CN114717028B - High-stability methanol gasoline and preparation method thereof - Google Patents
High-stability methanol gasoline and preparation method thereof Download PDFInfo
- Publication number
- CN114717028B CN114717028B CN202110763559.XA CN202110763559A CN114717028B CN 114717028 B CN114717028 B CN 114717028B CN 202110763559 A CN202110763559 A CN 202110763559A CN 114717028 B CN114717028 B CN 114717028B
- Authority
- CN
- China
- Prior art keywords
- methanol
- methanol gasoline
- gasoline
- surfactant
- parts
- 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.)
- Active
Links
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 title claims abstract description 339
- 239000003502 gasoline Substances 0.000 title claims abstract description 105
- 238000002360 preparation method Methods 0.000 title claims abstract description 26
- 239000002199 base oil Substances 0.000 claims abstract description 48
- 230000007797 corrosion Effects 0.000 claims abstract description 44
- 238000005260 corrosion Methods 0.000 claims abstract description 44
- 239000006184 cosolvent Substances 0.000 claims abstract description 41
- 239000003112 inhibitor Substances 0.000 claims abstract description 41
- 239000006079 antiknock agent Substances 0.000 claims abstract description 40
- 239000012752 auxiliary agent Substances 0.000 claims abstract description 37
- 239000002216 antistatic agent Substances 0.000 claims description 49
- MWKFXSUHUHTGQN-UHFFFAOYSA-N decan-1-ol Chemical compound CCCCCCCCCCO MWKFXSUHUHTGQN-UHFFFAOYSA-N 0.000 claims description 44
- 239000000203 mixture Substances 0.000 claims description 44
- 239000004094 surface-active agent Substances 0.000 claims description 38
- 239000002736 nonionic surfactant Substances 0.000 claims description 36
- 238000003756 stirring Methods 0.000 claims description 36
- 239000003945 anionic surfactant Substances 0.000 claims description 35
- 239000003963 antioxidant agent Substances 0.000 claims description 30
- 239000000314 lubricant Substances 0.000 claims description 29
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 25
- PLLBRTOLHQQAQQ-UHFFFAOYSA-N 8-methylnonan-1-ol Chemical compound CC(C)CCCCCCCO PLLBRTOLHQQAQQ-UHFFFAOYSA-N 0.000 claims description 22
- 239000004440 Isodecyl alcohol Substances 0.000 claims description 22
- 239000002994 raw material Substances 0.000 claims description 14
- 150000001298 alcohols Chemical class 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 2
- 230000008569 process Effects 0.000 claims description 2
- 239000002671 adjuvant Substances 0.000 claims 1
- 239000000126 substance Substances 0.000 abstract description 14
- 239000000446 fuel Substances 0.000 abstract description 5
- 230000003749 cleanliness Effects 0.000 abstract description 4
- 239000000463 material Substances 0.000 abstract 1
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 40
- -1 isooctyl ester Chemical class 0.000 description 30
- 230000003078 antioxidant effect Effects 0.000 description 29
- 235000019387 fatty acid methyl ester Nutrition 0.000 description 24
- 150000002191 fatty alcohols Chemical group 0.000 description 23
- 229920000056 polyoxyethylene ether Polymers 0.000 description 23
- 229940051841 polyoxyethylene ether Drugs 0.000 description 23
- AZVCGYPLLBEUNV-UHFFFAOYSA-N lithium;ethanolate Chemical group [Li+].CC[O-] AZVCGYPLLBEUNV-UHFFFAOYSA-N 0.000 description 21
- 239000003208 petroleum Substances 0.000 description 21
- AGAHETWGCFCMDK-UHFFFAOYSA-N 4-methoxybenzene-1,2-diamine Chemical group COC1=CC=C(N)C(N)=C1 AGAHETWGCFCMDK-UHFFFAOYSA-N 0.000 description 20
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical group [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 20
- 239000003921 oil Substances 0.000 description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- ZMRUPTIKESYGQW-UHFFFAOYSA-N propranolol hydrochloride Chemical compound [H+].[Cl-].C1=CC=C2C(OCC(O)CNC(C)C)=CC=CC2=C1 ZMRUPTIKESYGQW-UHFFFAOYSA-N 0.000 description 10
- 239000011780 sodium chloride Substances 0.000 description 10
- 239000002904 solvent Substances 0.000 description 10
- 230000007613 environmental effect Effects 0.000 description 8
- 238000000926 separation method Methods 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 5
- 229910052799 carbon Inorganic materials 0.000 description 5
- 239000010779 crude oil Substances 0.000 description 5
- 230000032798 delamination Effects 0.000 description 5
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 4
- 239000004215 Carbon black (E152) Substances 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 125000000217 alkyl group Chemical group 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 230000008021 deposition Effects 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 239000000693 micelle Substances 0.000 description 3
- 238000011056 performance test Methods 0.000 description 3
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000004721 Polyphenylene oxide Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 238000004220 aggregation Methods 0.000 description 2
- 230000004075 alteration Effects 0.000 description 2
- 150000001412 amines Chemical class 0.000 description 2
- 239000011324 bead Substances 0.000 description 2
- 235000014113 dietary fatty acids Nutrition 0.000 description 2
- 229930195729 fatty acid Natural products 0.000 description 2
- 239000000194 fatty acid Substances 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- PHTQWCKDNZKARW-UHFFFAOYSA-N isoamylol Chemical compound CC(C)CCO PHTQWCKDNZKARW-UHFFFAOYSA-N 0.000 description 2
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000005191 phase separation Methods 0.000 description 2
- 229920000570 polyether Polymers 0.000 description 2
- LPXPTNMVRIOKMN-UHFFFAOYSA-M sodium nitrite Chemical compound [Na+].[O-]N=O LPXPTNMVRIOKMN-UHFFFAOYSA-M 0.000 description 2
- DAJSVUQLFFJUSX-UHFFFAOYSA-M sodium;dodecane-1-sulfonate Chemical group [Na+].CCCCCCCCCCCCS([O-])(=O)=O DAJSVUQLFFJUSX-UHFFFAOYSA-M 0.000 description 2
- OYHQOLUKZRVURQ-NTGFUMLPSA-N (9Z,12Z)-9,10,12,13-tetratritiooctadeca-9,12-dienoic acid Chemical compound C(CCCCCCC\C(=C(/C\C(=C(/CCCCC)\[3H])\[3H])\[3H])\[3H])(=O)O OYHQOLUKZRVURQ-NTGFUMLPSA-N 0.000 description 1
- ICLYJLBTOGPLMC-KVVVOXFISA-N (z)-octadec-9-enoate;tris(2-hydroxyethyl)azanium Chemical compound OCCN(CCO)CCO.CCCCCCCC\C=C/CCCCCCCC(O)=O ICLYJLBTOGPLMC-KVVVOXFISA-N 0.000 description 1
- NLZUEZXRPGMBCV-UHFFFAOYSA-N Butylhydroxytoluene Chemical compound CC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 NLZUEZXRPGMBCV-UHFFFAOYSA-N 0.000 description 1
- MKQBAYZOZPXFGK-UHFFFAOYSA-N C(C=1C(O)=CC=CC1)=NCC(C)N Chemical compound C(C=1C(O)=CC=CC1)=NCC(C)N MKQBAYZOZPXFGK-UHFFFAOYSA-N 0.000 description 1
- 101150076749 C10L gene Proteins 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- BZLVMXJERCGZMT-UHFFFAOYSA-N Methyl tert-butyl ether Chemical compound COC(C)(C)C BZLVMXJERCGZMT-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 235000010354 butylated hydroxytoluene Nutrition 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 239000000539 dimer Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 239000003254 gasoline additive Substances 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002780 morpholines Chemical class 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 125000004430 oxygen atom Chemical group O* 0.000 description 1
- 230000005501 phase interface Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 1
- TVDSBUOJIPERQY-UHFFFAOYSA-N prop-2-yn-1-ol Chemical compound OCC#C TVDSBUOJIPERQY-UHFFFAOYSA-N 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 235000010288 sodium nitrite Nutrition 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 125000001273 sulfonato group Chemical group [O-]S(*)(=O)=O 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 229940117013 triethanolamine oleate Drugs 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Classifications
