US2993772A - Acid additives - Google Patents
Acid additives Download PDFInfo
- Publication number
- US2993772A US2993772A US790352A US79035259A US2993772A US 2993772 A US2993772 A US 2993772A US 790352 A US790352 A US 790352A US 79035259 A US79035259 A US 79035259A US 2993772 A US2993772 A US 2993772A
- Authority
- US
- United States
- Prior art keywords
- engine
- fuel
- succinic acid
- deposits
- test
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000002253 acid Substances 0.000 title description 17
- 239000000654 additive Substances 0.000 title description 14
- 239000000446 fuel Substances 0.000 claims description 81
- 238000002485 combustion reaction Methods 0.000 claims description 31
- 238000000034 method Methods 0.000 claims description 18
- 229930195733 hydrocarbon Natural products 0.000 claims description 16
- 150000002430 hydrocarbons Chemical class 0.000 claims description 16
- 239000004215 Carbon black (E152) Substances 0.000 claims description 14
- 150000008064 anhydrides Chemical class 0.000 claims description 14
- 230000008569 process Effects 0.000 claims description 12
- 238000009835 boiling Methods 0.000 claims description 11
- 230000002401 inhibitory effect Effects 0.000 claims description 7
- KDYFGRWQOYBRFD-UHFFFAOYSA-N succinic acid Chemical compound OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 claims description 5
- 230000015572 biosynthetic process Effects 0.000 claims description 4
- 239000001384 succinic acid Substances 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 1
- 238000012360 testing method Methods 0.000 description 39
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 32
- 150000001875 compounds Chemical class 0.000 description 23
- 239000000203 mixture Substances 0.000 description 17
- -1 alkenyl succinic acid salts Chemical class 0.000 description 15
- MRMOZBOQVYRSEM-UHFFFAOYSA-N tetraethyllead Chemical compound CC[Pb](CC)(CC)CC MRMOZBOQVYRSEM-UHFFFAOYSA-N 0.000 description 14
- 230000006835 compression Effects 0.000 description 12
- 238000007906 compression Methods 0.000 description 12
- 230000000694 effects Effects 0.000 description 11
- 239000003921 oil Substances 0.000 description 9
- RINCXYDBBGOEEQ-UHFFFAOYSA-N succinic anhydride Chemical compound O=C1CCC(=O)O1 RINCXYDBBGOEEQ-UHFFFAOYSA-N 0.000 description 8
- 230000000996 additive effect Effects 0.000 description 7
- 125000004432 carbon atom Chemical group C* 0.000 description 7
- 238000005260 corrosion Methods 0.000 description 6
- 230000007797 corrosion Effects 0.000 description 6
- YAXXOCZAXKLLCV-UHFFFAOYSA-N 3-dodecyloxolane-2,5-dione Chemical class CCCCCCCCCCCCC1CC(=O)OC1=O YAXXOCZAXKLLCV-UHFFFAOYSA-N 0.000 description 5
- 230000003197 catalytic effect Effects 0.000 description 5
- 238000005474 detonation Methods 0.000 description 5
- 239000003112 inhibitor Substances 0.000 description 5
- 235000011044 succinic acid Nutrition 0.000 description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- 150000007513 acids Chemical class 0.000 description 4
- 150000001336 alkenes Chemical class 0.000 description 4
- 239000006079 antiknock agent Substances 0.000 description 4
- 239000002826 coolant Substances 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 150000002611 lead compounds Chemical class 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- 239000011593 sulfur Substances 0.000 description 4
- 229910052717 sulfur Inorganic materials 0.000 description 4
- 239000002966 varnish Substances 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- 239000008186 active pharmaceutical agent Substances 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 3
- 229910052753 mercury Inorganic materials 0.000 description 3
- 239000003607 modifier Substances 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- PAAZPARNPHGIKF-UHFFFAOYSA-N 1,2-dibromoethane Chemical compound BrCCBr PAAZPARNPHGIKF-UHFFFAOYSA-N 0.000 description 2
- IIZPXYDJLKNOIY-JXPKJXOSSA-N 1-palmitoyl-2-arachidonoyl-sn-glycero-3-phosphocholine Chemical compound CCCCCCCCCCCCCCCC(=O)OC[C@H](COP([O-])(=O)OCC[N+](C)(C)C)OC(=O)CCC\C=C/C\C=C/C\C=C/C\C=C/CCCCC IIZPXYDJLKNOIY-JXPKJXOSSA-N 0.000 description 2
- RURPJGZXBHYNEM-UHFFFAOYSA-N 2-[2-[(2-hydroxyphenyl)methylideneamino]propyliminomethyl]phenol Chemical compound C=1C=CC=C(O)C=1C=NC(C)CN=CC1=CC=CC=C1O RURPJGZXBHYNEM-UHFFFAOYSA-N 0.000 description 2
- CQHADWBXOMARTO-UHFFFAOYSA-N 3-prop-1-enyloxolane-2,5-dione Chemical compound CC=CC1CC(=O)OC1=O CQHADWBXOMARTO-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 125000003342 alkenyl group Chemical group 0.000 description 2
- 150000001412 amines Chemical class 0.000 description 2
- 150000003863 ammonium salts Chemical class 0.000 description 2
- 230000003373 anti-fouling effect Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 2
- 229910052794 bromium Inorganic materials 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 230000002939 deleterious effect Effects 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 239000000787 lecithin Substances 0.000 description 2
- 229940067606 lecithin Drugs 0.000 description 2
- 235000010445 lecithin Nutrition 0.000 description 2
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000010705 motor oil Substances 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 230000000979 retarding effect Effects 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 239000003381 stabilizer Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 1
- SYSJYMFBTIURJC-UHFFFAOYSA-N 2-(1,2-diiodooctyl)butanedioic acid Chemical compound CCCCCCC(I)C(I)C(C(O)=O)CC(O)=O SYSJYMFBTIURJC-UHFFFAOYSA-N 0.000 description 1
- ABRQEKLWRRPQTC-UHFFFAOYSA-N 2-(3,3-dimethylbut-1-enyl)butanedioic acid Chemical compound CC(C)(C)C=CC(C(O)=O)CC(O)=O ABRQEKLWRRPQTC-UHFFFAOYSA-N 0.000 description 1
- IFKFNEFGEWVZIM-UHFFFAOYSA-N 2-(4-ethylhex-1-enyl)butanedioic acid Chemical compound CCC(CC)CC=CC(C(O)=O)CC(O)=O IFKFNEFGEWVZIM-UHFFFAOYSA-N 0.000 description 1
- FALRKNHUBBKYCC-UHFFFAOYSA-N 2-(chloromethyl)pyridine-3-carbonitrile Chemical compound ClCC1=NC=CC=C1C#N FALRKNHUBBKYCC-UHFFFAOYSA-N 0.000 description 1
- HLOQHECIPXZHSX-MDZDMXLPSA-N 2-[(e)-dec-1-enyl]butanedioic acid Chemical compound CCCCCCCC\C=C\C(C(O)=O)CC(O)=O HLOQHECIPXZHSX-MDZDMXLPSA-N 0.000 description 1
- QDCPNGVVOWVKJG-VAWYXSNFSA-N 2-[(e)-dodec-1-enyl]butanedioic acid Chemical compound CCCCCCCCCC\C=C\C(C(O)=O)CC(O)=O QDCPNGVVOWVKJG-VAWYXSNFSA-N 0.000 description 1
- XACKAZKMZQZZDT-MDZDMXLPSA-N 2-[(e)-octadec-9-enyl]butanedioic acid Chemical compound CCCCCCCC\C=C\CCCCCCCCC(C(O)=O)CC(O)=O XACKAZKMZQZZDT-MDZDMXLPSA-N 0.000 description 1
- PFBBCIYIKJWDIN-BUHFOSPRSA-N 2-[(e)-tetradec-1-enyl]butanedioic acid Chemical compound CCCCCCCCCCCC\C=C\C(C(O)=O)CC(O)=O PFBBCIYIKJWDIN-BUHFOSPRSA-N 0.000 description 1
- FGDWASZPMIGAFI-UHFFFAOYSA-N 2-but-1-enylbutanedioic acid Chemical compound CCC=CC(C(O)=O)CC(O)=O FGDWASZPMIGAFI-UHFFFAOYSA-N 0.000 description 1
- FJZNROVGLPJDEE-UHFFFAOYSA-N 2-ethenylbutanedioic acid Chemical compound OC(=O)CC(C=C)C(O)=O FJZNROVGLPJDEE-UHFFFAOYSA-N 0.000 description 1
