CN105733709A - 一种环保燃油添加剂的制备方法 - Google Patents
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Abstract
本发明公开了一种环保燃油添加剂的制备方法,包括以下步骤:按重量份计,将4~23份正丁醇、2~10份三乙醇胺、6~17份邻苯二甲酸二辛酯、48~62份碳酸二甲酯、15~28份聚异丁烯胺加入反应釜中,搅拌均匀,得到混合物一;将反应釜中的温度加热至40~55℃,向混合物一中加入2~15份甲基叔丁醚、3~9份硝酸铜,超声后降温,再加入2~16份二羟甲基丁酸和5~19份甲基丙烯酸羟丙酯,搅拌均匀,保温后冷却至室温,得到混合物二;将混合物二沉降后过滤灌装,即得。本发明制得的燃油添加剂通过组分之间达到减少污染物排放量和提高节油率的效果,具有良好的市场应用前景。
Description
技术领域
本发明涉及一种燃油添加剂,特别涉及一种环保燃油添加剂的制备方法。
背景技术
发动机在运行过程中,内部会产生积碳,会慢慢吞噬发动机动力,降低燃油经济性,恶化排放,以及导致一系列的发动机故障,燃油添加剂可清除积碳,提升动力,节省燃油,降低噪音,防止燃油导致的发动机故障。
申请号为CN201410003212.5的中国发明专利,公开了一种燃油添加剂,包含C12~C18异构饱和脂肪酸作为乳化剂、用于与所述脂肪酸形成盐的中和剂和任选的稀释剂。申请号为201210102171.6的中国发明专利,公开了一种纳米燃油添加剂及其制备方法,包括如下重量百分比的原料:脂肪酸25~35%、脂肪醚20~30%、乳化剂司盘系列15~25%、水10~20%、一元醇4~8%、脂肪胺或醇胺6~12%。制备步骤包括依次按重量比例先后将脂肪酸、脂肪醚、乳化剂司盘系列、水、一元醇和脂肪胺加入反应装置内,控制温度在常温、常压下机械搅拌4~6小时,直至出现均匀稳定的混合溶液后,得到所述纳米燃油添加剂。以上方法制得的燃油添加剂在使用过程中会产生一氧化碳、二氧化硫、碳氢化合物及
发明内容
本发明解决的技术问题是,提供一种环保燃油添加剂的制备方法,制得的燃油添加剂通过组分之间达到减少污染物排放量和提高节油率的效果,具有良好的市场应用前景。
本发明采用的技术方案是:
一种环保燃油添加剂的制备方法,包括以下步骤:
(1)按重量份计,将4~23份正丁醇、2~10份三乙醇胺、6~17份邻苯二甲酸二辛酯、48~62份碳酸二甲酯、15~28份聚异丁烯胺加入反应釜中,搅拌均匀,得到混合物一;
(2)将反应釜中的温度加热至40~55℃,向步骤(1)所得混合物一中加入2~15份甲基叔丁醚、3~9份硝酸铜,超声后降温至30~40℃,再加入2~16份二羟甲基丁酸和5~19份甲基丙烯酸羟丙酯,搅拌均匀,保温后冷却至室温,得到混合物二;
(3)将步骤(2)所得混合物二沉降后过滤灌装,即得所述环保燃油添加剂。
优选的,上述步骤(1)中正丁醇、三乙醇胺、邻苯二甲酸二辛酯、碳酸二甲酯和聚异丁烯胺在30~40min内加完。
优选的,上述步骤(1)中搅拌速率为500~800r/min。
优选的,上述步骤(2)中超声时间为10~20min。
优选的,上述步骤(2)中搅拌速率为400~800r/min。
优选的,上述步骤(2)中保温时间为20~40min。
优选的,上述步骤(3)中沉降时间为1~4h。
有益效果:本发明制得的燃油添加剂污染物排放量减少率在58~79%之间,节油率在15.7~16.8%之间;对比例1中未添加二羟甲基丁酸,制得的燃油添加剂污染物排放量减少率为55%,节油率为12.9%;对比例2中未添加甲基丙烯酸羟丙酯,制得的燃油添加剂污染物排放量减少率为42%,节油率为15.8%。由此可知,本发明制得的燃油添加剂通过组分之间达到减少污染物排放量效果,同时能够提高节油率,具有良好的市场应用前景。
具体实施方式
实施例1
一种环保燃油添加剂的制备方法,包括以下步骤:
(1)按重量份计,将4份正丁醇、2份三乙醇胺、6份邻苯二甲酸二辛酯、48份碳酸二甲酯、15份聚异丁烯胺在30min内加入反应釜中,500r/min速率下搅拌均匀,得到混合物一;