-
- 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
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
-
- 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
- C10L1/103—Liquid carbonaceous fuels containing additives stabilisation of anti-knock agents
-
- 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
- C10L1/143—Organic compounds mixtures of organic macromolecular compounds with organic non-macromolecular compounds
-
- 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
- C10L10/00—Use of additives to fuels or fires for particular purposes
-
- 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
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/04—Use of additives to fuels or fires for particular purposes for minimising corrosion or incrustation
-
- 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
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/08—Use of additives to fuels or fires for particular purposes for improving lubricity; for reducing wear
-
- 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
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/18—Use of additives to fuels or fires for particular purposes use of detergents or dispersants for purposes not provided for in groups C10L10/02 - C10L10/16
-
- 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
- C10L1/182—Organic compounds containing oxygen containing hydroxy groups; Salts thereof
- C10L1/1822—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms
-
- 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
- C10L1/182—Organic compounds containing oxygen containing hydroxy groups; Salts thereof
- C10L1/1822—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms
- C10L1/1824—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms mono-hydroxy
-
- 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
- C10L1/182—Organic compounds containing oxygen containing hydroxy groups; Salts thereof
- C10L1/1828—Salts thereof
-
- 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
- C10L1/185—Ethers; Acetals; Ketals; Aldehydes; Ketones
- C10L1/1852—Ethers; Acetals; Ketals; Orthoesters
-
- 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
- C10L1/185—Ethers; Acetals; Ketals; Aldehydes; Ketones
- C10L1/1857—Aldehydes; Ketones
-
- 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
- C10L1/19—Esters ester radical containing compounds; ester ethers; carbonic acid esters
-
- 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
- C10L1/1985—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 polyethers, e.g. di- polygylcols and derivatives; ethers - esters
-
- 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
- C10L1/22—Organic compounds containing nitrogen
- C10L1/234—Macromolecular compounds
- C10L1/238—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
-
- 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
- C10L1/24—Organic compounds containing sulfur, selenium and/or tellurium
- C10L1/2431—Organic compounds containing sulfur, selenium and/or tellurium sulfur bond to oxygen, e.g. sulfones, sulfoxides
- C10L1/2437—Sulfonic acids; Derivatives thereof, e.g. sulfonamides, sulfosuccinic acid esters
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Lubricants (AREA)
Abstract
The invention belongs to the field of fuel chemical industry, and particularly relates to high-stability methanol gasoline and a preparation method thereof. The high stability methanol gasoline is prepared with the materials including at least base oil 40-80 weight portions, methanol 20-50 weight portions, cosolvent 1-10 weight portions, corrosion inhibitor 1-5 weight portions, antiknock agent 0.5-1 weight portions and assistant 20-40 weight portions. The inventor adds a certain cosolvent into the methanol gasoline, and improves the compatibility and stability between the methanol and the gasoline through the cosolvent, so that the methanol gasoline can still keep a uniform state after being placed for a long time, and the layering phenomenon of the methanol gasoline is reduced. The inventor reduces the corrosiveness of the methanol gasoline to the gasoline engine by adding a certain corrosion inhibitor, improves the antiknock performance of the methanol gasoline by adding a certain antiknock agent, further improves the stability of the methanol gasoline, and improves the cleanliness and stability of the methanol gasoline by adding a certain auxiliary agent, thereby improving the use quality of the methanol gasoline.
Description
Technical Field
The invention belongs to the technical field of fuel chemical industry, belongs to the technical field of classification number C10L, and particularly relates to high-stability methanol gasoline and a preparation method thereof.
Background
The methanol gasoline is a novel environment-friendly fuel, is a fuel substitute for automobiles, and is an important component of new energy. Crude oil is the most prominent primary energy source worldwide, and the essence of current energy shortage is crude oil shortage. The vehicle fuel is the most main application field of crude oil, and accounts for more than 70% of the total consumption of the crude oil worldwide. Methanol gasoline is a path of replacing oil with coal, and can be used as a substitute of gasoline so as to realize partial substitution of crude oil. However, the methanol gasoline sold in the market at present has poor stability, serious corrosion to a gasoline engine and more carbon deposition, and seriously reduces the use quality of the methanol gasoline.
The patent application number is CN201310721981.4, which discloses a methanol gasoline additive and methanol gasoline containing the additive, the raw materials for preparing the methanol gasoline in the technical scheme mainly comprise methanol, toluene, xylene, isobutanol, isopropanol, isoamyl alcohol, ethanol, 2, 6-di-tert-butyl-p-cresol antioxidant anti-glue agent, N-salicylidene-1, 2-propylenediamine metal passivating agent, polyisobutenylamide isooctyl ester, calcium petroleum sulfonate, benzotriazo file, dimer linoleic acid, sodium nitrite, alkyl polyglycoside, methyl tertiary butyl ether, triethanolamine oleate soap and emulsifier, and more additives are added in the methanol gasoline, so that a better balance state can not be maintained in the aspects of combustion effect and stability.
Patent application number CN201610553994. X discloses a methanol gasoline, wherein the raw materials for preparing the methanol gasoline comprise methanol, methylnaphthalene bisquinoline quaternary ammonium salt, morpholine derivatives, propynyl alcohol and a leveling agent, and the methanol gasoline has better corrosion resistance but poorer stability.
Disclosure of Invention
In order to solve the technical problems, the first aspect of the invention provides high-stability methanol gasoline, which is prepared from the following raw materials, by weight, at least 40-80 parts of base oil, 20-50 parts of methanol, 1-10 parts of cosolvent, 1-5 parts of corrosion inhibitor, 0.5-1 part of antiknock agent and 20-40 parts of auxiliary agent.
As a preferred embodiment, the cosolvent comprises at least one hydrocarbon and its derivatives.
As a preferred embodiment, the hydrocarbon and its derivative have at least one oxygen atom in their molecule.
As a preferred embodiment, the hydrocarbon and its derivative are selected from at least one of alkanes, alcohols, alcohol ethers, ketones, esters and ethers.
As a preferred technical scheme, the alcohol comprises a linear alcohol and a branched alcohol, and the mass ratio of the linear alcohol to the branched alcohol is 1: (3-5).
As a preferred embodiment, the straight-chain alcohol is n-decyl alcohol and the branched-chain alcohol is isodecyl alcohol.