- FHLXKMYDQSUXJY-UHFFFAOYSA-N 2-hexacos-1-enylbutanedioic acid Chemical compound CCCCCCCCCCCCCCCCCCCCCCCCC=CC(C(O)=O)CC(O)=O FHLXKMYDQSUXJY-UHFFFAOYSA-N 0.000 description 1
- ZJVMHPVIAUKERS-UHFFFAOYSA-N 2-hexylbutanedioic acid Chemical compound CCCCCCC(C(O)=O)CC(O)=O ZJVMHPVIAUKERS-UHFFFAOYSA-N 0.000 description 1
- RAJIUSUUWAFGME-UHFFFAOYSA-N 3-(1,2-dibromo-2-methylpentadec-3-enyl)oxolane-2,5-dione Chemical compound CCCCCCCCCCCC=CC(C)(Br)C(Br)C1CC(=O)OC1=O RAJIUSUUWAFGME-UHFFFAOYSA-N 0.000 description 1
- AMJYNJWHZOZUIZ-UHFFFAOYSA-N 3-(1,2-diiodotetracos-1-enyl)oxolane-2,5-dione Chemical compound CCCCCCCCCCCCCCCCCCCCCCC(I)=C(I)C1CC(=O)OC1=O AMJYNJWHZOZUIZ-UHFFFAOYSA-N 0.000 description 1
- ACYSNJVODXTRAQ-UHFFFAOYSA-N 3-(2-methylhept-1-enyl)oxolane-2,5-dione Chemical compound CCCCCC(C)=CC1CC(=O)OC1=O ACYSNJVODXTRAQ-UHFFFAOYSA-N 0.000 description 1
- KFEQNMBDMDWBAL-UHFFFAOYSA-N 3-(2-propan-2-ylpent-1-enyl)oxolane-2,5-dione Chemical compound CCCC(C(C)C)=CC1CC(=O)OC1=O KFEQNMBDMDWBAL-UHFFFAOYSA-N 0.000 description 1
- UZLNNZUYUHUIGI-UHFFFAOYSA-N 3-(2-propylhex-1-enyl)oxolane-2,5-dione Chemical compound CCCCC(CCC)=CC1CC(=O)OC1=O UZLNNZUYUHUIGI-UHFFFAOYSA-N 0.000 description 1
- FDKTYZZWPLTXCW-UHFFFAOYSA-N 3-(2-tert-butyl-3-ethylpent-1-enyl)oxolane-2,5-dione Chemical compound CCC(CC)C(C(C)(C)C)=CC1CC(=O)OC1=O FDKTYZZWPLTXCW-UHFFFAOYSA-N 0.000 description 1
- GPEKWZNZRVQKNQ-UHFFFAOYSA-N 3-(3-butyloct-1-enyl)oxolane-2,5-dione Chemical compound CCCCCC(CCCC)C=CC1CC(=O)OC1=O GPEKWZNZRVQKNQ-UHFFFAOYSA-N 0.000 description 1
- WVRNUXJQQFPNMN-VAWYXSNFSA-N 3-[(e)-dodec-1-enyl]oxolane-2,5-dione Chemical compound CCCCCCCCCC\C=C\C1CC(=O)OC1=O WVRNUXJQQFPNMN-VAWYXSNFSA-N 0.000 description 1
- UWERUIGPWOVNGG-UHFFFAOYSA-N 3-dec-1-enyloxolane-2,5-dione Chemical compound CCCCCCCCC=CC1CC(=O)OC1=O UWERUIGPWOVNGG-UHFFFAOYSA-N 0.000 description 1
- YOWKKGPNCDIFFB-UHFFFAOYSA-N 3-decyloxolane-2,5-dione Chemical compound CCCCCCCCCCC1CC(=O)OC1=O YOWKKGPNCDIFFB-UHFFFAOYSA-N 0.000 description 1
- QRCRYGXAOIFJGN-UHFFFAOYSA-N 3-ethenyloxolane-2,5-dione Chemical class C=CC1CC(=O)OC1=O QRCRYGXAOIFJGN-UHFFFAOYSA-N 0.000 description 1
- YRTGWRSQRUHPKX-UHFFFAOYSA-N 3-ethyloxolane-2,5-dione Chemical compound CCC1CC(=O)OC1=O YRTGWRSQRUHPKX-UHFFFAOYSA-N 0.000 description 1
- DEILKUZHRZGBOK-UHFFFAOYSA-N 3-hept-1-enyloxolane-2,5-dione Chemical compound CCCCCC=CC1CC(=O)OC1=O DEILKUZHRZGBOK-UHFFFAOYSA-N 0.000 description 1
- MHALQPUFCVTXKV-UHFFFAOYSA-N 3-hex-1-enyloxolane-2,5-dione Chemical compound CCCCC=CC1CC(=O)OC1=O MHALQPUFCVTXKV-UHFFFAOYSA-N 0.000 description 1
- HJGXRNVSLRUWAC-UHFFFAOYSA-N 3-hexacos-1-enyloxolane-2,5-dione Chemical compound CCCCCCCCCCCCCCCCCCCCCCCCC=CC1CC(=O)OC1=O HJGXRNVSLRUWAC-UHFFFAOYSA-N 0.000 description 1
- RSPWVGZWUBNLQU-UHFFFAOYSA-N 3-hexadec-1-enyloxolane-2,5-dione Chemical compound CCCCCCCCCCCCCCC=CC1CC(=O)OC1=O RSPWVGZWUBNLQU-UHFFFAOYSA-N 0.000 description 1
- ZJFCVUTYZHUNSW-UHFFFAOYSA-N 3-octadecyloxolane-2,5-dione Chemical compound CCCCCCCCCCCCCCCCCCC1CC(=O)OC1=O ZJFCVUTYZHUNSW-UHFFFAOYSA-N 0.000 description 1
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 1
- GPNQBNQJRIBZJC-UHFFFAOYSA-N CCCCCCCCCCCCCCCCCCCCCCCCCCCCCC=CC1CC(=O)OC1=O Chemical compound CCCCCCCCCCCCCCCCCCCCCCCCCCCCCC=CC1CC(=O)OC1=O GPNQBNQJRIBZJC-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 241000283111 Macroderes minutus Species 0.000 description 1
- 241000722921 Tulipa gesneriana Species 0.000 description 1
- ZUFOPGXRJSRHQV-UHFFFAOYSA-N [Pb].C=C.C=C.C=C.C=C Chemical compound [Pb].C=C.C=C.C=C.C=C ZUFOPGXRJSRHQV-UHFFFAOYSA-N 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 229920002877 acrylic styrene acrylonitrile Polymers 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000029936 alkylation Effects 0.000 description 1
- 238000005804 alkylation reaction Methods 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000001351 cycling effect Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 150000005826 halohydrocarbons Chemical class 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- KCYQMQGPYWZZNJ-BQYQJAHWSA-N hydron;2-[(e)-oct-1-enyl]butanedioate Chemical compound CCCCCC\C=C\C(C(O)=O)CC(O)=O KCYQMQGPYWZZNJ-BQYQJAHWSA-N 0.000 description 1
- 229910001410 inorganic ion Inorganic materials 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 239000011630 iodine Substances 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 238000006317 isomerization reaction Methods 0.000 description 1
- 238000009533 lab test Methods 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000006078 metal deactivator Substances 0.000 description 1
- 150000002790 naphthalenes Chemical class 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 229920000768 polyamine Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 238000012797 qualification Methods 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000002829 reductive effect Effects 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 125000005063 tetradecenyl group Chemical group C(=CCCCCCCCCCCCC)* 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C57/00—Unsaturated compounds having carboxyl groups bound to acyclic carbon atoms
- C07C57/02—Unsaturated compounds having carboxyl groups bound to acyclic carbon atoms with only carbon-to-carbon double bonds as unsaturation
- C07C57/13—Dicarboxylic acids
-
- 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
-
- 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
- C10L1/198—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
Definitions
- This invention relates to deposit modifiers for substantially hydrocarbon fuels. More specifically, this invention relates to substantially hydrocarbon fuels containing deposit modifiers which inhibit and/or prevent the deposit-forming tendency of hydrocarbon fuels during combustion, and/ or modify the deterious effect of the formed deposits, in both leaded and unleaded fuels, particularly in gasoline, jet fuels, etc., and to the process of inhibiting and/or preventing and/r modifying the formation deposits inengines employing hydrocarbon fuels.
- the smooth operation of an internal combustion engine depends on the gradual propagation of the flame toward the cylinder walls and the fuel-air mixture is ignited at many spots at the same time, progressive combustion is interrupted; If several compressive waves are created, they subject the unburned charge to unduly high pressure and temperature so as to produce engine knock. This generally occurs if the cylinder deposits, which contain carbonaceous materials and lead compounds, retain sufficient heat to ignite the fuel-air mixture before the flame which had been originated by the spark plugs reaches all parts of the combustion chamber. Deposited lead compounds are believed to lower the temperature at which the deposits glow and ignite the fuel and it is desirable to reduce the deposits and/or neutralize the catalytic effect of such deposits in igniting the fuel. By so doing, these additives lower the octane number required to prevent knock or surface ignition.
