CN114410354A - 一种炼油厂专用汽油动力清净剂及制备方法 - Google Patents
一种炼油厂专用汽油动力清净剂及制备方法 Download PDFInfo
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- CN114410354A CN114410354A CN202210144849.0A CN202210144849A CN114410354A CN 114410354 A CN114410354 A CN 114410354A CN 202210144849 A CN202210144849 A CN 202210144849A CN 114410354 A CN114410354 A CN 114410354A
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- detergent
- parts
- minutes
- power
- dispersant
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- 239000003599 detergent Substances 0.000 title claims abstract description 98
- 239000003502 gasoline Substances 0.000 title claims abstract description 73
- 238000002360 preparation method Methods 0.000 title claims abstract description 19
- 238000002485 combustion reaction Methods 0.000 claims abstract description 82
- 239000002270 dispersing agent Substances 0.000 claims abstract description 76
- 239000003921 oil Substances 0.000 claims abstract description 68
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 39
- 239000001301 oxygen Substances 0.000 claims abstract description 39
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 38
- 230000001360 synchronised effect Effects 0.000 claims abstract description 30
- 239000013556 antirust agent Substances 0.000 claims abstract description 24
- 239000000314 lubricant Substances 0.000 claims abstract description 24
- 239000003963 antioxidant agent Substances 0.000 claims abstract description 17
- 230000003078 antioxidant effect Effects 0.000 claims abstract description 17
- 230000000694 effects Effects 0.000 claims abstract description 16
- 238000004140 cleaning Methods 0.000 claims abstract description 8
- 239000002994 raw material Substances 0.000 claims abstract description 8
- 238000003756 stirring Methods 0.000 claims description 46
- 238000006243 chemical reaction Methods 0.000 claims description 42
- 238000002156 mixing Methods 0.000 claims description 40
- 238000012545 processing Methods 0.000 claims description 30
- 125000004122 cyclic group Chemical group 0.000 claims description 20
- 239000000203 mixture Substances 0.000 claims description 19
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 18
- KZNICNPSHKQLFF-UHFFFAOYSA-N succinimide Chemical compound O=C1CCC(=O)N1 KZNICNPSHKQLFF-UHFFFAOYSA-N 0.000 claims description 16
- CMGDVUCDZOBDNL-UHFFFAOYSA-N 4-methyl-2h-benzotriazole Chemical compound CC1=CC=CC2=NNN=C12 CMGDVUCDZOBDNL-UHFFFAOYSA-N 0.000 claims description 15