The methanol gasoline contains a certain amount of methanol, the methanol contains hydroxyl with stronger polarity, is easy to form hydrogen bond with water to dissolve with each other, has stronger water absorption, can automatically absorb water from air in the process of storing and using the methanol gasoline, and is a hydrophobic substance. The inventor unexpectedly discovers that when a certain amount of long straight-chain alcohol and long branched-chain alcohol are added into the methanol gasoline, the stability of the methanol gasoline can be better improved, so that the methanol gasoline has certain water-resistant stability. Particularly when the straight chain alcohol is n-decyl alcohol and the branched chain alcohol is isodecyl alcohol, the water separation resistance is better. The inventor considers that possible reasons are that the n-decyl alcohol and the isodecyl alcohol both have alcoholic hydroxyl groups and lipophilic alkyl groups, so that the problems of large polarity difference and incompatibility among oil, water and alcohol can be well relieved. Particularly, branched alcohols, in which a plurality of alkyl chains are adsorbed on the oil phase interface, can improve the compatibility well, but when a large amount of branched alcohols are added, the viscosity of the system increases, and the usability and cleanliness of methanol gasoline are reduced.
As a preferable technical scheme, the corrosion inhibitor at least comprises nitrogen element.
As a preferred technical scheme, the corrosion inhibitor is polyetheramine.
As a preferred embodiment, the polyetheramine has a weight average molecular weight of 400.
When in use, the methanol gasoline can cause larger influence on the gasoline engine, can corrode the gasoline engine and damage the performance of the engine, thereby reducing the service life of the gasoline engine. The inventor finds that by adding certain polyether amine as a corrosion inhibitor, the polyether amine not only can form an adsorption film on the surface of a gasoline engine to prevent the gasoline engine from being corroded and protect the performance of the gasoline engine, but also can improve the separation resistance of methanol gasoline and the stability of the whole methanol gasoline, and can conduct charges generated in a gasoline product due to the existence of amino, so that the charges can leak out in time and the antistatic property and the safety of the product are improved. The inventors found that the use of a smaller molecular weight polyetheramine or a larger molecular weight polyetheramine, while having better corrosion inhibition to gasoline engines, does not improve the compatibility and phase separation resistance of methanol gasoline.
As a preferable technical scheme, the antiknock agent at least comprises ethanol and derivatives thereof.
As a preferable technical scheme, the antiknock agent is lithium ethoxide.
As a preferred embodiment, the auxiliary agent is at least one selected from the group consisting of a surfactant, an antistatic agent, an antioxidant, and a lubricant.
As a preferred embodiment, the surfactant is a nonionic surfactant and/or an anionic surfactant.
As a preferable technical scheme, the surfactant is a mixture of nonionic surfactant and anionic surfactant, and the mass ratio of the nonionic surfactant to the anionic surfactant is (5-7): 1.
as a preferred technical scheme, the anionic surfactant is sulfonate surfactant.
As a preferred embodiment, the sulfonate surfactant has an HLB of 11 to 13.
As a preferable technical scheme, the nonionic surfactant is fatty alcohol polyoxyethylene ether.
Because of the poor compatibility between methanol and base oil, the inventors increased the compatibility between methanol and base oil by adding certain surfactants. The inventor can better improve the compatibility between alcohol and oil and the cleanness and antistatic property of the whole gasoline product by adding a certain anionic surfactant and a nonionic surfactant, especially when the HLB of the sulfonate anionic surfactant is 11-13, and hydrophilic groups in the surfactant are tightly adsorbed on the interface of the oil and alcohol, so that the surface tension can be effectively reduced, brownian movement among methanol liquid beads is prevented, the liquid beads are not easy to agglomerate and grow, and the intersolubility between the methanol and the base oil is improved. And the cleanliness and water separation resistance of the gasoline product can be improved by adding the surfactant. The inventor considers that the water and alcohols in the methanol gasoline can be emulsified due to the combined action of the fatty acid sulfonate and the fatty alcohol polyoxyethylene ether, even if the methanol and the water form a water-in-oil structure, the oil-water interface is converted into an oil-oil interface, so that the methanol gasoline is not easy to phase separation, meanwhile, the micelle formed by the fatty acid sulfonate and the fatty alcohol polyoxyethylene ether are mutually doped and entangled, the mutual action of the micelle is avoided, the aggregation and adhesion of oil sludge and carbon deposit on the surface of a gasoline engine are avoided, meanwhile, the aggregation and the precipitation of the micelle are also avoided, and the storage stability of the whole methanol gasoline is improved.
The second aspect of the invention provides a preparation method of the high-stability methanol gasoline, which at least comprises the following steps:
(1) Adding methanol, cosolvent, corrosion inhibitor, antiknock agent and auxiliary agent into stirring kettle, stirring for 0.1-3h under the condition of 100r/min-500r/min to obtain mixture A;
(2) Adding base oil into the mixture A, and stirring for 1-3h under the condition of 100-500 r/min.
In addition, the raw materials used are commercially available unless otherwise indicated.
The beneficial effects are that: the inventor adds a certain cosolvent into the methanol gasoline, and improves the compatibility and stability between the methanol and the gasoline through the cosolvent, so that the methanol gasoline can still keep a uniform state after being placed for a long time, and the layering phenomenon of the methanol gasoline is reduced. The inventor reduces the corrosiveness of the methanol gasoline to the gasoline engine by adding a certain corrosion inhibitor, improves the antiknock performance of the methanol gasoline by adding a certain antiknock agent, further improves the stability of the methanol gasoline, and improves the cleanliness and stability of the methanol gasoline by adding a certain auxiliary agent, thereby improving the use quality of the methanol gasoline.
Detailed Description
Example 1
In order to solve the technical problem, the first aspect of the present embodiment provides a high-stability methanol gasoline, wherein the preparation raw materials include, by weight, 40 parts of base oil, 20 parts of methanol, 1 part of cosolvent, 1 part of corrosion inhibitor, 0.5 part of antiknock agent and 20 parts of auxiliary agent.
The base oil comprises No. 93 gasoline, no. 120 solvent oil and industrial petroleum ether, and the weight ratio of the base oil is 1:2:1, the industrial petroleum ether is purchased from Shandong Xin chemical industry Co., ltd, and the CAS number is: 133-1-51. The cosolvent is a mixture of n-decyl alcohol and isodecyl alcohol, and the mass ratio between the n-decyl alcohol and the isodecyl alcohol is 1:3. the corrosion inhibitor is polyetheramine, the weight average molecular weight of the polyetheramine is 400, and the polyetheramine is purchased from Aite (Shandong) New Material Co., ltd., CAS number: 9046-10-0. The antiknock agent is lithium ethoxide purchased from the wuhan kemi biotechnology pharmaceutical technology company, CAS number: 2388-07-0. The auxiliary agent is a surfactant, an antistatic agent, an antioxidant and a lubricant, wherein the surfactant is 18 parts, the antistatic agent is 1 part, the antioxidant is 0.5 part and the lubricant is 0.5 part, the surfactant is a mixture of a nonionic surfactant and an anionic surfactant, and the mass ratio of the nonionic surfactant to the anionic surfactant is 5:1. the anionic surfactant is fatty acid methyl ester ethoxylated sodium sulfonate, the HLB of the fatty acid methyl ester ethoxylated sodium sulfonate is 12.5, the fatty acid methyl ester ethoxylated sodium sulfonate is purchased from Jinhui environmental protection technology Co., dongguan city, the nonionic surfactant is fatty alcohol polyoxyethylene ether, and the fatty alcohol polyoxyethylene ether is purchased from Jiangsu province sea-ampere petrochemical plant, model: AEO-8. The antistatic agent is an antistatic agent T1502, and the antistatic agent T1502 is purchased from sea-ampere petrochemical plant in Jiangsu province. The antioxidant is 4-methoxy o-phenylenediamine, and the 4-methoxy o-phenylenediamine is purchased from Shanghai Michelin Biochemical technology Co., ltd, and has the product number of: m828055. The lubricant is sodium chloride.