- octane requirement the octane requirement
- the weight of material deposited upon the top or head of the piston reaches a maximum in a single cylinder engine after approximately 20 hours of operation and that thereafter it decreases slightly, possibly due to a flaking action, until it levels 011? after about 40 hours of operation. It has also been found that the weight of the material deposited upon the exhaust valves reaches a maximum in the same engine after about 30 hours of operation and thereafter it decreases slightly and levels off after about 40 hours of operation.
- the octane requirement increase of an engine is not determined solely by the quantity of material deposited in the combustion zone and that it is not due to a decrease in the thermal conductivity of the surfaces enclosing said zone, it is believed that it is due to a catalytic action wherein the deposits in the combustion zone act as catalysts to accelerate the oxidation of petroleum hydrocarbons. It has, therefore, been suggested that the proper approach to the problem of reducing the octane demand increase of an engine is that of adding to the fuel asubstance having an anti-catalytic effect, or, in other words, the elfect of suppressing or, inhibiting the catalytic properties of the deposits formed, especially the troublesome lead-containing deposits.
- anti-knock agents have been provided with corrective agents commonly known as scavengers, which eflectively reduce the amount of metallic deposits in the engine by forming volatile metallic compounds which emanate from the engine in the exhaust gas stream the accumulation of engine deposits in combustion chambers and on other engine parts such as pistons, valves, and the like cannot -be entirely prevented.
- This accumulation of deposits is particularly prevalent when the vehicles are operated under conditions of low speed and high load as encountered in metropolitan localities.
- fuel anti-knock quality which have been made in recent years, such deposits present but a few minor problems in low compression engines, whereas with engines of higher compression ratios two more serious problems are becoming increasingly prevalent, those of detonation and deposit-induced autoignition or wild ping.
- Ordinary detonation in the internal combustion engine has been defined as the spontaneous combustion of an appreciable portion of the charge, which results in an extremely rapid local pressure rise and produces a sharp metallic knock.
- the control of ordinary detonation may be effected by retarding ignition timing, by operating under part throttle conditions, by reducing the compression ratio of the engine, and by using'fuels having high anti-knock qualities, that is, by using an organolead-containing fuel.
- Deposit-induced autoignition may be defined as the erratic ignition of the combustible charge by combustion chamber deposits resulting in uncontrolled combustion and isolated bursts of audible and inaudible manifestations of combustion, somewhat similar to knocking.
- hydrocarbon fuels of this invention are characterized by low deposit-forming tendencies with the result that an engine operated therewith shows exceptionally clean intake system combustion space, valves, ring belt area, cleaner spark plugs, etc.
- the low deposit level in the engine, spark plugs, etc. minimizes surface ignition in all its manifestations, for example preignition, knock, wild ping, spark plug fouling, etc.
- the low deposit level reduces the surfaces contacted by the lubricating oil, such as piston engines octane requirement increase, and deposits on skirts and cylinder walls, are very markedly reduced.
- these compounds have an anti-catalytic effect, or, in other words, have the effect of suppressing or inhibiting the catalytic properties of the deposits found, especially the troublesome lead-containing deposits. Furthermore, these compounds are also effective corrosion inhibitors.
- compositions of this invention are alkenyl succinic anhydrides (ASA) or the equivalent such as alkenyl succinic acid salts thereof, and the like.
- ASA alkenyl succinic anhydrides
- Substantially any ASA or its equivalent may be employed provided it is sutficiently soluble in the fuel to be effective as a deposit modifier.
- R is an alkenyl radical.
- the alkenyl radical can be straight-chain or branched-chain; and it can be saturated at the point of unsaturation by the addition of a substance which adds to olefinic double bonds, such as hydrogen, sulfur, bromine, chlorine, or iodine. It is obvious, of course, that there must be at least two carbon atoms in the alkenyl radical, but there is no real upper limit to the number of carbon atoms therein. However, it is preferred to use an alkenyl succinic acid anhydride reactant having between about 8 and about 18 car-bon atoms per alkenyl radical.
- alkenyl succinic acid anhydride when used herein, it must be clearly understood that it embraces the alkenyl succinic acids as Well as their anhydrides, and the derivatives thereof in which the olefinic double bond has been saturated as set forth hereinbefore. Thus, it includes the hydrogenated alkenyl group, i.e. alkyl succinic acids and anhydride.
- Salts of the above compounds in the acid state can be employed, for example, ammonium salts, amine salts, and in certain instances small amounts of inorganic ion salts although the latter is not as satisfactory as amine or ammonium salts since they tend to leave a residue 011 combustion.
- alkenyl succinic acid anhydrides are well known to those familiar with the art. The most feasible method is by the reaction of an olefin with maleic acid anhydride. Since relatively pure olefins aredifiicult to obtain, and when thus obtainable, are often too expensive for commercial use, alkenyl succinic acid anhydrides are usually prepared as mixtures by reacting mixtures of olefins with maleic acid anhydride. Such mixtures, as well as relatively pure anhydrides, are utilizable herein.
- deposit-preventing, inhibiting and/ or modifying amounts of the compounds are employed.
- the products of this invention are effective as a deposit-control additive in concentrations between 0.001 and 2.0 weight percent of the fuel.
- dirtier fuels having a higher concentration of olefinic components require higher concentrations whereas cleaner burning premium fuels are improved with respect to deposit- 'forming characteristics by smaller concentrations.
- dirtierf gasolines require a concentration between 0.01 and 1.0 percent whereas clean-burning premium fuels only need a concentration of between 0.001 and 0.5 percent.
- concentration be less than .1 percent.
- the compounds in this invention are effective in controlling deposits in hydrocarbon fuels having boiling points up to about 500 F. or higher, although benefits also result when they are added-to fuels containing residual stocks of higher boiling point.
- the major application of the additive is in gasoline for automotive engines wherein fuel-derived engine deposits have become a particularly vexing problem.
- the deposit-forming propertics of fuels designed for use in jets are also improved by the compounds of this invention. They find particular application in jet fuels which are used as cooling mediums prior to their consumption.
- the compoundcontaining jet fuel is an excellent'heat exchange medium since it is relatively free from deposits in the cooling system and burner nozzle where deposits cannot be tolerated.
- the deposit-forming properties of both regular and premium gasolines and aviation gasoline, whether leaded and of the non-leaded type, are improved by the addition of these compounds.
- the gasolines to which they are added can be broadly defined as a hydrocarbon fuel having a boiling point up to approximately 450 F.
- ASAs and corresponding acids are suitable in the process of this invention.
- the acids are prepared from hydrolysing the ASA.
- TEST I Performance tests show that the present invention produces substantial improvement in engine cleanliness, as compared to the same fuel not containing the additive.
- the test procedure involves a 40 hour engine run on a dynamometer under conditions chosen to correlate, on an accelerated scale, with field performance.
- a 216.5 cubic-inch, six-cylinder Chevrolet engine is run continuously for forty hours at a speed of 1900 r.p.m. (plus or minus 25 r.p.m.) under an engine load of 36 B.H.P. (plus or minus 1 B.H.P.)
- the air-fuel ratio is 14.5 (plus or minus 0.5) to 1.
- the spark advance is 35 (plus or minus 3).
- the spark plug gap, ignition cam angle, valve clearance, exhaust back pressure and other similar conditions are also maintained at predetermined values.
- Corrosion or rust rating (10 for none, 9 for light, 8 for medium, and 7 for heavy corrosion).
- a perfectly clean engine will thus rate 100.
- a total rating of 85 is considered acceptable if the piston skirt varnish is 7.5 or better.
- the gasoline employed in the tests is composed of about 50% mixed thermal naphtha having about 95 400 F. boiling range, about 20% light straight-run naphtha having 95 -250 F. boiling range, about 25% heavy cracked (catalytic) naphtha having 270-400 F. boiling range, and about of light natural gasoline. It contains as additives about 1.75 ml. per gallon of tetraethyllead and an amine inhibitor in normal amounts. It analyzes 0.11% sulfur. Gum is present at about 2 to 5 mg. per 100 ml. in the ASTM test and the copper dish test shows about 16-26 mg. of gum per 100 ml.
- the gasoline has the following volatility specifications: evaporated at l34-l50 F., 50% at 244250 F., and 90% at about 360 F.
- the approximate composition of the gasoline is:
- An example of a high quality premium grade fuel with which similar results are obtained comprises mainly fluid catalytically cracked stock and straight run gasoline.
- This fuel has a 95 A.S.T.M. research octane rating, contains 2.74 mi. of TEL fluid per gallon, had an API gravity of 60 to 65 and a boiling point range between 100 and 400 F.; the base fuel is negative in the copper corrosion test and has :an oxidation stability in the ASTM test of 240 minutes minimum.