- 239000002904 solvent Substances 0.000 claims description 14
- 229920002367 Polyisobutene Polymers 0.000 claims description 10
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 claims description 9
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 claims description 9
- 238000000034 method Methods 0.000 claims description 9
- -1 alkenyl succinate Chemical compound 0.000 claims description 8
- 229960002317 succinimide Drugs 0.000 claims description 8
- 229910021389 graphene Inorganic materials 0.000 claims description 6
- CWQXQMHSOZUFJS-UHFFFAOYSA-N molybdenum disulfide Chemical compound S=[Mo]=S CWQXQMHSOZUFJS-UHFFFAOYSA-N 0.000 claims description 6
- 229910052982 molybdenum disulfide Inorganic materials 0.000 claims description 6
- XZZNDPSIHUTMOC-UHFFFAOYSA-N triphenyl phosphate Chemical compound C=1C=CC=CC=1OP(OC=1C=CC=CC=1)(=O)OC1=CC=CC=C1 XZZNDPSIHUTMOC-UHFFFAOYSA-N 0.000 claims description 6
- 239000007822 coupling agent Substances 0.000 claims description 5
- 150000002191 fatty alcohols Chemical class 0.000 claims description 5
- 150000002195 fatty ethers Chemical class 0.000 claims description 5
- 150000002927 oxygen compounds Chemical class 0.000 claims description 5
- 230000008569 process Effects 0.000 claims description 5
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 2
- 229910052750 molybdenum Inorganic materials 0.000 claims description 2
- 239000011733 molybdenum Substances 0.000 claims description 2
- 239000003112 inhibitor Substances 0.000 claims 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 claims 2
- 238000001556 precipitation Methods 0.000 claims 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract description 28
- 239000000446 fuel Substances 0.000 abstract description 16
- 239000013049 sediment Substances 0.000 abstract description 12
- 230000002035 prolonged effect Effects 0.000 abstract description 5
- 239000000295 fuel oil Substances 0.000 abstract description 2
- 229910052799 carbon Inorganic materials 0.000 description 11
- 239000000126 substance Substances 0.000 description 8
- 239000007789 gas Substances 0.000 description 7
- 230000008021 deposition Effects 0.000 description 6
- 239000000243 solution Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- XYRMLECORMNZEY-UHFFFAOYSA-B [Mo+4].[Mo+4].[Mo+4].[O-]P([O-])([S-])=S.[O-]P([O-])([S-])=S.[O-]P([O-])([S-])=S.[O-]P([O-])([S-])=S Chemical compound [Mo+4].[Mo+4].[Mo+4].[O-]P([O-])([S-])=S.[O-]P([O-])([S-])=S.[O-]P([O-])([S-])=S.[O-]P([O-])([S-])=S XYRMLECORMNZEY-UHFFFAOYSA-B 0.000 description 4