The second aspect of the invention provides a preparation method of the high-stability methanol gasoline, which comprises the following steps:
(1) Adding methanol, a cosolvent, a corrosion inhibitor, an antiknock agent and an auxiliary agent into a stirring kettle, and stirring for 0.2h under the condition of 200r/min to obtain a mixture A;
(2) Adding base oil into the mixture A, and stirring for 0.5h under the condition of 500 r/min.
Example 2
In order to solve the technical problem, the first aspect of the embodiment provides a high-stability methanol gasoline, which comprises, by weight, 60 parts of base oil, 35 parts of methanol, 5 parts of cosolvent, 2.5 parts of corrosion inhibitor, 0.75 part of antiknock agent and 30 parts of auxiliary agent. The base oil comprises No. 93 gasoline, no. 120 solvent oil and industrial petroleum ether, and the weight ratio of the base oil is 1:2:1, the industrial petroleum ether is purchased from Shandong Xin chemical industry Co., ltd, and the CAS number is: 133-1-51. The cosolvent is a mixture of n-decyl alcohol and isodecyl alcohol, and the mass ratio between the n-decyl alcohol and the isodecyl alcohol is 1:3. the corrosion inhibitor is polyetheramine, the weight average molecular weight of the polyetheramine is 400, and the polyetheramine is purchased from Aite (Shandong) New Material Co., ltd., CAS number: 9046-10-0. The antiknock agent is lithium ethoxide purchased from the wuhan kemi biotechnology pharmaceutical technology company, CAS number: 2388-07-0. The auxiliary agent comprises 24 parts of surfactant, 3 parts of antistatic agent, 1.5 parts of antioxidant and 1.5 parts of lubricant, wherein the surfactant is a mixture of nonionic surfactant and anionic surfactant, and the mass ratio of the nonionic surfactant to the anionic surfactant is 5:1. the anionic surfactant is fatty acid methyl ester ethoxylated sodium sulfonate, the HLB of the fatty acid methyl ester ethoxylated sodium sulfonate is 12.5, the fatty acid methyl ester ethoxylated sodium sulfonate is purchased from Jinhui environmental protection technology Co., dongguan city, the nonionic surfactant is fatty alcohol polyoxyethylene ether, and the fatty alcohol polyoxyethylene ether is purchased from Jiangsu province sea-ampere petrochemical plant, model: AEO-8. The antistatic agent is an antistatic agent T1502, and the antistatic agent T1502 is purchased from sea-ampere petrochemical plant in Jiangsu province. The antioxidant is 4-methoxy o-phenylenediamine, and the 4-methoxy o-phenylenediamine is purchased from Shanghai Michelin Biochemical technology Co., ltd, and has the product number of: m828055. The lubricant is sodium chloride.
The second aspect of the invention provides a preparation method of the high-stability methanol gasoline, which comprises the following steps:
(1) Adding methanol, a cosolvent, a corrosion inhibitor, an antiknock agent and an auxiliary agent into a stirring kettle, and stirring for 0.2h under the condition of 200r/min to obtain a mixture A;
(2) Adding base oil into the mixture A, and stirring for 0.5h under the condition of 500 r/min.
Example 3
In order to solve the technical problem, the first aspect of the present embodiment provides a high-stability methanol gasoline, wherein the preparation raw materials include, by weight, 80 parts of base oil, 50 parts of methanol, 10 parts of cosolvent, 5 parts of corrosion inhibitor, 1 part of antiknock agent and 40 parts of auxiliary agent. The base oil comprises No. 93 gasoline, no. 120 solvent oil and industrial petroleum ether, and the weight ratio of the base oil is 1:2:1, the industrial petroleum ether is purchased from Shandong Xin chemical industry Co., ltd, and the CAS number is: 133-1-51. The cosolvent is a mixture of n-decyl alcohol and isodecyl alcohol, and the mass ratio between the n-decyl alcohol and the isodecyl alcohol is 1:3. the corrosion inhibitor is polyetheramine, the weight average molecular weight of the polyetheramine is 400, and the polyetheramine is purchased from Aite (Shandong) New Material Co., ltd., CAS number: 9046-10-0. The antiknock agent is lithium ethoxide purchased from the wuhan kemi biotechnology pharmaceutical technology company, CAS number: 2388-07-0. The auxiliary agent comprises 30 parts of surfactant, 4 parts of antistatic agent, 3 parts of antioxidant and 3 parts of lubricant, wherein the surfactant is a mixture of nonionic surfactant and anionic surfactant, and the mass ratio of the nonionic surfactant to the anionic surfactant is 5:1. the anionic surfactant is fatty acid methyl ester ethoxylated sodium sulfonate, the HLB of the fatty acid methyl ester ethoxylated sodium sulfonate is 12.5, the fatty acid methyl ester ethoxylated sodium sulfonate is purchased from Jinhui environmental protection technology Co., dongguan city, the nonionic surfactant is fatty alcohol polyoxyethylene ether, and the fatty alcohol polyoxyethylene ether is purchased from Jiangsu province sea-ampere petrochemical plant, model: AEO-8. The antistatic agent is an antistatic agent T1502, and the antistatic agent T1502 is purchased from sea-ampere petrochemical plant in Jiangsu province. The antioxidant is 4-methoxy o-phenylenediamine, and the 4-methoxy o-phenylenediamine is purchased from Shanghai Michelin Biochemical technology Co., ltd, and has the product number of: m828055. The lubricant is sodium chloride.
The second aspect of the invention provides a preparation method of the high-stability methanol gasoline, which comprises the following steps:
(1) Adding methanol, a cosolvent, a corrosion inhibitor, an antiknock agent and an auxiliary agent into a stirring kettle, and stirring for 0.2h under the condition of 200r/min to obtain a mixture A;
(2) Adding base oil into the mixture A, and stirring for 0.5h under the condition of 500 r/min.
Example 4
In order to solve the technical problem, the first aspect of the present embodiment provides a high-stability methanol gasoline, wherein the preparation raw materials include, by weight, 40 parts of base oil, 20 parts of methanol, 1 part of cosolvent, 1 part of corrosion inhibitor, 0.5 part of antiknock agent and 20 parts of auxiliary agent.