- This fuel also contains minor amounts of conventional gasoline inhibitors, namely, approximately 6 pounds of N,N'-disecondary butyl-pphenylenediamine, a gum inhibitor, per thousand barrels of gasoline, about 1.2 pounds of N,N'-disalicylidene-1,2- diamino-propane, a metal deactivator, per thousand barrels of gasoline, and about 1.1 pounds of lecithin, a tetraethyl lead stabilizer, per thousand barrels of gasoline.
- conventional gasoline inhibitors namely, approximately 6 pounds of N,N'-disecondary butyl-pphenylenediamine, a gum inhibitor, per thousand barrels of gasoline, about 1.2 pounds of N,N'-disalicylidene-1,2- diamino-propane, a metal deactivator, per thousand barrels of gasoline, and about 1.1 pounds of lecithin, a tetraethyl lead stabilizer, per thousand barrels of gasoline.
- This regular base fuel has an 87.0 ASTM Research octane rating, contained 2.90 ml. of TEL per gallon, has an API gravity of 58.0 and a boiling range between 100" F. and 450 F.; the base fuel is negative in the copper corrosion test and has an oxidation stability in the ASTM test of 530 minutes minimum.
- the reference fuel also contains minor amounts of gasoline inhibitors, namely N,N'-disecondary butyl-p-pheny1enediarnine, lecithin, and N,N'-disalicylidene-1,2-diaminopropane.
- compositions are also similarly effective when tested in an aviation grade gasoline as exemplified by 115/130 grade aviation gasoline containing 4.6 ml. of tetraethyl lead.
- the motor fuels employed in this invention comprise '8 a mixture of hydrocarbons boiling in the gasoline boil? ing range.
- the gasoline employed can be a straight-run gasoline or a gasoline obtained from a conventional. cracking process, or mixtures thereof.
- the gasoline can also include components obtained from processes other than cracking such as alkylation, isomerization, hydrogenation, polymerization, hydro-desulfurization, hydroforming, platforming or combinations thereof, as well as synthetic gasoline obtained from the Fischer- Tropsch and related processes.
- Test 11 SPARK PLUG FOULING A production model .1956 Oldsmobile Super 88 engine is used to accomplish the evaluation.
- the engine is connected directly to a power absorption dynamometer through a conventional multiple disc coupling.
- the dynamometer and engine are fully instrumented to control operating conditions and to indicate data which are recorded hourly throughout the test.
- Preparation of the engine for the test includes a thorough cleaning, inspection and measurement of all components.
- the engine is assembled according to the manufacturers specifications. After subjecting the engine to an eight hour break-in a thirty two hour oil consumption check follows. During this check a speed of 2000 r.p.m. and 50 B.H.P. is maintained. At eight hour intervals the oil is drained and weighed. Having established oil consumption stability the cylinder compression pressures were measured to indicate valve condition. . The cylinder heads are removed and all combustion chamber deposits eliminated.
- the cylinder heads are assembled to the engine and preselected test spark plugs are installed for the first time.
- the engine starts on test schedule with an electromechanical intermittent controller attached to the throttle and dynamorneter control which timed and actuated the throttle opening and dynamometer assistance for engine speed and load change. These changes are 2000 r.p.m. at 37.5 B.H.P. for five minutes and 450 r.p.m. at idle for one minute. Fifty of these cycles or five hours comprise one interval. At the completion of each interval a check is made for misfiring at 2400 r.p.m. at full load. If no misfiring is observed, the test continued for another interval of five hours. In the event of misfiring it is determined whether one or more spark plugs are failing.
- a criterion for test termination is three fouled plugs in three difierent cylinders. If less than three plugs fouled simultaneously the fouled plug or plugs are replaced with a new plug and the test continued until a total of three plugs fouled in three different cylinders. The reasons for replacing the fouled plugs with new plugs before continuing the test are:
- the fuel treated with the additive is blended as follows:
- a 4000 gallon capacity storage tank is flushed with the base fuel. 1200 gallons of base fuel are pumped into the tank. A circulating pump is placed in operation with the intake at one end of the tank and the delivery at the opposite end of the required amount of additive is mixed with five gallons of the base gasoline. This mixture is slowly fed into the delivery stream of the fuel from the circulating pump. The fuel blend is recirculated for sixteenhours before start of the test.
- the spark plugs selected for the test are AC-43. This spark plug is one degree colder in the heat range than the engine manufacturer recommends for this model. Twenty-four plugs are inspected and pre-tested under air pressure for firing for each test phase. From each batch of 24 plugs eight are selected which were nearly uniform in resistance at maximum pressure. All electrode gaps are adjusted to .040".
- the air-fuel ratio was determined by a Cambridge Exhaust Gas Tester.
- Jacket coolant in Jacket coolant out Intake air at carburetor Motor oil in oil pan sump Wet bulb Dry bulb Exhaust back pressures and intake manifold vacuum are measured by means of mercury manometers. Barometric pressure is observed on a convention mercury barometer and was corrected for temperature. Engine oil pressure is measured by a standard Bourdon-type gage.
- the rate of fuel consumption is determined on a weight basis using a tip balance.
- a flowmeter in the supply line provides a check upon engine fuel consumption determined by weighing.
- Engine speed is determined by an electronic counter.
- Spark plug performance characteristics are observed by means of a multiple trace oscilloscope.
- the base fuel used for the test operations is described as follows:
- spark plug fouling is a function of the lead content of the gasoline, the optimum amount will vary with such content.
- weight ratios of 0.00l2% or more can be employed in gasolines containing about 3 cc. of tetraethylene lead or its equivalent/ gallon of gasoline, generally 0.0011% is usually sufficient for anti-fouling purposes.
- the optimum amount or the weight bases for one particular compound may not be the optimum amount for another compound.
- the effectiveness of the compounds vary from one compound to another.
- Another reason is the variance of molecular weights so that one compound may be twice the molecular weight of another.
- anti-fouling can be effected.
- Test III These compounds in the above table are also tested in a hour full scale reciprocity engine test employing Military Specification MIL-G-5572A grade /145 fuel in a Wright R 3350-30W compound engine operated according to the following cycle:
- the invention includes various fuels such as all grades of gasolines which may contain a wide variety of additives such as antioxidants, organolead stabilizers, organic dyes, solubilizers, etc., as Well as the halide scavengers generally employed such as ethylene dibromide and/ or ethylene dichloride and other scavengers. for example those disclosed in the patents listed above relating to such compositions. Such variations and modifications one considered to be within the purview and scope of the appended claims.
- a process offpreve'nting, inhibiting and modifying the formation of deposits in internal combustion and jet engines employing a substantially hydrocarbon fuel whichrcomprises burning in such engines a fuel consisting of a liquid hydrocarbon having a boiling point up to about 500 F. and a minor amount in the range of approximately 0.001 to 2% -by weight of the fuel, sufficient to prevent, inhibit and modify such deposits, of a member selected from the group consisting of an oil soluble alkenyl succinic acid and the anhydride thereof, having 8 to 31 carbon atoms on the alkenyl group.
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Description
United States Patent C 2,993,772 ACID ADDITIVES Verner L. Stromberg, Webster Groves, Mo., assignmto Petrolite Corporation, Wilmington, Del., a corporation of Delaware No Drawing. Filed Feb. 2, 1959, Ser. No. 790,352 6 Claims. (Cl.52.5)
This invention relates to deposit modifiers for substantially hydrocarbon fuels. More specifically, this invention relates to substantially hydrocarbon fuels containing deposit modifiers which inhibit and/or prevent the deposit-forming tendency of hydrocarbon fuels during combustion, and/ or modify the deterious effect of the formed deposits, in both leaded and unleaded fuels, particularly in gasoline, jet fuels, etc., and to the process of inhibiting and/or preventing and/r modifying the formation deposits inengines employing hydrocarbon fuels.
The smooth operation of an internal combustion engine depends on the gradual propagation of the flame toward the cylinder walls and the fuel-air mixture is ignited at many spots at the same time, progressive combustion is interrupted; If several compressive waves are created, they subject the unburned charge to unduly high pressure and temperature so as to produce engine knock. This generally occurs if the cylinder deposits, which contain carbonaceous materials and lead compounds, retain sufficient heat to ignite the fuel-air mixture before the flame which had been originated by the spark plugs reaches all parts of the combustion chamber. Deposited lead compounds are believed to lower the temperature at which the deposits glow and ignite the fuel and it is desirable to reduce the deposits and/or neutralize the catalytic effect of such deposits in igniting the fuel. By so doing, these additives lower the octane number required to prevent knock or surface ignition.
As automobile manufacturers annually raise the compression ratio of their automobile engines in the race for higher horsepower, the need becomes greater for gasolines which burn cleanly, that is, have low deposit-forming tendencies. Engine deposits which find their origin in the fuel are primarily responsible for surface ignition phenomena such as preignition and octane requirement increase (ORI) which is the tendency of spark ignition engines in service to require higher octane fuels for proper performance. As a consequence, gasoline manufacturers have placed increasing stress on reducing the depositforming tendencies of their fuels and have resorted to various additives either to reduce the amount of deposits or to minimize their effects.