- 150000001412 amines Chemical class 0.000 description 4
- 230000007547 defect Effects 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 230000001376 precipitating effect Effects 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- 238000005303 weighing Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- NLZUEZXRPGMBCV-UHFFFAOYSA-N Butylhydroxytoluene Chemical group CC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 NLZUEZXRPGMBCV-UHFFFAOYSA-N 0.000 description 2
- 239000004721 Polyphenylene oxide Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 235000010354 butylated hydroxytoluene Nutrition 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 238000004945 emulsification Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
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- 229920000570 polyether Polymers 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 230000002195 synergetic effect Effects 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
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- 239000000654 additive Substances 0.000 description 1
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- 150000001336 alkenes Chemical class 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000009194 climbing Effects 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 239000003623 enhancer Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 239000000383 hazardous chemical Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 231100000053 low toxicity Toxicity 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 150000002736 metal compounds Chemical class 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000006213 oxygenation reaction Methods 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical compound C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000003380 propellant Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000002760 rocket fuel Substances 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
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Abstract
本发明涉及清净剂技术领域,为了解决当前燃油在使用中容易形成进气系统沉积物和燃烧室沉积物,导致的发动机性能下降、乙醇汽油燃料热值低、动力差、油耗高等问题,公开了一种炼油厂专用汽油动力清净剂及制备方法,所述一种炼油厂专用汽油动力清净剂,包括以下原料:载体分散剂、高能含氧助燃剂、清净分散剂A、清净分散剂B、清净分散剂C、同步燃烧动力提高剂、防锈剂、节能抗磨润滑剂、抗氧剂、破乳剂。本发明使乙醇汽油续航里程效果大大提升;确保燃烧室内的高清汽油、乙醇汽油能够得到充分燃烧,使得汽油发动机的启动性能得到改善、功率增加、动力性能增强、提高发动机输出功率,延长发动机使用寿命。