The base oil comprises No. 93 gasoline, no. 120 solvent oil and industrial petroleum ether, and the weight ratio of the base oil is 1:2:1, the industrial petroleum ether is purchased from Shandong Xin chemical industry Co., ltd, and the CAS number is: 133-1-51. The cosolvent is a mixture of n-decyl alcohol and isodecyl alcohol, and the mass ratio between the n-decyl alcohol and the isodecyl alcohol is 1:5. the corrosion inhibitor is polyetheramine, the weight average molecular weight of the polyetheramine is 400, and the polyetheramine is purchased from Aite (Shandong) New Material Co., ltd., CAS number: 9046-10-0. The antiknock agent is lithium ethoxide purchased from the wuhan kemi biotechnology pharmaceutical technology company, CAS number: 2388-07-0. The auxiliary agent is a surfactant, an antistatic agent, an antioxidant and a lubricant, wherein the surfactant is 18 parts, the antistatic agent is 1 part, the antioxidant is 0.5 part and the lubricant is 0.5 part, the surfactant is a mixture of a nonionic surfactant and an anionic surfactant, and the mass ratio of the nonionic surfactant to the anionic surfactant is 5:1. the anionic surfactant is fatty acid methyl ester ethoxylated sodium sulfonate, the HLB of the fatty acid methyl ester ethoxylated sodium sulfonate is 12.5, the fatty acid methyl ester ethoxylated sodium sulfonate is purchased from Jinhui environmental protection technology Co., dongguan city, the nonionic surfactant is fatty alcohol polyoxyethylene ether, and the fatty alcohol polyoxyethylene ether is purchased from Jiangsu province sea-ampere petrochemical plant, model: AEO-8. The antistatic agent is an antistatic agent T1502, and the antistatic agent T1502 is purchased from sea-ampere petrochemical plant in Jiangsu province. The antioxidant is 4-methoxy o-phenylenediamine, and the 4-methoxy o-phenylenediamine is purchased from Shanghai Michelin Biochemical technology Co., ltd, and has the product number of: m828055. The lubricant is sodium chloride.
The second aspect of the invention provides a preparation method of the high-stability methanol gasoline, which comprises the following steps:
(1) Adding methanol, a cosolvent, a corrosion inhibitor, an antiknock agent and an auxiliary agent into a stirring kettle, and stirring for 0.2h under the condition of 200r/min to obtain a mixture A;
(2) Adding base oil into the mixture A, and stirring for 0.5h under the condition of 500 r/min.
Example 5
In order to solve the technical problem, the first aspect of the present embodiment provides a high-stability methanol gasoline, wherein the preparation raw materials include, by weight, 40 parts of base oil, 20 parts of methanol, 1 part of cosolvent, 1 part of corrosion inhibitor, 0.5 part of antiknock agent and 20 parts of auxiliary agent.
The base oil comprises No. 93 gasoline, no. 120 solvent oil and industrial petroleum ether, and the weight ratio of the base oil is 1:2:1, the industrial petroleum ether is purchased from Shandong Xin chemical industry Co., ltd, and the CAS number is: 133-1-51. The cosolvent is a mixture of n-decyl alcohol and isodecyl alcohol, and the mass ratio between the n-decyl alcohol and the isodecyl alcohol is 1:10. the corrosion inhibitor is polyetheramine, the weight average molecular weight of the polyetheramine is 400, and the polyetheramine is purchased from Aite (Shandong) New Material Co., ltd., CAS number: 9046-10-0. The antiknock agent is lithium ethoxide purchased from the wuhan kemi biotechnology pharmaceutical technology company, CAS number: 2388-07-0. The auxiliary agent is a surfactant, an antistatic agent, an antioxidant and a lubricant, wherein the surfactant is 18 parts, the antistatic agent is 1 part, the antioxidant is 0.5 part and the lubricant is 0.5 part, the surfactant is a mixture of a nonionic surfactant and an anionic surfactant, and the mass ratio of the nonionic surfactant to the anionic surfactant is 5:1. the anionic surfactant is fatty acid methyl ester ethoxylated sodium sulfonate, the HLB of the fatty acid methyl ester ethoxylated sodium sulfonate is 12.5, the fatty acid methyl ester ethoxylated sodium sulfonate is purchased from Jinhui environmental protection technology Co., dongguan city, the nonionic surfactant is fatty alcohol polyoxyethylene ether, and the fatty alcohol polyoxyethylene ether is purchased from Jiangsu province sea-ampere petrochemical plant, model: AEO-8. The antistatic agent is an antistatic agent T1502, and the antistatic agent T1502 is purchased from sea-ampere petrochemical plant in Jiangsu province. The antioxidant is 4-methoxy o-phenylenediamine, and the 4-methoxy o-phenylenediamine is purchased from Shanghai Michelin Biochemical technology Co., ltd, and has the product number of: m828055. The lubricant is sodium chloride.
The second aspect of the invention provides a preparation method of the high-stability methanol gasoline, which comprises the following steps:
(1) Adding methanol, a cosolvent, a corrosion inhibitor, an antiknock agent and an auxiliary agent into a stirring kettle, and stirring for 0.2h under the condition of 200r/min to obtain a mixture A;
(2) Adding base oil into the mixture A, and stirring for 0.5h under the condition of 500 r/min.
Example 6
In order to solve the technical problem, the first aspect of the present embodiment provides a high-stability methanol gasoline, wherein the preparation raw materials include, by weight, 40 parts of base oil, 20 parts of methanol, 1 part of cosolvent, 1 part of corrosion inhibitor, 0.5 part of antiknock agent and 20 parts of auxiliary agent.
The base oil comprises No. 93 gasoline, no. 120 solvent oil and industrial petroleum ether, and the weight ratio of the base oil is 1:2:1, the industrial petroleum ether is purchased from Shandong Xin chemical industry Co., ltd, and the CAS number is: 133-1-51. The cosolvent is isopropanol. The corrosion inhibitor is polyetheramine, the weight average molecular weight of the polyetheramine is 400, and the polyetheramine is purchased from Aite (Shandong) New Material Co., ltd., CAS number: 9046-10-0. The antiknock agent is lithium ethoxide purchased from the wuhan kemi biotechnology pharmaceutical technology company, CAS number: 2388-07-0. The auxiliary agent is a surfactant, an antistatic agent, an antioxidant and a lubricant, wherein the surfactant is 18 parts, the antistatic agent is 1 part, the antioxidant is 0.5 part and the lubricant is 0.5 part, the surfactant is a mixture of a nonionic surfactant and an anionic surfactant, and the mass ratio of the nonionic surfactant to the anionic surfactant is 5:1. the anionic surfactant is fatty acid methyl ester ethoxylated sodium sulfonate, the HLB of the fatty acid methyl ester ethoxylated sodium sulfonate is 12.5, the fatty acid methyl ester ethoxylated sodium sulfonate is purchased from Jinhui environmental protection technology Co., dongguan city, the nonionic surfactant is fatty alcohol polyoxyethylene ether, and the fatty alcohol polyoxyethylene ether is purchased from Jiangsu province sea-ampere petrochemical plant, model: AEO-8. The antistatic agent is an antistatic agent T1502, and the antistatic agent T1502 is purchased from sea-ampere petrochemical plant in Jiangsu province. The antioxidant is 4-methoxy o-phenylenediamine, and the 4-methoxy o-phenylenediamine is purchased from Shanghai Michelin Biochemical technology Co., ltd, and has the product number of: m828055. The lubricant is sodium chloride.
The second aspect of the invention provides a preparation method of the high-stability methanol gasoline, which comprises the following steps:
(1) Adding methanol, a cosolvent, a corrosion inhibitor, an antiknock agent and an auxiliary agent into a stirring kettle, and stirring for 0.2h under the condition of 200r/min to obtain a mixture A;
(2) Adding base oil into the mixture A, and stirring for 0.5h under the condition of 500 r/min.