The deposits formed in the combustion zone, particularly on the piston head and the exhaust valves, appear to have the most immediate effects upon engine performance in that their presence requires a fuel having a higher octane rating in order not to knock, than is required by a new or clean engine. This means, in other words, that the octane value of a fuel required by an engine containing deposits in the combustion zone in order not to knock (referred to hereinafter as octane requirement) is higher than the octane requirement of a clean engine. For example, a clean engine. which requires a gasoline having an octane rating of 60in order not to knock is said to have an octane requirement of 60. If the same engine, when dirty, i.e., with deposits in the combustion chamber, requires a gasoline having an octane rating of 75 in order not to knock, such an engine is said to have an octane requirement of 75, or an octane requirement increase of 15. If a clean engine starts to get dirty, the octane requirement rises with continued use. Finally there is no more octane requirement increase with continued use and apparently the engine has then become Patented July 25, 1961 as dirty as it is ever going to be with continued use, or if it becomes dirtier after a certain point, it does not require a gasoline of greater octane value in order not to knock.
It has been found, for example, that the weight of material deposited upon the top or head of the piston reaches a maximum in a single cylinder engine after approximately 20 hours of operation and that thereafter it decreases slightly, possibly due to a flaking action, until it levels 011? after about 40 hours of operation. It has also been found that the weight of the material deposited upon the exhaust valves reaches a maximum in the same engine after about 30 hours of operation and thereafter it decreases slightly and levels off after about 40 hours of operation. The fact that the weight of deposits in the combustion zone first reachm a maximum value and then levels Off to a somewhat lower value while the octane requirement levels off at the maximum value is believed to disprove the formerly accepted theory that the octane requirement of an engine in proportional to the weight of deposits in the combustion chamber.
The undesirable effects of the deposits in the combustion chamber are further aggravated when tetraethyl lead is contained in the fuel because these deposits then are no longer primarily carbonaceous but contain appreciable quantitiesof lead. Accordingly, it has been found that the total weight of deposits formed in the combustion zone is appreciably greater when using a leaded fuel than when using a non-leaded fuel. The octane requirement increase of an engine operating on leaded fuel, however, is not in proportion to the difference in deposit weights. From this it is concluded that the octane requirement increase of an engine is determined not so much byithe quantity of material deposited as by its presence and character.
It has also previously been found that the increase in octane requirement resulting from the formation of engine deposits is not attributable to a decrease in the. thermal conductivity of the surfaces enclosing the combustion zone.
Since it has been found that the octane requirement increase of an engine is not determined solely by the quantity of material deposited in the combustion zone and that it is not due to a decrease in the thermal conductivity of the surfaces enclosing said zone, it is believed that it is due to a catalytic action wherein the deposits in the combustion zone act as catalysts to accelerate the oxidation of petroleum hydrocarbons. It has, therefore, been suggested that the proper approach to the problem of reducing the octane demand increase of an engine is that of adding to the fuel asubstance having an anti-catalytic effect, or, in other words, the elfect of suppressing or, inhibiting the catalytic properties of the deposits formed, especially the troublesome lead-containing deposits.
The use of lead compounds in gasolines to increase the octane ratings thereof is extremely widespread. There are, however, several rather serious adverse effects which accompany the use of leaded gasolines. One of these effects, the deposition of various lead compounds within the combustion chambers of the engines, has been at least partially remedied by the use of halohydrocarbon'scavengers such as ethylene dibromide and related compounds for example those disclosed in US. Patents 2,398,281, 2,490,606, 2,479,900, 2,479,902, 2,479,901, 2,479,903, etc' Another adverse effect, which has been attributed to the lead anti-knock compounds, is mis-firing due to spark plug fouling. This spark plug fouling is quite prevalent under conditions of high temperature engine operation and, particularly in the case of aircraft engines is a very serious type of trouble.
As stated above, there has been a marked trend in recent years in the automotive industry toward utilizing in- 3 ternal combustion engines having high compression ratios in passenger cars and trucks. It has been found that this increase in compression ratios results in increased engine efficiency whereby the motoring public is provided with both greater power availability and greater economy of operation. High compression engines almost uniformly require fuels of high octane number for most efficient operation. Of the several methods of raising the octane number of gasoline developed to date, that of utilizing an anti-knock agent, particularly of the organolead type, has been most successful. Although such anti-knock agents have been provided with corrective agents commonly known as scavengers, which eflectively reduce the amount of metallic deposits in the engine by forming volatile metallic compounds which emanate from the engine in the exhaust gas stream the accumulation of engine deposits in combustion chambers and on other engine parts such as pistons, valves, and the like cannot -be entirely prevented. This accumulation of deposits is particularly prevalent when the vehicles are operated under conditions of low speed and high load as encountered in metropolitan localities. As a result of the notable improvements in fuel anti-knock quality, which have been made in recent years, such deposits present but a few minor problems in low compression engines, whereas with engines of higher compression ratios two more serious problems are becoming increasingly prevalent, those of detonation and deposit-induced autoignition or wild ping. Although detonation can successfully be obviated by the utilization of organolead anti-knock agents such as tetraethyllead, it has been found that the severity of the wild ping problem often increases with the octane quality of the fuel. Hence, the automotive industry is faced with the dilemma resulting from the fact that each time the octane quality of the fuel is raised to coincide with increases in compression ratio, deposit-induced autoignition generally becomes more severe.
Ordinary detonation in the internal combustion engine has been defined as the spontaneous combustion of an appreciable portion of the charge, which results in an extremely rapid local pressure rise and produces a sharp metallic knock. The control of ordinary detonation may be effected by retarding ignition timing, by operating under part throttle conditions, by reducing the compression ratio of the engine, and by using'fuels having high anti-knock qualities, that is, by using an organolead-containing fuel. Deposit-induced autoignition may be defined as the erratic ignition of the combustible charge by combustion chamber deposits resulting in uncontrolled combustion and isolated bursts of audible and inaudible manifestations of combustion, somewhat similar to knocking. Aside from the nuisance experienced by the passenger car operator, deposit-induced autoignition or wild ping often produces deleterious effects inasmuch as it is a precurser of preignition. Therefore, wild ping results in rough engine operating conditions and very often increases the wear of engine parts, piston burning and the like. In contrast to ordinary detonation, deposit-induced autoignition or wild ping cannot be satisfactorily controlled by retarding ignition timing nor by operating under part throttle conditions. Inasmuch as automotive engineers are desirous of utilizing in internal combustion engines the highest compression ratios permitted by the commercially available fuels, the reduction of compression ratios to eliminate this problem is not desirable nor feasible. Indeed, it is the consensus of opinion among the designers of internal combustion engines that engine developments have heretofore been greatly hindered by the limitations imposed by deposit-induced autoignition. It is evident, therefore, that the present requirement for fuel having high anti-knock qualities shall be greatly surpassed by future requirements. Notwithstanding attempts to attain these qualities by alternative means, it is entirely probable that the most satisfactory method for the attain- .ment of high octane fuels shall continue to be the use w 4 of anti-knock agents, particularly of the organolead type. As a result, there is a paramount need existing for a new and improved method for altering the physical and chemical characteristics of deposits and for modifying the combustion process such that the detrimental effects of deposit-induced autoignition may be markedly suppressed or be eliminated.
I have now found that a particular class of compounds effectively controls (by inhibiting and/ or preventing and/or modifying) the deposit-forming tendencies of substantially hydrocarbon fuels, for example gasoline jet fuels and the like, with resulting advantages. The hydrocarbon fuels of this invention are characterized by low deposit-forming tendencies with the result that an engine operated therewith shows exceptionally clean intake system combustion space, valves, ring belt area, cleaner spark plugs, etc. The low deposit level in the engine, spark plugs, etc., minimizes surface ignition in all its manifestations, for example preignition, knock, wild ping, spark plug fouling, etc. The low deposit level reduces the surfaces contacted by the lubricating oil, such as piston engines octane requirement increase, and deposits on skirts and cylinder walls, are very markedly reduced.
In addition, these compounds have an anti-catalytic effect, or, in other words, have the effect of suppressing or inhibiting the catalytic properties of the deposits found, especially the troublesome lead-containing deposits. Furthermore, these compounds are also effective corrosion inhibitors.
The compositions of this invention are alkenyl succinic anhydrides (ASA) or the equivalent such as alkenyl succinic acid salts thereof, and the like. Substantially any ASA or its equivalent may be employed provided it is sutficiently soluble in the fuel to be effective as a deposit modifier.
The general structural formulae of these compounds are:
Anhydride Acid wherein R is an alkenyl radical. The alkenyl radical can be straight-chain or branched-chain; and it can be saturated at the point of unsaturation by the addition of a substance which adds to olefinic double bonds, such as hydrogen, sulfur, bromine, chlorine, or iodine. It is obvious, of course, that there must be at least two carbon atoms in the alkenyl radical, but there is no real upper limit to the number of carbon atoms therein. However, it is preferred to use an alkenyl succinic acid anhydride reactant having between about 8 and about 18 car-bon atoms per alkenyl radical.