Description
技术领域
本发明涉及清净剂技术领域,尤其涉及一种炼油厂专用汽油动力清净剂及制备方法。
背景技术
当前市场上的某些92#、95#汽油、E92#、E95#汽油普遍存在动力不足、油耗量高影响汽车续航里程、并违规使用有机金属化合物类辛烷值改进剂,导致金属在火花塞与燃烧室沉积,使电喷系统判断错误,出现点火时间不正常的问题,或导致发动机积炭增加。因为汽车发动机随着车辆的持续运行,会不知不觉的在发动机内部的节气门、喷油嘴、气缸等部门产生油泥、积碳等影响汽车正常运行的物质。它们慢慢吞噬发动机动力性,降低燃油经济性,增加污染环境的物质排放,并可导致一系列的发动机故。
发明内容
本发明的目的是为了解决现有技术中存在的缺点,而提出的一种炼油厂专用汽油动力清净剂及制备方法。
为了实现上述目的,本发明采用了如下技术方案:
一种炼油厂专用汽油动力清净剂,包括以下重量份的原料:载体分散剂35~55份、高能含氧助燃剂5~10份、清净分散剂A15~25份、清净分散剂B10~20份、清净分散剂C 20~30份、同步燃烧动力提高剂5~15份、防锈剂0.02~0.8份、节能抗磨润滑剂2~5份、抗氧剂0.5~1份、破乳剂0.01~0.05份。
优选的,包括以下重量份的原料:载体分散剂40~50份、高能含氧助燃剂5~10份、清净分散剂A15~20份、清净分散剂B15~20份、清净分散剂C20~25份、同步燃烧动力提高剂6~15份、防锈剂0.05~0.5份、节能抗磨润滑剂3~5份、抗氧剂0.8~1份、破乳剂0.02~0.05份。
优选的,包括以下重量份的原料:载体分散剂40份、高能含氧助燃剂5份、清净分散剂A15份、清净分散剂B10份、清净分散剂C 20份、同步燃烧动力提高剂5份、防锈剂0.48份、节能抗磨润滑剂4份、抗氧剂0.5份、破乳剂0.02份。
优选的,所述的载体分散剂是由D系列溶剂油组成。
优选的,所述的高能含氧助燃剂由具有自供氧性的化合物组成。
优选的,所述的清净分散剂A是聚异丁烯胺;清净分散剂B是聚醚胺;清净分散剂C是聚异丁烯丁二酰亚胺。
优选的,所述同步燃烧动力提高剂为一种分子碳链催化剂。
优选的,所述防锈剂包括由甲基苯并三氮唑与乙二胺、单乙醇胺复配的混合物和烯基丁二酸酯。
优选的,所述抗氧剂为2,6-二叔丁基对甲酚。
优选的,所述破乳剂为AR型破乳剂。
优选的,所述高能含氧助燃剂的制备方法包括以下步骤:将闪点大于60℃的含氧脂肪醇类、醚类化合物与高活性氧化合物加入到反应釜中,常温搅拌过程中加入偶联剂,混合搅拌30~60分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工60~120分钟,得到高能含氧助燃剂。
优选的,所述清净分散剂的制备方法包括以下步骤:将清净分散剂A、清净分散剂、清净分散剂C、D60环保溶剂油加入到反应釜中,常温搅拌混合30~50分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工30~60分钟,得到清净分散剂。
优选的,所述同步燃烧动力提高剂的制备方法包括以下步骤:将同步燃烧动力提高剂与D60环保溶剂油加入到反应釜中,常温搅拌混合40~80分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工60~120分钟,得到同步燃烧动力提高剂。
优选的,所述防锈剂的制备方法包括以下步骤:将甲基苯并三氮唑与乙二胺、单乙醇胺加入到反应釜中,常温搅拌混合30~50分钟,然后加入烯基丁二酸酯,再常温搅拌混合30~50分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工40~60分钟,得到防锈剂。
优选的,所述节能抗磨润滑剂的制备方法包括以下步骤:将二硫化钼、石墨烯、二烷基二硫代磷酸氧钼、甲基苯并三氮唑、聚异丁烯丁二酰亚胺、磷酸三苯酯加入到反应釜中,常温搅拌混合40~70分钟;然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工50~80分钟,得到节能抗磨润滑剂。
上述的一种炼油厂专用汽油动力清净剂的制备方法,包括以下步骤:将高能含氧助燃剂、清净分散剂、同步燃烧动力提高剂、防锈剂和节能抗磨润滑剂,分别加入的反应釜中充分混合搅拌40~60分钟;
再将破乳剂、抗氧剂加入到反应釜中,常温搅拌混合40~60分钟;
然后将反应釜中的混合物加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工60~120分钟,完成对炼油厂专用汽油动力清净剂的制备。
优选的,将制备完成后的炼油厂专用汽油动力清净剂加入静置沉淀48小时后,连接过滤机将沉淀好的炼油厂专用汽油动力清净剂进行过滤。
本发明的有益效果为:
解决了当前燃油在使用中容易形成进气系统沉积物和燃烧室沉积物,导致的发动机性能下降、乙醇汽油燃料热值低、动力差、油耗高等弊病,使乙醇汽油续航里程效果大大提升;确保燃烧室内的高清汽油、乙醇汽油能够得到充分燃烧,使得汽油发动机的启动性能得到改善、功率增加、动力性能增强、提高发动机输出功率,延长发动机使用寿命。
具体实施方式
下面将对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。