Example 7
In order to solve the technical problem, the first aspect of the present embodiment provides a high-stability methanol gasoline, wherein the preparation raw materials include, by weight, 40 parts of base oil, 20 parts of methanol, 1 part of cosolvent, 1 part of corrosion inhibitor, 0.5 part of antiknock agent and 20 parts of auxiliary agent.
The base oil comprises No. 93 gasoline, no. 120 solvent oil and industrial petroleum ether, and the weight ratio of the base oil is 1:2:1, the industrial petroleum ether is purchased from Shandong Xin chemical industry Co., ltd, and the CAS number is: 133-1-51. The cosolvent is a mixture of n-decyl alcohol and isodecyl alcohol, and the mass ratio between the n-decyl alcohol and the isodecyl alcohol is 1:3. the corrosion inhibitor is polyetheramine, the weight average molecular weight of the polyetheramine is 230, and the polyetheramine is purchased from Aite (Shandong) New Material Co., ltd., CAS number: 9046-10-0. The antiknock agent is lithium ethoxide purchased from the wuhan kemi biotechnology pharmaceutical technology company, CAS number: 2388-07-0. The auxiliary agent is a surfactant, an antistatic agent, an antioxidant and a lubricant, wherein the surfactant is 18 parts, the antistatic agent is 1 part, the antioxidant is 0.5 part and the lubricant is 0.5 part, the surfactant is a mixture of a nonionic surfactant and an anionic surfactant, and the mass ratio of the nonionic surfactant to the anionic surfactant is 5:1. the anionic surfactant is fatty acid methyl ester ethoxylated sodium sulfonate, the HLB of the fatty acid methyl ester ethoxylated sodium sulfonate is 12.5, the fatty acid methyl ester ethoxylated sodium sulfonate is purchased from Jinhui environmental protection technology Co., dongguan city, the nonionic surfactant is fatty alcohol polyoxyethylene ether, and the fatty alcohol polyoxyethylene ether is purchased from Jiangsu province sea-ampere petrochemical plant, model: AEO-8. The antistatic agent is an antistatic agent T1502, and the antistatic agent T1502 is purchased from sea-ampere petrochemical plant in Jiangsu province. The antioxidant is 4-methoxy o-phenylenediamine, and the 4-methoxy o-phenylenediamine is purchased from Shanghai Michelin Biochemical technology Co., ltd, and has the product number of: m828055. The lubricant is sodium chloride.
The second aspect of the invention provides a preparation method of the high-stability methanol gasoline, which comprises the following steps:
(1) Adding methanol, a cosolvent, a corrosion inhibitor, an antiknock agent and an auxiliary agent into a stirring kettle, and stirring for 0.2h under the condition of 200r/min to obtain a mixture A;
(2) Adding base oil into the mixture A, and stirring for 0.5h under the condition of 500 r/min.
Example 8
In order to solve the technical problem, the first aspect of the present embodiment provides a high-stability methanol gasoline, wherein the preparation raw materials include, by weight, 40 parts of base oil, 20 parts of methanol, 1 part of cosolvent, 1 part of corrosion inhibitor, 0.5 part of antiknock agent and 20 parts of auxiliary agent.
The base oil comprises No. 93 gasoline, no. 120 solvent oil and industrial petroleum ether, and the weight ratio of the base oil is 1:2:1, the industrial petroleum ether is purchased from Shandong Xin chemical industry Co., ltd, and the CAS number is: 133-1-51. The cosolvent is a mixture of n-decyl alcohol and isodecyl alcohol, and the mass ratio between the n-decyl alcohol and the isodecyl alcohol is 1:3. the corrosion inhibitor is polyetheramine, the weight average molecular weight of the polyetheramine is 2000, and the polyetheramine is purchased from Aite (Shandong) New Material Co., ltd., CAS number: 9046-10-0. The antiknock agent is lithium ethoxide purchased from the wuhan kemi biotechnology pharmaceutical technology company, CAS number: 2388-07-0. The auxiliary agent is a surfactant, an antistatic agent, an antioxidant and a lubricant, wherein the surfactant is 18 parts, the antistatic agent is 1 part, the antioxidant is 0.5 part and the lubricant is 0.5 part, the surfactant is a mixture of a nonionic surfactant and an anionic surfactant, and the mass ratio of the nonionic surfactant to the anionic surfactant is 5:1. the anionic surfactant is fatty acid methyl ester ethoxylated sodium sulfonate, the HLB of the fatty acid methyl ester ethoxylated sodium sulfonate is 12.5, the fatty acid methyl ester ethoxylated sodium sulfonate is purchased from Jinhui environmental protection technology Co., dongguan city, the nonionic surfactant is fatty alcohol polyoxyethylene ether, and the fatty alcohol polyoxyethylene ether is purchased from Jiangsu province sea-ampere petrochemical plant, model: AEO-8. The antistatic agent is an antistatic agent T1502, and the antistatic agent T1502 is purchased from sea-ampere petrochemical plant in Jiangsu province. The antioxidant is 4-methoxy o-phenylenediamine, and the 4-methoxy o-phenylenediamine is purchased from Shanghai Michelin Biochemical technology Co., ltd, and has the product number of: m828055. The lubricant is sodium chloride.
The second aspect of the invention provides a preparation method of the high-stability methanol gasoline, which comprises the following steps:
(1) Adding methanol, a cosolvent, a corrosion inhibitor, an antiknock agent and an auxiliary agent into a stirring kettle, and stirring for 0.2h under the condition of 200r/min to obtain a mixture A;
(2) Adding base oil into the mixture A, and stirring for 0.5h under the condition of 500 r/min.
Example 9
In order to solve the technical problem, the first aspect of the present embodiment provides a high-stability methanol gasoline, wherein the preparation raw materials include, by weight, 40 parts of base oil, 20 parts of methanol, 1 part of cosolvent, 1 part of corrosion inhibitor, 0.5 part of antiknock agent and 20 parts of auxiliary agent.
The base oil comprises No. 93 gasoline, no. 120 solvent oil and industrial petroleum ether, and the weight ratio of the base oil is 1:2:1, the industrial petroleum ether is purchased from Shandong Xin chemical industry Co., ltd, and the CAS number is: 133-1-51. The cosolvent is a mixture of n-decyl alcohol and isodecyl alcohol, and the mass ratio between the n-decyl alcohol and the isodecyl alcohol is 1:3. the corrosion inhibitor is polyetheramine, the weight average molecular weight of the polyetheramine is 400, and the polyetheramine is purchased from Aite (Shandong) New Material Co., ltd., CAS number: 9046-10-0. The antiknock agent is lithium ethoxide purchased from the wuhan kemi biotechnology pharmaceutical technology company, CAS number: 2388-07-0. The auxiliary agent is a surfactant, an antistatic agent, an antioxidant and a lubricant, wherein the surfactant is 18 parts, the antistatic agent is 1 part, the antioxidant is 0.5 part and the lubricant is 0.5 part, the surfactant is a mixture of a nonionic surfactant and an anionic surfactant, and the mass ratio of the nonionic surfactant to the anionic surfactant is 5:1. the anionic surfactant is sodium dodecyl sulfonate, the HLB of the sodium dodecyl sulfonate is 40, the nonionic surfactant is fatty alcohol polyoxyethylene ether, and the fatty alcohol polyoxyethylene ether is purchased from Jiangsu province sea-ampere petrochemical plant, model: AEO-8. The antistatic agent is an antistatic agent T1502, and the antistatic agent T1502 is purchased from sea-ampere petrochemical plant in Jiangsu province. The antioxidant is 4-methoxy o-phenylenediamine, and the 4-methoxy o-phenylenediamine is purchased from Shanghai Michelin Biochemical technology Co., ltd, and has the product number of: m828055. The lubricant is sodium chloride.