Accordingly, when the term alkenyl succinic acid anhydride, is used herein, it must be clearly understood that it embraces the alkenyl succinic acids as Well as their anhydrides, and the derivatives thereof in which the olefinic double bond has been saturated as set forth hereinbefore. Thus, it includes the hydrogenated alkenyl group, i.e. alkyl succinic acids and anhydride. Nonlimiting examples of the alkenyl succinic acid anhydride are ethenyl succinic acid anhydrides; ethenyl succinic acid; ethyl succinic acid anhydride; propenyl succinic acid anhydride; sulfurized propenyl succinic acid anhydride; butenyl succinic acid; Z-methyl-butenyl succinic acid anhydride; l,2-dichloropenty1 succinic acid anhydride; hexenyl succinic acid anhydride; hexyl succinic acid; sulfurized :3-methylpentenyl succinic acid anhydride; 2,'3-dimethyl-butenyl succinic acid anhydride; 3,3-dimethylbutenyl succinic acid; =1,2-dibromo-2-ethylbutyl succinic acid; heptenyl succinic acid anhydride; 1,2-diiodooctyl succinic acid; octenyl succinic acid anhydride; 2-methylheptenyl succinic acid anhydride; 4-ethylhexenyl succinic acid; 2-isopropylpentenyl succinic acid anhydride; nonenyl succinic acid anhydride; 2-propylhexenyl succinic acid anhydride; decenyl succinic acid; decenyl succinic acid anhydride; 5-methy1-2-isopropylhexenyl succinic acid anhydride; 1,Z-dibromo-Z-ethyloctenyl succinic acid anhydride; decyl succinic acid anhydride; undecenyl succinic acid anhydride; 1,?2-dichloro-undecyl succinic acid; 3-ethyl-2-t-butylpentenyl succinic acid anhydride; dodecenyl succinic acid anhydride; dodecenyl succinic acid; .2-propylnonenyl succinic acid anhydride; 3-butyloctenyl succinic acid anhydride; tridecenyl succinic acid anhydride; tetradecenyl succinic acid anhydride; hexadecenyl succinic acid anhydride; sulfurized octadecenyl succinic acid; octadecyl succinic acid anhydride; 1,2-dibromo-2-methylpentadecenyl succinic acid anhydride; B-propylpentadecyl succinic acid anhydride; eicosenyl succinic acid anhydride; '1,2-dichloro-2-methylnonadecenyl succinic acid anhydride; Z-octyI-dodecenyl succinic acid; 1,2-diiodotetracosenyl succinic acid anhydride; hexacosenyl succinic acid; hexacosenyl succinic acid anhydride; and hentriacontenyl succinic acid anhydride, as well as the corresponding acids and anhydn'des of the above compounds. Salts of the above compounds in the acid state can be employed, for example, ammonium salts, amine salts, and in certain instances small amounts of inorganic ion salts although the latter is not as satisfactory as amine or ammonium salts since they tend to leave a residue 011 combustion.
The methods of preparing the alkenyl succinic acid anhydrides are well known to those familiar with the art. The most feasible method is by the reaction of an olefin with maleic acid anhydride. Since relatively pure olefins aredifiicult to obtain, and when thus obtainable, are often too expensive for commercial use, alkenyl succinic acid anhydrides are usually prepared as mixtures by reacting mixtures of olefins with maleic acid anhydride. Such mixtures, as well as relatively pure anhydrides, are utilizable herein.
In general, deposit-preventing, inhibiting and/ or modifying amounts of the compounds are employed. For example, the products of this invention are effective as a deposit-control additive in concentrations between 0.001 and 2.0 weight percent of the fuel. Generally, dirtier fuels having a higher concentration of olefinic components require higher concentrations whereas cleaner burning premium fuels are improved with respect to deposit- 'forming characteristics by smaller concentrations. In general, dirtierf gasolines require a concentration between 0.01 and 1.0 percent whereas clean-burning premium fuels only need a concentration of between 0.001 and 0.5 percent. There is no critical upper limit from a functional viewpoint but economics dictate that the concentration be less than .1 percent.
The compounds in this invention are effective in controlling deposits in hydrocarbon fuels having boiling points up to about 500 F. or higher, although benefits also result when they are added-to fuels containing residual stocks of higher boiling point. The major application of the additive is in gasoline for automotive engines wherein fuel-derived engine deposits have become a particularly vexing problem. The deposit-forming propertics of fuels designed for use in jets are also improved by the compounds of this invention. They find particular application in jet fuels which are used as cooling mediums prior to their consumption. The compoundcontaining jet fuel is an excellent'heat exchange medium since it is relatively free from deposits in the cooling system and burner nozzle where deposits cannot be tolerated.
The deposit-forming properties of both regular and premium gasolines and aviation gasoline, whether leaded and of the non-leaded type, are improved by the addition of these compounds. The gasolines to which they are added can be broadly defined as a hydrocarbon fuel having a boiling point up to approximately 450 F.
Representative compounds for the above classes are incorporated, for example, in fuels used in automobile,
aircraft, and jet engines. Laboratory tests are carried out employing these fuels in such systems.
The following examples of ASAs and corresponding acids are suitable in the process of this invention. The acids are prepared from hydrolysing the ASA.
TABLE I Example Alkeuyl Group Molecular Form anhydride. acid.
anhydride.
o acid Octeglyl (branched)-.-
Decgnyl (straight chain) anhydride.
. acid.
anhydride. acid.
. anlaydride.
o Tetradecenyl (straight chain) Heptadecenyl (straight chain) o octaidecenyl (straight chain). o
.. acl
anhydride.
acid.
anhydride.
anhydride. acid.
anhydride. acid.
anhydridc.
acid.
anhydride.
acid.
TEST I Performance tests show that the present invention produces substantial improvement in engine cleanliness, as compared to the same fuel not containing the additive. The test procedure involves a 40 hour engine run on a dynamometer under conditions chosen to correlate, on an accelerated scale, with field performance. In this test a 216.5 cubic-inch, six-cylinder Chevrolet engine is run continuously for forty hours at a speed of 1900 r.p.m. (plus or minus 25 r.p.m.) under an engine load of 36 B.H.P. (plus or minus 1 B.H.P.) The jacket coolant inlet temperature is kept at F. minimum, the jacket coolant outlet temperature is kept within two degrees of =F., and the crankcase oil temperature is kept within two degrees of F. The air-fuel ratio is 14.5 (plus or minus 0.5) to 1. The spark advance is 35 (plus or minus 3). The spark plug gap, ignition cam angle, valve clearance, exhaust back pressure and other similar conditions are also maintained at predetermined values. Before the test, the engine is disassembled and cleaned, and a new set of piston rings is installed. The engine is given a standard twohour break-in before the actual test is begun.
After the test run of 40 hours, the engine is dismantled and inspected, and is rated on ten items, as follows:
(1) Piston skirt varnish rat-ing. (2) Cylinder wall varnish rating.
(3) Intake valve stem deposit rating.
'(4) Intake valve tulip deposit rating.
(5) Intake port deposit rating.
(6) Overall engine sludge rating.
(7) Overall engine varnish rating.
On these first seven items, the rating runs between for dirty to 10 for clean.
(8) Corrosion or rust rating (10 for none, 9 for light, 8 for medium, and 7 for heavy corrosion).
(9) Stuck ring rating (10, minus 0.5 demerit for each 90 of ring stuck in the groove).
(10) Ti-ght ring rating (10, minus 0.5 demerit for each tight ring).
A perfectly clean engine will thus rate 100. A total rating of 85 is considered acceptable if the piston skirt varnish is 7.5 or better.
The gasoline employed in the tests is composed of about 50% mixed thermal naphtha having about 95 400 F. boiling range, about 20% light straight-run naphtha having 95 -250 F. boiling range, about 25% heavy cracked (catalytic) naphtha having 270-400 F. boiling range, and about of light natural gasoline. It contains as additives about 1.75 ml. per gallon of tetraethyllead and an amine inhibitor in normal amounts. It analyzes 0.11% sulfur. Gum is present at about 2 to 5 mg. per 100 ml. in the ASTM test and the copper dish test shows about 16-26 mg. of gum per 100 ml. The gasoline has the following volatility specifications: evaporated at l34-l50 F., 50% at 244250 F., and 90% at about 360 F. The approximate composition of the gasoline is:
Percent Parafiins and naphthalenes About 66 Olefins About 16 Aromatics About 18 Sulfur About 0.1 Phenols -About- 0.4 Nitrogen .About 0.001
The alkenyl succinic anhydrides and the corresponding acids shown in the above table when tested in concentrations of 0001-05 weight percent gave cleaner engines and therefore higher ratings than the control containing no additives.