本发明为了解决当前燃油在使用中容易形成进气系统沉积物和燃烧室沉积物,导致发动机性能下降,而汽油动力清净剂使用后能在一定程度上控制喷嘴沉积物和进气阀沉积物的形成,杜绝燃烧室沉积物增加的问题。本发明提出了一种炼油厂专用汽油动力清净剂,包括以下重量份的原料:载体分散剂35~55份、高能含氧助燃剂5~10份、清净分散剂A15~25份、清净分散剂B10~20份、清净分散剂C 20~30份、同步燃烧动力提高剂5~15份、防锈剂0.02~0.8份、节能抗磨润滑剂2~5份、抗氧剂0.5~1份、破乳剂0.01~0.05份。
本发明中,载体分散剂是由D系列溶剂油组成。
本发明中,在线式太赫兹超声均质器,就是利用超声波辐射压强产生的强烈空化效应、机械振动、扰动效应、高的加速度、扩散和搅拌作用等多级效应,增大物质分子运动频率和速度,增加溶剂间溶解度,加速化学反应彻底。物料经过12层聚能量筛板及量子材料活化腔,在在线式太赫兹超声均质器的作用下,太赫兹高分子量子能量球形成高频能量波,使添加剂原料分子瞬间被活化,使分子间表面张力减小、粘度下降、溶解性增强,实现物料均匀融合。从而使多种物料之间加速溶解,加速化学反应,形成均匀的混合物。本发明的炼油厂专用汽油动力清净剂闪点大于60℃,不属于危险化学品,具有存储、运输安全系数高等特点。
作为本发明的一种优选实施例,载体分散剂采用D60环保溶剂油,具有溶解能力强,性能稳定,挥发性好,低硫、低芳、低毒、无味的特点,闪点大于60℃具有安全环保的优点。
作为本发明的一种优选实施例,高能含氧助燃剂是具有自供氧性的化合物组成。含高能含氧助燃剂汽油的好处在于蒸发性好,抗爆性提高,辛烷值相对提高,燃烧时积碳相对减少,延长发动机的使用寿命,减少尾气中CO和未燃烃类的含量,汽车燥音小动力明显增加,爬坡有力,无积碳,车速平稳,冷启动快等特点,使其充分燃烧,增大发热量,从而提高了发动机的功率。
作为本发明的一种优选实施例,清净分散剂A是聚异丁烯胺,能有效控制和去除车辆供油系统中,汽车喷油嘴、进气阀和燃烧室里的沉积物和积碳,降低发动机的废气排放和油耗。
作为本发明的一种优选实施例,清净分散剂B是聚醚胺,能清除燃料系统油泥,使喷油嘴雾化效果更好,可清除燃烧室积碳,恢复新车技术参数,更能清除原有发动机燃烧室形成的沉积物,可以抑制燃油系统内部沉淀物的生成,又能将生成的氧化沉淀物迅速分散、清除、进而确保发动机动力正常发挥,延长发动机使用寿命,改善汽油的燃烧性能,降低油耗,减少尾气有害物质的排放,延长汽车续航里程。
作为本发明的一种优选实施例,清净分散剂C是聚异丁烯丁二酰亚胺,具有良好的清净分散性,可抑制发动机活塞上积炭和漆膜的生成。
作为本发明的一种优选实施例,同步燃烧动力提高剂是一种分子碳链催化剂,高能火箭燃料推进剂,其研究法(RON)辛烷值高达140,具有良好的热传递性能,改善汽油的燃烧性能,增强动力、提高热效率,从而达到节能环保的要求,节油效应十分明显,显著减少尾气污染物排放。
作为本发明的一种优选实施例,防锈剂包括由甲基苯并三氮唑与乙二胺、单乙醇胺复配的混合物和烯基丁二酸酯。甲基苯并三氮唑和乙二胺、单乙醇胺复配使用,能产生协同效应,具有良好的油溶性,能在金属表面形成保护膜,防止金属表面腐蚀和锈蚀,与金属形成致密的油膜,是性能优良的防锈剂,可以保护发动机,延长其使用寿命。
作为本发明的一种优选实施例,节能抗磨润滑剂可以减少发动机各部件的摩擦损失,主要是减少活塞环、活塞裙和气缸壁之间摩擦损耗。降低发动机摩擦损失是提高燃油经济性的有效途径之一,明显提高发动机输出功率,延长发动机使用寿命,节能抗磨润滑剂主要由二硫化钼、石墨烯、二烷基二硫代磷酸氧钼、甲基苯并三氮唑、聚异丁烯丁二酰亚胺、磷酸三苯酯等,复配组成的节能抗磨润滑剂。
作为本发明的一种优选实施例,抗氧剂是2,6-二叔丁基对甲酚,在汽油中起到抗氧化的作用,防止汽油中烯烃聚合及氧化而生成弱酸性油泥和积碳,能够与汽油中的活性自由基,发生反应,消耗油中的自由基,阻止油分子自身氧化。
作为本发明的一种优选实施例,破乳剂为AR型破乳剂,由于我们选用的清净剂为表面活性剂,如没有适当破乳剂加入就容易在汽油输送和储存、使用过程中遇水而引起油层乳化及油水界面形成乳化浮渣。乳化浮渣容易导致滤网堵塞,而油层乳化易将水分带入进气系统及燃烧室中造成腐蚀和影响发动机的正常运转。AR型破乳剂分子不大,具有较好的溶解、扩散、渗透效应,能使汽油中的微量水,行成水滴絮凝、聚结在一起,分散出去。
实施例1
称取载体分散剂40份、高能含氧助燃剂5份、清净分散剂A15份、清净分散剂B10份、清净分散剂C 20份、同步燃烧动力提高剂5份、防锈剂0.48份、节能抗磨润滑剂4份、抗氧剂0.5份。破乳剂0.02份;
将闪点大于60℃的含氧脂肪醇类、醚类化合物与高活性氧化合物加入到反应釜中,常温搅拌过程中加入偶联剂,混合搅拌30分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工60分钟,得到高能含氧助燃剂;
将清净分散剂A、清净分散剂、清净分散剂C、D60环保溶剂油加入到反应釜中,常温搅拌混合30分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工30分钟,得到清净分散剂;
将同步燃烧动力提高剂与D60环保溶剂油加入到反应釜中,常温搅拌混合40分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工60分钟,得到同步燃烧动力提高剂;
将甲基苯并三氮唑与乙二胺、单乙醇胺加入到反应釜中,常温搅拌混合30分钟,然后加入烯基丁二酸酯,再常温搅拌混合30分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工40分钟,得到防锈剂;
将二硫化钼、石墨烯、二烷基二硫代磷酸氧钼、甲基苯并三氮唑、聚异丁烯丁二酰亚胺、磷酸三苯酯加入到反应釜中,常温搅拌混合40分钟;然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工50分钟,得到节能抗磨润滑剂;
