow properties of high boiling fuel oils |
US4138227A (en) * | 1976-10-28 | 1979-02-06 | Texaco Inc. | Production of low pour, low sulfur fuel oils |
US4396398A (en) * | 1980-10-01 | 1983-08-02 | The Secretary Of State For Defence In Her Britannic Majesty's Government Of The United Kingdom Of Great Britain And Northern Ireland | Antimisting additives for aviation fuels |
US5851429A (en) * | 1996-04-08 | 1998-12-22 | The Lubrizol Corporation | Dispersions of waxy pour point depressants |
GB2308129B (en) * | 1995-11-29 | 1999-11-10 | Lubrizol Corp | Dispersions of waxy pour point depressants |
US20080210595A1 (en) * | 2005-07-18 | 2008-09-04 | Oiltreid Limited Liabilities Company | Light Oil Fuel |
US10087310B2 (en) | 2013-03-15 | 2018-10-02 | California Institute Of Technology | Associative polymers and related compositions, methods and systems |
US10119084B2 (en) | 2015-09-18 | 2018-11-06 | California Institute Of Technology | Associative polymers to control formation of particulate matter from ignitable compositions and related compositions, methods and systems |
US10400186B2 (en) | 2009-04-17 | 2019-09-03 | California Institute Of Technology | Associative polymers for mist-control |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2664388A (en) * | 1951-09-19 | 1953-12-29 | Socony Vacuum Oil Co Inc | Hydrocarbon fuel oil of lowered pour point |
US3567639A (en) * | 1966-06-01 | 1971-03-02 | Exxon Research Engineering Co | Hydrocarbon-containing compositions |
-
1970
- 1970-06-25 US US00049991A patent/US3792984A/en not_active Expired - Lifetime
-
1971
- 1971-06-22 DE DE19712130816 patent/DE2130816A1/en active Pending
- 1971-06-24 CH CH923771A patent/CH557869A/en not_active IP Right Cessation
- 1971-06-25 CA CA116722A patent/CA934549A/en not_active Expired
- 1971-06-25 AT AT552271A patent/AT309645B/en not_active IP Right Cessation
- 1971-08-13 BR BR5237/71A patent/BR7105237D0/en unknown
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2664388A (en) * | 1951-09-19 | 1953-12-29 | Socony Vacuum Oil Co Inc | Hydrocarbon fuel oil of lowered pour point |
US3567639A (en) * | 1966-06-01 | 1971-03-02 | Exxon Research Engineering Co | Hydrocarbon-containing compositions |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4074978A (en) * | 1973-10-12 | 1978-02-21 | Exxon Research & Engineering Co. | Combination of asphaltenes with flow improver polymers to improve the flow properties of high boiling fuel oils |
US4138227A (en) * | 1976-10-28 | 1979-02-06 | Texaco Inc. | Production of low pour, low sulfur fuel oils |
US4396398A (en) * | 1980-10-01 | 1983-08-02 | The Secretary Of State For Defence In Her Britannic Majesty's Government Of The United Kingdom Of Great Britain And Northern Ireland | Antimisting additives for aviation fuels |
GB2308129B (en) * | 1995-11-29 | 1999-11-10 | Lubrizol Corp | Dispersions of waxy pour point depressants |
US5851429A (en) * | 1996-04-08 | 1998-12-22 | The Lubrizol Corporation | Dispersions of waxy pour point depressants |
US7695610B2 (en) | 2005-07-18 | 2010-04-13 | Oiltreid Limited Liabilities Company | Light fuel oil |
US20080210595A1 (en) * | 2005-07-18 | 2008-09-04 | Oiltreid Limited Liabilities Company | Light Oil Fuel |
US10400186B2 (en) | 2009-04-17 | 2019-09-03 | California Institute Of Technology | Associative polymers for mist-control |
US12116540B2 (en) | 2009-04-17 | 2024-10-15 | California Institute Of Technology | Associative polymers for mist-control |
US10087310B2 (en) | 2013-03-15 | 2018-10-02 | California Institute Of Technology | Associative polymers and related compositions, methods and systems |
US10494509B2 (en) | 2013-03-15 | 2019-12-03 | California Institute Of Technology | Associative polymers and related compositions, methods and systems |
US10119084B2 (en) | 2015-09-18 | 2018-11-06 | California Institute Of Technology | Associative polymers to control formation of particulate matter from ignitable compositions and related compositions, methods and systems |
US10428286B2 (en) | 2015-09-18 | 2019-10-01 | California Institute Of Technology | Associative polymers for use in a flow and related compositions, methods and systems |
Also Published As
Publication number | Publication date |
---|---|
DE2130816A1 (en) | 1972-03-16 |
CH557869A (en) | 1975-01-15 |
CA934549A (en) | 1973-10-02 |
BR7105237D0 (en) | 1973-05-03 |
AT309645B (en) | 1973-08-27 |
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