An example of a high quality premium grade fuel with which similar results are obtained comprises mainly fluid catalytically cracked stock and straight run gasoline. This fuel has a 95 A.S.T.M. research octane rating, contains 2.74 mi. of TEL fluid per gallon, had an API gravity of 60 to 65 and a boiling point range between 100 and 400 F.; the base fuel is negative in the copper corrosion test and has :an oxidation stability in the ASTM test of 240 minutes minimum. This fuel also contains minor amounts of conventional gasoline inhibitors, namely, approximately 6 pounds of N,N'-disecondary butyl-pphenylenediamine, a gum inhibitor, per thousand barrels of gasoline, about 1.2 pounds of N,N'-disalicylidene-1,2- diamino-propane, a metal deactivator, per thousand barrels of gasoline, and about 1.1 pounds of lecithin, a tetraethyl lead stabilizer, per thousand barrels of gasoline.
Similar results are obtained with a high quality regular grade gasoline comprising a mixture of thermal cracked stock, fluid catalytically cracked stock and straight run gasoline. This regular base fuel has an 87.0 ASTM Research octane rating, contained 2.90 ml. of TEL per gallon, has an API gravity of 58.0 and a boiling range between 100" F. and 450 F.; the base fuel is negative in the copper corrosion test and has an oxidation stability in the ASTM test of 530 minutes minimum. The reference fuel also contains minor amounts of gasoline inhibitors, namely N,N'-disecondary butyl-p-pheny1enediarnine, lecithin, and N,N'-disalicylidene-1,2-diaminopropane.
These compositions are also similarly effective when tested in an aviation grade gasoline as exemplified by 115/130 grade aviation gasoline containing 4.6 ml. of tetraethyl lead.
The motor fuels employed in this invention comprise '8 a mixture of hydrocarbons boiling in the gasoline boil? ing range. For instance, the gasoline employed can be a straight-run gasoline or a gasoline obtained from a conventional. cracking process, or mixtures thereof. The gasoline can also include components obtained from processes other than cracking such as alkylation, isomerization, hydrogenation, polymerization, hydro-desulfurization, hydroforming, platforming or combinations thereof, as well as synthetic gasoline obtained from the Fischer- Tropsch and related processes.
Test 11 SPARK PLUG FOULING A production model .1956 Oldsmobile Super 88 engine is used to accomplish the evaluation. The engine is connected directly to a power absorption dynamometer through a conventional multiple disc coupling. The dynamometer and engine are fully instrumented to control operating conditions and to indicate data which are recorded hourly throughout the test.
Preparation of the engine for the test includes a thorough cleaning, inspection and measurement of all components. The engine is assembled according to the manufacturers specifications. After subjecting the engine to an eight hour break-in a thirty two hour oil consumption check follows. During this check a speed of 2000 r.p.m. and 50 B.H.P. is maintained. At eight hour intervals the oil is drained and weighed. Having established oil consumption stability the cylinder compression pressures were measured to indicate valve condition. .The cylinder heads are removed and all combustion chamber deposits eliminated.
The cylinder heads are assembled to the engine and preselected test spark plugs are installed for the first time. The engine starts on test schedule with an electromechanical intermittent controller attached to the throttle and dynamorneter control which timed and actuated the throttle opening and dynamometer assistance for engine speed and load change. These changes are 2000 r.p.m. at 37.5 B.H.P. for five minutes and 450 r.p.m. at idle for one minute. Fifty of these cycles or five hours comprise one interval. At the completion of each interval a check is made for misfiring at 2400 r.p.m. at full load. If no misfiring is observed, the test continued for another interval of five hours. In the event of misfiring it is determined whether one or more spark plugs are failing. A criterion for test termination is three fouled plugs in three difierent cylinders. If less than three plugs fouled simultaneously the fouled plug or plugs are replaced with a new plug and the test continued until a total of three plugs fouled in three different cylinders. The reasons for replacing the fouled plugs with new plugs before continuing the test are:
A. To prevent upsetting test conditions which would affect fouling in other cylinders.
B. To assure that misfiring is caused by the plug or plugs in question.
C. To confirm that some abnormal condition in the cylinder is not causing unusually early fouling.
The foregoing procedure and conditions are observed for the first 139 hours of each test phase. At the end of 139 hours the conditions conducive to spark plug fouling are further enhanced. Consideration is carefully given to future possibility of test duplication before making any change. Beginning with the 140th hour of each test phase and continuing until phase termination, the following changes are in effect:
('1) The air fuel ratio is decreased from 12.4:1 to 11.1:1.
(2) The speed and load cycling is discontinued and changed to a constant speed of 2200 rpm. at 41.2 B.H.P.
(3) As a consequence of the above changes the fuel flow increases from 27.0 #s./hr. to 40.0 #s./hr.
(4) Instead of checking the spark plugs at five hour intervals at full load, an observation with the DuMont Engine analyzer are made each hour without changing the speed or load unless plug fouling is detected.
Throughout the entire test a careful check is keptfion oil consumption. At each 20 hours, as the test progressed, the engine is shut down for a crankcase oil level check. At each 60 hours the oil is changed.
The fuel treated with the additive is blended as follows:
A 4000 gallon capacity storage tank is flushed with the base fuel. 1200 gallons of base fuel are pumped into the tank. A circulating pump is placed in operation with the intake at one end of the tank and the delivery at the opposite end of the required amount of additive is mixed with five gallons of the base gasoline. This mixture is slowly fed into the delivery stream of the fuel from the circulating pump. The fuel blend is recirculated for sixteenhours before start of the test.
The spark plugs selected for the test are AC-43. This spark plug is one degree colder in the heat range than the engine manufacturer recommends for this model. Twenty-four plugs are inspected and pre-tested under air pressure for firing for each test phase. From each batch of 24 plugs eight are selected which were nearly uniform in resistance at maximum pressure. All electrode gaps are adjusted to .040".
' SPECIFICATIONS Engine:
Oldsmobile 1956 Super 88 Type- No. of cylinders 90 degree V-8.
Valve arrangement In head. Bore and stroke 3%" x 3 Piston displacement (cu. in.) 324.31. Compression ratio 9.25:1. Max. brake horsepower, at 4,400
r.p.m. 240. Carburetor:
Rochester 4-barrel- Front Rear A/F Barrel Barrel Ratio jet sizes jet sizes Standard Equipment 49 51 13.121 -139 hours of test. 55 51 12. 4:1 140 hours to termina test 59 5s 11.1;1
Equipment air cleaner used. The air-fuel ratio was determined by a Cambridge Exhaust Gas Tester.
Dynamometer:
Mid West eddy current water cooled 175 h.p. capacity. Torque reaction measured by a Fairbanks Morse beam scale. Instrumentation:
The following temperatures are measured by means of mercury thermometers: Jacket coolant in Jacket coolant out Intake air at carburetor Motor oil in oil pan sump Wet bulb Dry bulb Exhaust back pressures and intake manifold vacuum are measured by means of mercury manometers. Barometric pressure is observed on a convention mercury barometer and was corrected for temperature. Engine oil pressure is measured by a standard Bourdon-type gage.
The rate of fuel consumption is determined on a weight basis using a tip balance. A flowmeter in the supply line provides a check upon engine fuel consumption determined by weighing.
Engine speed is determined by an electronic counter.
Spark plug performance characteristics are observed by means of a multiple trace oscilloscope.
. l0 i Both incipient fouling and 100% fouling of each'spark plug are recorded in hours.
The base fuel used for the test operations is described as follows:
Composition-Mixture of straight run and catalytically cracked gasolines:
Gravity, API 58.8 Bromine number 53 Doctor Negative Sulfur, percent wt. 0.017 Corrosion, cu. strip, 3 hrs. at 122 F None Gum, A.S.T.M. mg. 2.8 Oxidation stability, A.S.T.M. minutes 600 Octane number:
C.F.R.M. 87 C.F.R.R.. 96 Reid vapor pressure at 100 F 8.0 Distillation: e
I IBP, F. 100 10%; 133 20% 148 50% 202 330 End point 386 Recovery 98.5 Residue 0.8 Tetraethyl lead, ml./ gal. 2.92
Fuels containing the compositions of this invention in weight percent of 0.001 to 0.5%, according to this test,
are superior to corresponding fuels containing no additive.
Since spark plug fouling is a function of the lead content of the gasoline, the optimum amount will vary with such content. Although weight ratios of 0.00l2% or more can be employed in gasolines containing about 3 cc. of tetraethylene lead or its equivalent/ gallon of gasoline, generally 0.0011% is usually sufficient for anti-fouling purposes. However, it should be understood that the optimum amount or the weight bases for one particular compound may not be the optimum amount for another compound. One reason for this is that the effectiveness of the compounds vary from one compound to another. Another reason is the variance of molecular weights so that one compound may be twice the molecular weight of another. However, by proper adjustment of concentrations, anti-fouling can be effected. These principles also apply to the other ratios herein stated.