将高能含氧助燃剂、清净分散剂、同步燃烧动力提高剂、防锈剂和节能抗磨润滑剂,分别加入的反应釜中充分混合搅拌40分钟;再将破乳剂、抗氧剂加入到反应釜中,常温搅拌混合40分钟;然后将反应釜中的混合物加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工60分钟,完成对炼油厂专用汽油动力清净剂的制备,将制备完成后的炼油厂专用汽油动力清净剂加入静置沉淀48小时。
实施例2
称取载体分散剂38份、高能含氧助燃剂7份、清净分散剂A13份、清净分散剂B11份、清净分散剂C15份、同步燃烧动力提高剂10份、防锈剂0.47份、节能抗磨润滑剂5份、抗氧剂0.5份、破乳剂0.03份;
将闪点大于60℃的含氧脂肪醇类、醚类化合物与高活性氧化合物加入到反应釜中,常温搅拌过程中加入偶联剂,混合搅拌45分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工60分钟,得到高能含氧助燃剂;
将清净分散剂A、清净分散剂、清净分散剂C、D60环保溶剂油加入到反应釜中,常温搅拌混合40分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工40分钟,得到清净分散剂;
将同步燃烧动力提高剂与D60环保溶剂油加入到反应釜中,常温搅拌混合50分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工80分钟,得到同步燃烧动力提高剂;
将甲基苯并三氮唑与乙二胺、单乙醇胺加入到反应釜中,常温搅拌混合30分钟,然后加入烯基丁二酸酯,再常温搅拌混合30分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工50分钟,得到防锈剂;
将二硫化钼、石墨烯、二烷基二硫代磷酸氧钼、甲基苯并三氮唑、聚异丁烯丁二酰亚胺、磷酸三苯酯加入到反应釜中,常温搅拌混合50分钟;然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工60分钟,得到节能抗磨润滑剂;
将高能含氧助燃剂、清净分散剂、同步燃烧动力提高剂、防锈剂和节能抗磨润滑剂,分别加入的反应釜中充分混合搅拌40分钟;再将破乳剂、抗氧剂加入到反应釜中,常温搅拌混合40分钟;然后将反应釜中的混合物加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工80分钟,完成对炼油厂专用汽油动力清净剂的制备,将制备完成后的炼油厂专用汽油动力清净剂加入静置沉淀48小时。
实施例3
称取载体分散剂45份、高能含氧助燃剂6份、清净分散剂A10份、清净分散剂B10份、清净分散剂C15份、同步燃烧动力提高剂7份、防锈剂0.56份、节能抗磨润滑剂6份、抗氧剂0.4份。破乳剂0.04份;
将闪点大于60℃的含氧脂肪醇类、醚类化合物与高活性氧化合物加入到反应釜中,常温搅拌过程中加入偶联剂,混合搅拌50分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工90分钟,得到高能含氧助燃剂;
将清净分散剂A、清净分散剂、清净分散剂C、D60环保溶剂油加入到反应釜中,常温搅拌混合50分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工60分钟,得到清净分散剂;
将同步燃烧动力提高剂与D60环保溶剂油加入到反应釜中,常温搅拌混合60分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工90分钟,得到同步燃烧动力提高剂;
将甲基苯并三氮唑与乙二胺、单乙醇胺加入到反应釜中,常温搅拌混合45分钟,然后加入烯基丁二酸酯,再常温搅拌混合40分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工50分钟,得到防锈剂;
将二硫化钼、石墨烯、二烷基二硫代磷酸氧钼、甲基苯并三氮唑、聚异丁烯丁二酰亚胺、磷酸三苯酯加入到反应釜中,常温搅拌混合60分钟;然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工80分钟,得到节能抗磨润滑剂;
将高能含氧助燃剂、清净分散剂、同步燃烧动力提高剂、防锈剂和节能抗磨润滑剂,分别加入的反应釜中充分混合搅拌50分钟;再将破乳剂、抗氧剂加入到反应釜中,常温搅拌混合50分钟;然后将反应釜中的混合物加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工100分钟,完成对炼油厂专用汽油动力清净剂的制备,将制备完成后的炼油厂专用汽油动力清净剂加入静置沉淀48小时。
本发明利用三种不同功效的清净剂、高能含氧助燃剂、同步燃烧动力提高剂及多种化学物质制成的炼油厂专用汽油动力清净剂,利用多种化学物质的协同作用在高清汽油、乙醇汽油燃油中添加后,能控制和清除喷嘴沉积物和进气阀沉积物的形成,更能清除原有发动机燃烧室形成的沉积物,可以抑制燃油系统内部沉淀物的生成,又能将生成的氧化沉淀物迅速分散、清除、进而确保发动机动力正常发挥,延长发动机使用寿命。特别添加了高能含氧助燃剂,能降低燃料燃点,提高火焰强度、增加能量释放。高能含氧助燃剂气体中氧含量增高以及氮含量下降强化了燃烧过程,可以显著提高燃烧过程的热量利用率。从而提高燃烧效率,既能提高燃烧效率,节约能源,又能减少有害气体排放,保护环境,具有明显的节油效果。并可提高高清汽油、乙醇汽油中的含氧量,能有效增加发动机的氧气供应量,对发动机进行有氧补偿。改善汽油的燃烧性能,还能改善汽油在发动机中的燃烧状况,确保燃烧室内的燃油能够得到充分燃烧,提高了高清汽油、乙醇汽油的燃烧效率,大幅度提高热效率,改善汽油发动机的启动性能、提高汽车动力性能,车辆的行驶效率和安全状况,从而使发动机处于良好的工况,减少了发动机各部件的摩擦损失,提高发动机输出功率,延长发动机使用寿命,降低故障率,降低了保养维护的费用。提高了高清汽油、乙醇汽油释放能量利用率,大大节省高清汽油、乙醇汽油的消耗量,增加汽车的机动性能。降低油耗,减少尾气有害物质的排放,延长汽车续航里程。