The second aspect of the invention provides a preparation method of the high-stability methanol gasoline, which comprises the following steps:
(1) Adding methanol, a cosolvent, a corrosion inhibitor, an antiknock agent and an auxiliary agent into a stirring kettle, and stirring for 0.2h under the condition of 200r/min to obtain a mixture A;
(2) Adding base oil into the mixture A, and stirring for 0.5h under the condition of 500 r/min.
Example 10
In order to solve the technical problem, the first aspect of the present embodiment provides a high-stability methanol gasoline, wherein the preparation raw materials include, by weight, 40 parts of base oil, 20 parts of methanol, 1 part of cosolvent, 1 part of corrosion inhibitor, 0.5 part of antiknock agent and 20 parts of auxiliary agent.
The base oil comprises No. 93 gasoline, no. 120 solvent oil and industrial petroleum ether, and the weight ratio of the base oil is 1:2:1, the industrial petroleum ether is purchased from Shandong Xin chemical industry Co., ltd, and the CAS number is: 133-1-51. The cosolvent is a mixture of n-decyl alcohol and isodecyl alcohol, and the mass ratio between the n-decyl alcohol and the isodecyl alcohol is 1:3. the corrosion inhibitor is polyetheramine, the weight average molecular weight of the polyetheramine is 400, and the polyetheramine is purchased from Aite (Shandong) New Material Co., ltd., CAS number: 9046-10-0. The antiknock agent is lithium ethoxide purchased from the wuhan kemi biotechnology pharmaceutical technology company, CAS number: 2388-07-0. The auxiliary agent comprises 18 parts of surfactant, 1 part of antistatic agent, 0.5 part of antioxidant and 0.5 part of lubricant, wherein the surfactant is a nonionic surfactant, the nonionic surfactant is fatty alcohol polyoxyethylene ether, and the fatty alcohol polyoxyethylene ether is purchased from Jiangsu province sea-ampere petrochemical factory, model: AEO-8. The antistatic agent is an antistatic agent T1502, and the antistatic agent T1502 is purchased from sea-ampere petrochemical plant in Jiangsu province. The antioxidant is 4-methoxy o-phenylenediamine, and the 4-methoxy o-phenylenediamine is purchased from Shanghai Michelin Biochemical technology Co., ltd, and has the product number of: m828055. The lubricant is sodium chloride.
The second aspect of the invention provides a preparation method of the high-stability methanol gasoline, which comprises the following steps:
(1) Adding methanol, a cosolvent, a corrosion inhibitor, an antiknock agent and an auxiliary agent into a stirring kettle, and stirring for 0.2h under the condition of 200r/min to obtain a mixture A;
(2) Adding base oil into the mixture A, and stirring for 0.5h under the condition of 500 r/min.
Performance testing
Performance test 1
The methanol gasoline of examples 1 to 10 was left in the room temperature (25 ℃) and low temperature (-30 ℃) environments for 48 hours, respectively, and visually examined for delamination, wherein delamination at room temperature (25 ℃) was recorded as failed, delamination at room temperature (25 ℃) was not recorded as failed, delamination at low temperature (-30 ℃) was recorded as failed, and delamination at low temperature (-30 ℃) was recorded as failed.
Performance test II
Adding 1wt% of water into the methanol gasoline of examples 1-10, and oscillating for 5min up and down; the frequency is 5 times/s up and down, then standing is carried out for 48 hours, and the existence of layering phenomenon is observed, wherein the methanol gasoline is not layered, the separation resistance is recorded as qualified, the methanol gasoline is layered, and the separation resistance is recorded as unqualified.
Performance test III
The gasoline prepared in examples 1-10 was used in automobiles, and the carbon deposition index was tested by the original gasoline engine carbon deposition detection method of oellcheck.
Room temperature stability | Low temperature stability | Resistance to separation | Carbon index | |
Example 1 | Qualified product | Qualified product | Qualified product | 0.01 |
Example 2 | Qualified product | Qualified product | Qualified product | 0.01 |
Example 3 | Qualified product | Qualified product | Qualified product | 0.01 |
Example 4 | Qualified product | Qualified product | Qualified product | 0.01 |
Example 5 | Qualified product | Qualified product | Failure to pass | 0.08 |
Example 6 | Qualified product | Failure to pass | Failure to pass | 0.16 |
Example 7 | Failure to pass | Failure to pass | Failure to pass | 0.18 |
Example 8 | Failure to pass | Failure to pass | Failure to pass | 0.20 |
Example 9 | Qualified product | Failure to pass | Failure to pass | 0.13 |
Example 10 | Qualified product | Failure to pass | Failure to pass | 0.15 |
The above description is only a preferred embodiment of the present invention, and is not intended to limit the invention in any way, and any person skilled in the art may make modifications or alterations to the disclosed technical content to equivalent embodiments without departing from the technical content of the present invention, and any simple modification, equivalent changes and alterations to the above embodiments according to the technical substance of the present invention still fall within the scope of the technical solution of the present invention.
Claims (6)
1. The methanol gasoline with high stability is characterized in that the preparation raw materials at least comprise 40-80 parts by weight of base oil, 20-50 parts by weight of methanol, 1-10 parts by weight of cosolvent, 1-5 parts by weight of corrosion inhibitor, 0.5-1 part by weight of antiknock agent and 20-40 parts by weight of auxiliary agent; the cosolvent comprises alcohols; the alcohols are straight-chain alcohols and branched-chain alcohols; the mass ratio between the linear alcohol and the branched alcohol is 1: (3-5); the straight chain alcohol is n-decyl alcohol, and the branched chain alcohol is isodecyl alcohol; the corrosion inhibitor is polyetheramine; the polyetheramine has a weight average molecular weight of 400.
2. The high stability methanol gasoline of claim 1 wherein the antiknock agent comprises at least ethanol and its derivatives.
3. The high stability methanol gasoline of claim 1 wherein the adjuvant is selected from at least one of surfactants, antistatic agents, antioxidants, and lubricants.
4. A highly stable methanol gasoline according to claim 3, characterized in that the surfactant is a nonionic surfactant and/or an anionic surfactant.
5. The high stability methanol gasoline of claim 4 wherein the surfactant is a mixture of nonionic surfactant and anionic surfactant in a mass ratio of (5-7): 1.