Test III These compounds in the above table are also tested in a hour full scale reciprocity engine test employing Military Specification MIL-G-5572A grade /145 fuel in a Wright R 3350-30W compound engine operated according to the following cycle:
Time per cycle (min.)
Idle l0 Take-oifpower and speed 5 Normal rated power and speed 30 Cruise 90 10% normal rated power and 93% normal rated 30 Cruise 90 Total min 255 The compounds in the above tables are also tested in a 100 hour full scale gas turbine engine test in a Pratt &
Whitney I57-P29 gas turbine engineemploying Specification MIL-J-5624D Grade JP-4 fuel. The engine is operated for 100 hours and cycled in accordance with the Specification MILE-5009 Model qualification ,test. After 100 hours of operation, the engine combustion components and turbine sections are disassembled and inspected for deposits and deleterious effects.
Fuels containing the compositions of thisinvention in weight percent of 0.001 to 0.5%, according to this test, are superior to corresponding fuels containing no additive.
Although the present invention has been described with prefered embodiments, it is to be understood that modifications may be resorted to without departing from the spirit and scope thereof.
The invention includes various fuels such as all grades of gasolines which may contain a wide variety of additives such as antioxidants, organolead stabilizers, organic dyes, solubilizers, etc., as Well as the halide scavengers generally employed such as ethylene dibromide and/ or ethylene dichloride and other scavengers. for example those disclosed in the patents listed above relating to such compositions. Such variations and modifications one considered to be within the purview and scope of the appended claims.
Compounds also included within the scope of the claims are those in the .form of their salts. The basic constituent of these salts can be, for example, any of the monoamines, hydroxylated monoaminegpolyami'nes, hydroxylated polyamines and other variations disclosed in my patent application serial No. 790,351, filed of even date, and assigned to the same assignee as ,the present application.
Having thus. described my invention, what I claim as new and desire to obtain by Letters Patent i's; i
l-. A process offpreve'nting, inhibiting and modifying the formation of deposits in internal combustion and jet engines employing a substantially hydrocarbon fuel whichrcomprises burning in such engines a fuel consisting of a liquid hydrocarbon having a boiling point up to about 500 F. and a minor amount in the range of approximately 0.001 to 2% -by weight of the fuel, sufficient to prevent, inhibit and modify such deposits, of a member selected from the group consisting of an oil soluble alkenyl succinic acid and the anhydride thereof, having 8 to 31 carbon atoms on the alkenyl group.
2. The process of claim 1 where the alkenyl radical has 8-18 carbon atoms. I
3. The process of claim 1 where the hydrocarbon fuel is gasoline.
4. The process of claim 3 where the alkenyl radical has 8-18 carbon atoms. 7 p
5'. The process of claim 1 where the hydrocarbon fuel is a jet fuel. I
6. The process of claim 5 where the alkenyl radical has 8-18 carbon atoms.
References Cited in the file of this patent UNITED STATES PATENTS
Claims (1)
1. A PROCESS OF PREVENTING, INHIBITING AND MODIFYING THE FORMATION OF DEPOSITS IN INTERNAL COMBUSTION AND JET ENGINES EMPLOYING A SUBSTANTIALLY HYDROCARBON FUEL WHICH COMPRISES BURNING IN SUCH ENGINES A FUEL CONSISTING OF A LIQUID HYDROCARBON HAVING A BOILING POINT UP TO ABOUT 500*F. AND A MINOR AMOUNT IN THE RANGE OF APPROXIMATELY 0.001 TO 2% BY WEIGHT OF THE FUEL, SUFFICIENT TO PREVENT, INHIBIT AND MODIFY SUCH DEPOSITS, OF A MEMBER SELECTED FROM THE GROUP CONSISTING OF AN OIL SOLUBLE ALKENYL SUCCINIC ACID AND THE ANHYDRIDE THEREOF, HAVING 8 TO 31 CARBON ATOMS ON THE ALKENYL GROUP.
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US790352A US2993772A (en) | 1959-02-02 | 1959-02-02 | Acid additives |
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US790352A US2993772A (en) | 1959-02-02 | 1959-02-02 | Acid additives |
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US2993772A true US2993772A (en) | 1961-07-25 |
Family
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US790352A Expired - Lifetime US2993772A (en) | 1959-02-02 | 1959-02-02 | Acid additives |
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Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3346354A (en) * | 1963-07-02 | 1967-10-10 | Chvron Res Company | Long-chain alkenyl succinic acids, esters, and anhydrides as fuel detergents |
US4440545A (en) * | 1981-11-02 | 1984-04-03 | Ethyl Corporation | Gasohol having corrosion inhibiting properties |
EP0165776A2 (en) * | 1984-06-13 | 1985-12-27 | Ethyl Corporation | Corrosion inhibitors for alcohol-based fuels |
US4737159A (en) * | 1984-06-29 | 1988-04-12 | E. I. Du Pont De Nemours And Company | Corrosion inhibitor for liquid fuels |
US4752374A (en) * | 1987-04-20 | 1988-06-21 | Betz Laboratories, Inc. | Process for minimizing fouling of processing equipment |
EP0280417A1 (en) * | 1987-02-27 | 1988-08-31 | Petrolite Corporation | Diesel fuel injector additive comprising polyalkenyl succinic acid, diesel fuel containing same and method of use thereof |
EP0299120A1 (en) * | 1987-07-14 | 1989-01-18 | Petrolite Corporation | Alkyl or alkenyl succinic acids as corrosion inhibitors for oxygenated fuels |
WO2006063770A1 (en) * | 2004-12-13 | 2006-06-22 | Basf Aktiengesellschaft | Hydrocarbyl succinic acid and hydrocarbylsuccinic acid derivatives as friction modifiers |
US20160032208A1 (en) * | 2013-03-07 | 2016-02-04 | The Lubrizol Corporation | Ion tolerant corrosion inhibitors and inhibitor combinations for fuels |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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US2386445A (en) * | 1942-01-26 | 1945-10-09 | Petrolite Corp | Composition of matter |
US2450221A (en) * | 1945-08-21 | 1948-09-28 | Texas Co | Shear-resistant grease |
US2568746A (en) * | 1949-04-08 | 1951-09-25 | Visco Products Co | Emulsion breaking |
US2715108A (en) * | 1952-05-06 | 1955-08-09 | Shell Dev | Lubricating compositions |
US2733235A (en) * | 1956-01-31 | Table ii |
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Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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US2733235A (en) * | 1956-01-31 | Table ii | ||
US2386445A (en) * | 1942-01-26 | 1945-10-09 | Petrolite Corp | Composition of matter |
US2450221A (en) * | 1945-08-21 | 1948-09-28 | Texas Co | Shear-resistant grease |
US2568746A (en) * | 1949-04-08 | 1951-09-25 | Visco Products Co | Emulsion breaking |
US2715108A (en) * | 1952-05-06 | 1955-08-09 | Shell Dev | Lubricating compositions |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3346354A (en) * | 1963-07-02 | 1967-10-10 | Chvron Res Company | Long-chain alkenyl succinic acids, esters, and anhydrides as fuel detergents |
US4440545A (en) * | 1981-11-02 | 1984-04-03 | Ethyl Corporation | Gasohol having corrosion inhibiting properties |
EP0165776A2 (en) * | 1984-06-13 | 1985-12-27 | Ethyl Corporation | Corrosion inhibitors for alcohol-based fuels |
EP0165776A3 (en) * | 1984-06-13 | 1986-12-17 | Ethyl Corporation | Corrosion inhibitors for alcohol-based fuels |
US4737159A (en) * | 1984-06-29 | 1988-04-12 | E. I. Du Pont De Nemours And Company | Corrosion inhibitor for liquid fuels |
EP0280417A1 (en) * | 1987-02-27 | 1988-08-31 | Petrolite Corporation | Diesel fuel injector additive comprising polyalkenyl succinic acid, diesel fuel containing same and method of use thereof |
US4752374A (en) * | 1987-04-20 | 1988-06-21 | Betz Laboratories, Inc. | Process for minimizing fouling of processing equipment |
EP0299120A1 (en) * | 1987-07-14 | 1989-01-18 | Petrolite Corporation | Alkyl or alkenyl succinic acids as corrosion inhibitors for oxygenated fuels |
WO2006063770A1 (en) * | 2004-12-13 | 2006-06-22 | Basf Aktiengesellschaft | Hydrocarbyl succinic acid and hydrocarbylsuccinic acid derivatives as friction modifiers |
US20160032208A1 (en) * | 2013-03-07 | 2016-02-04 | The Lubrizol Corporation | Ion tolerant corrosion inhibitors and inhibitor combinations for fuels |
US9873847B2 (en) * | 2013-03-07 | 2018-01-23 | The Lubrizol Corporation | Ion tolerant corrosion inhibitors and inhibitor combinations for fuels |
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