本发明的目的在于提供一种炼油厂专用汽油动力清净剂,众所周知,油品质量的优劣不仅影响到用油量的多少,还直接影响到发动机的使用寿命。本发明创新采用炼油厂专用汽油动力清净剂,为高清汽油、乙醇汽油提供了高性价比、高体积能量密度、自供氧、使燃油充分燃烧、动力明显增强、噪音、积碳、烟度显著降低、节能率大步提升、冷起动能力增加、CO、NOX、HC等有害物质明显减少的环保和安全的高能高清汽油、乙醇汽油燃料。使其含有炼油厂专用汽油动力清净剂的燃油品质分子结构优化,燃烧更充分,动力性更强,燃料更节省,解决了乙醇汽油燃料热值低、动力差、油耗高等弊病,使乙醇汽油续航里程达到完美的效果。可以使发动输出功率提高30%以上。道路试验:节油8-15%,减少尾气污染物排放下降45%。达到发动机养护、清理积碳、提升动力三合一功能。
以上所述,仅为本发明较佳的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,根据本发明的技术方案及其发明构思加以等同替换或改变,都应涵盖在本发明的保护范围之内。
Claims (10)
1.一种炼油厂专用汽油动力清净剂,其特征在于,包括以下重量份的原料:载体分散剂35~55份、高能含氧助燃剂5~10份、清净分散剂A15~25份、清净分散剂B10~20份、清净分散剂C 20~30份、同步燃烧动力提高剂5~15份、防锈剂0.02~0.8份、节能抗磨润滑剂2~5份、抗氧剂0.5~1份、破乳剂0.01~0.05份。
2.根据权利要求1所述的一种炼油厂专用汽油动力清净剂,其特征在于,包括以下重量份的原料:载体分散剂40~50份、高能含氧助燃剂5~10份、清净分散剂A15~20份、清净分散剂B15~20份、清净分散剂C20~25份、同步燃烧动力提高剂6~15份、防锈剂0.05~0.5份、节能抗磨润滑剂3~5份、抗氧剂0.8~1份、破乳剂0.02~0.05份。
3.根据权利要求1所述的一种炼油厂专用汽油动力清净剂,其特征在于,所述防锈剂包括由甲基苯并三氮唑与乙二胺、单乙醇胺复配的混合物和烯基丁二酸酯。
4.根据权利要求1所述的一种炼油厂专用汽油动力清净剂,其特征在于,所述高能含氧助燃剂的制备方法包括以下步骤:将闪点大于60℃的含氧脂肪醇类、醚类化合物与高活性氧化合物加入到反应釜中,常温搅拌过程中加入偶联剂,混合搅拌30~60分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工60~120分钟,得到高能含氧助燃剂。
5.根据权利要求1所述的一种炼油厂专用汽油动力清净剂,其特征在于,所述清净分散剂的制备方法包括以下步骤:将清净分散剂A、清净分散剂、清净分散剂C、D60环保溶剂油加入到反应釜中,常温搅拌混合30~50分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工30~60分钟,得到清净分散剂。
6.根据权利要求1所述的一种炼油厂专用汽油动力清净剂,其特征在于,所述同步燃烧动力提高剂的制备方法包括以下步骤:将同步燃烧动力提高剂与D60环保溶剂油加入到反应釜中,常温搅拌混合40~80分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工60~120分钟,得到同步燃烧动力提高剂。
7.根据权利要求1所述的一种炼油厂专用汽油动力清净剂,其特征在于,所述防锈剂的制备方法包括以下步骤:将甲基苯并三氮唑与乙二胺、单乙醇胺加入到反应釜中,常温搅拌混合30~50分钟,然后加入烯基丁二酸酯,再常温搅拌混合30~50分钟,然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工40~60分钟,得到防锈剂。
8.根据权利要求1所述的一种炼油厂专用汽油动力清净剂,其特征在于,所述节能抗磨润滑剂的制备方法包括以下步骤:将二硫化钼、石墨烯、二烷基二硫代磷酸氧钼、甲基苯并三氮唑、聚异丁烯丁二酰亚胺、磷酸三苯酯加入到反应釜中,常温搅拌混合40~70分钟;然后加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工50~80分钟,得到节能抗磨润滑剂。
9.如权利要求1-8任一所述的一种炼油厂专用汽油动力清净剂的制备方法,其特征在于,包括以下步骤:将高能含氧助燃剂、清净分散剂、同步燃烧动力提高剂、防锈剂和节能抗磨润滑剂,分别加入的反应釜中充分混合搅拌40~60分钟;
再将破乳剂、抗氧剂加入到反应釜中,常温搅拌混合40~60分钟;
然后将反应釜中的混合物加入到在线式太赫兹超声均质器中,开启电子设备在线循环加工60~120分钟,完成对炼油厂专用汽油动力清净剂的制备。
10.根据权利要求9所述的一种炼油厂专用汽油动力清净剂的制备方法,其特征在于,将制备完成后的炼油厂专用汽油动力清净剂加入静置沉淀48小时后,连接过滤机将沉淀好的炼油厂专用汽油动力清净剂进行过滤。
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