6. a process for the preparation of a high stability methanol gasoline according to any one of claims 1 to 5, characterized in that it comprises at least the steps of:
(1) Adding methanol, cosolvent, corrosion inhibitor, antiknock agent and auxiliary agent into stirring kettle, stirring for 0.1-3h under the condition of 100r/min-500r/min to obtain mixture A;
(2) Adding base oil into the mixture A, and stirring for 1-3h under the condition of 100-500 r/min.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110763559.XA CN114717028B (en) | 2021-07-06 | 2021-07-06 | High-stability methanol gasoline and preparation method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110763559.XA CN114717028B (en) | 2021-07-06 | 2021-07-06 | High-stability methanol gasoline and preparation method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN114717028A CN114717028A (en) | 2022-07-08 |
CN114717028B true CN114717028B (en) | 2023-11-10 |
Family
ID=82234843
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202110763559.XA Active CN114717028B (en) | 2021-07-06 | 2021-07-06 | High-stability methanol gasoline and preparation method thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN114717028B (en) |
Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101885999A (en) * | 2010-07-14 | 2010-11-17 | 河南煤业化工集团有限责任公司 | Clean methanol gasoline and preparation method thereof |
CN101899330A (en) * | 2009-05-27 | 2010-12-01 | 中国石油化工股份有限公司 | Diesel composition and method for improving oxidation stability of biodiesel |
CN101935560A (en) * | 2010-09-09 | 2011-01-05 | 上海化工研究院 | Methanol diesel oil microemulsion and preparation method thereof |
CN101948396A (en) * | 2010-08-23 | 2011-01-19 | 李治 | Polyether amine, production method thereof and application of polyether amine in methanol gasoline |
CN102517101A (en) * | 2011-12-23 | 2012-06-27 | 江苏玖尚燃油发展有限公司 | Automobile methanol diesel fuel and preparation method thereof |
CN103361128A (en) * | 2013-07-24 | 2013-10-23 | 杨成山 | Methanol gasoline for vehicles |
CN108587810A (en) * | 2018-04-13 | 2018-09-28 | 华阳新兴科技(天津)集团有限公司 | A kind of aircraft external surface cleaning agent and preparation method thereof |
CN109321292A (en) * | 2018-10-24 | 2019-02-12 | 深圳市端致科技材料有限公司 | Engine high ethanol gasoline additive composition and its methanol gasoline under a kind of low temperature |
CN110564461A (en) * | 2019-09-19 | 2019-12-13 | 湖北清合新能源科技有限公司 | Methanol gasoline |
CN110564463A (en) * | 2019-09-19 | 2019-12-13 | 湖北清合新能源科技有限公司 | gasoline additive |
CN111139141A (en) * | 2019-12-26 | 2020-05-12 | 安徽渺微科技有限公司 | Cleaning agent for heavy oil dirt on inner wall of petrochemical pipeline and preparation method thereof |
-
2021
- 2021-07-06 CN CN202110763559.XA patent/CN114717028B/en active Active
Patent Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101899330A (en) * | 2009-05-27 | 2010-12-01 | 中国石油化工股份有限公司 | Diesel composition and method for improving oxidation stability of biodiesel |
CN101885999A (en) * | 2010-07-14 | 2010-11-17 | 河南煤业化工集团有限责任公司 | Clean methanol gasoline and preparation method thereof |
CN101948396A (en) * | 2010-08-23 | 2011-01-19 | 李治 | Polyether amine, production method thereof and application of polyether amine in methanol gasoline |
CN101935560A (en) * | 2010-09-09 | 2011-01-05 | 上海化工研究院 | Methanol diesel oil microemulsion and preparation method thereof |
CN102517101A (en) * | 2011-12-23 | 2012-06-27 | 江苏玖尚燃油发展有限公司 | Automobile methanol diesel fuel and preparation method thereof |
CN103361128A (en) * | 2013-07-24 | 2013-10-23 | 杨成山 | Methanol gasoline for vehicles |
CN108587810A (en) * | 2018-04-13 | 2018-09-28 | 华阳新兴科技(天津)集团有限公司 | A kind of aircraft external surface cleaning agent and preparation method thereof |
CN109321292A (en) * | 2018-10-24 | 2019-02-12 | 深圳市端致科技材料有限公司 | Engine high ethanol gasoline additive composition and its methanol gasoline under a kind of low temperature |
CN110564461A (en) * | 2019-09-19 | 2019-12-13 | 湖北清合新能源科技有限公司 | Methanol gasoline |
CN110564463A (en) * | 2019-09-19 | 2019-12-13 | 湖北清合新能源科技有限公司 | gasoline additive |
CN111139141A (en) * | 2019-12-26 | 2020-05-12 | 安徽渺微科技有限公司 | Cleaning agent for heavy oil dirt on inner wall of petrochemical pipeline and preparation method thereof |
Also Published As
Publication number | Publication date |
---|---|
CN114717028A (en) | 2022-07-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP2343353B1 (en) | Uses of emulsifying agents in non-aqueous fuels and oils | |
CN110129103A (en) | A kind of low-sulfur ordinary diesel oil | |
US2843464A (en) | Non-stalling gasoline fuel compositions | |
EP1349908B1 (en) | A microemulsion fuel containing a hydrocarbon fraction, ethanol, water and an additive comprising a nitrogen-containing surfactnant and a an alcohol | |
CN101024787A (en) | Fuel lubricity additives | |
CN108914132B (en) | Imidazoline corrosion inhibitor for hydrogen sulfide-containing oilfield sewage and preparation method thereof | |
CN113802124A (en) | Corrosion inhibitor for inhibiting corrosion of hydrogen sulfide and application thereof | |
WO2017096680A1 (en) | Environment-friendly antistatic agent for oil product and use method thereof | |
CN108329956B (en) | Environment-friendly gasoline additive and preparation method thereof | |
CN110564463A (en) | gasoline additive | |
CN114717028B (en) | High-stability methanol gasoline and preparation method thereof | |
CN100560801C (en) | Water-soluble high-temperature organic acid corrosion inhibitor and preparation method and use method thereof | |
CN111500328A (en) | Methanol fuel composite additive | |
CN102220170B (en) | Corrosion inhibitor for hydrogenation unit and preparation method thereof | |
CN103695050A (en) | Vehicle methanol gasoline composite additive | |
CN111394141A (en) | Environment-friendly energy-saving automobile detergent and preparation method thereof | |
CN110923024A (en) | High-cleanness methanol diesel oil for vehicles | |
CN101649230A (en) | Metal inhibiter of methanol gasoline | |
CN113430021A (en) | Methanol fuel additive and preparation method thereof | |
CN114350429A (en) | Lubricating oil, preparation method and application thereof | |
CN116043233B (en) | Water-based cleaning agent and preparation method thereof | |
RU2494139C2 (en) | Multifunctional gasoline additive and fuel composition containing said additive | |
CN114032077A (en) | Novel green long-acting fuel cell anti-freezing cooling liquid and preparation method thereof | |
CN110066694A (en) | A kind of clean fuel and preparation method thereof | |
CN112574790A (en) | Gasoline cleaning synergist and preparation method thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
TA01 | Transfer of patent application right |
Effective date of registration: 20230423 Address after: 438300 Low Carbon Industrial Park in Zhongguanyi Town, Macheng City, Huanggang City, Hubei Province (self declared) Applicant after: Hubei Xinyuexing Energy Co.,Ltd. Address before: 438300 Low Carbon Industrial Park, zhongguanyi Town, Macheng City, Huanggang City, Hubei Province Applicant before: Hubei Qinghe New Energy Technology Co.,Ltd. |
|
TA01 | Transfer of patent application right | ||
GR01 | Patent grant | ||
GR01 | Patent grant |