(2)将反应釜中的温度加热至40℃,向步骤(1)所得混合物一中加入2份甲基叔丁醚、3份硝酸铜,超声10min后降温至30℃,再加入2份二羟甲基丁酸和5份甲基丙烯酸羟丙酯,400r/min速率下搅拌均匀,保温20min后冷却至室温,得到混合物二;
(3)将步骤(2)所得混合物二沉降1h后过滤灌装,即得所述环保燃油添加剂。
实施例2
一种环保燃油添加剂的制备方法,包括以下步骤:
(1)按重量份计,将23份正丁醇、10份三乙醇胺、17份邻苯二甲酸二辛酯、62份碳酸二甲酯、28份聚异丁烯胺在40min内加入反应釜中,800r/min速率下搅拌均匀,得到混合物一;
(2)将反应釜中的温度加热至55℃,向步骤(1)所得混合物一中加入15份甲基叔丁醚、9份硝酸铜,超声20min后降温至40℃,再加入16份二羟甲基丁酸和19份甲基丙烯酸羟丙酯,800r/min速率下搅拌均匀,保温40min后冷却至室温,得到混合物二;
(3)将步骤(2)所得混合物二沉降4h后过滤灌装,即得所述环保燃油添加剂。
实施例3
一种环保燃油添加剂的制备方法,包括以下步骤:
(1)按重量份计,将7份正丁醇、3份三乙醇胺、9份邻苯二甲酸二辛酯、51份碳酸二甲酯、17份聚异丁烯胺在35min内加入反应釜中,600r/min速率下搅拌均匀,得到混合物一;
(2)将反应釜中的温度加热至45℃,向步骤(1)所得混合物一中加入4份甲基叔丁醚、4份硝酸铜,超声15min后降温至35℃,再加入4份二羟甲基丁酸和7份甲基丙烯酸羟丙酯,500r/min速率下搅拌均匀,保温5min后冷却至室温,得到混合物二;
(3)将步骤(2)所得混合物二沉降1.5h后过滤灌装,即得所述环保燃油添加剂。
实施例4
一种环保燃油添加剂的制备方法,包括以下步骤:
(1)按重量份计,将21份正丁醇、9份三乙醇胺、15份邻苯二甲酸二辛酯、58份碳酸二甲酯、25份聚异丁烯胺在35min内加入反应釜中,700r/min速率下搅拌均匀,得到混合物一;
(2)将反应釜中的温度加热至50℃,向步骤(1)所得混合物一中加入12份甲基叔丁醚、8份硝酸铜,超声15min后降温至35℃,再加入13份二羟甲基丁酸和15份甲基丙烯酸羟丙酯,700r/min速率下搅拌均匀,保温35min后冷却至室温,得到混合物二;
(3)将步骤(2)所得混合物二沉降3.5h后过滤灌装,即得所述环保燃油添加剂。
实施例5
一种环保燃油添加剂的制备方法,包括以下步骤:
(1)按重量份计,将15份正丁醇、6份三乙醇胺、12份邻苯二甲酸二辛酯、56份碳酸二甲酯、24份聚异丁烯胺在35min内加入反应釜中,600r/min速率下搅拌均匀,得到混合物一;
(2)将反应釜中的温度加热至50℃,向步骤(1)所得混合物一中加入11份甲基叔丁醚、6份硝酸铜,超声15min后降温至35℃,再加入14份二羟甲基丁酸和15份甲基丙烯酸羟丙酯,600r/min速率下搅拌均匀,保温60min后冷却至室温,得到混合物二;
(3)将步骤(2)所得混合物二沉降3h后过滤灌装,即得所述环保燃油添加剂。
对比例1
与实施例5的区别未添加二羟甲基丁酸。
一种环保燃油添加剂的制备方法,包括以下步骤:
(1)按重量份计,将15份正丁醇、6份三乙醇胺、12份邻苯二甲酸二辛酯、56份碳酸二甲酯、24份聚异丁烯胺在35min内加入反应釜中,600r/min速率下搅拌均匀,得到混合物一;
(2)将反应釜中的温度加热至50℃,向步骤(1)所得混合物一中加入11份甲基叔丁醚、6份硝酸铜,超声15min后降温至35℃,再加入15份甲基丙烯酸羟丙酯,600r/min速率下搅拌均匀,保温60min后冷却至室温,得到混合物二;
(3)将步骤(2)所得混合物二沉降3h后过滤灌装,即得所述环保燃油添加剂。
对比例2
与实施例5的区别是未添加甲基丙烯酸羟丙酯。
一种环保燃油添加剂的制备方法,包括以下步骤:
(1)按重量份计,将15份正丁醇、6份三乙醇胺、12份邻苯二甲酸二辛酯、56份碳酸二甲酯、24份聚异丁烯胺在35min内加入反应釜中,600r/min速率下搅拌均匀,得到混合物一;
(2)将反应釜中的温度加热至50℃,向步骤(1)所得混合物一中加入11份甲基叔丁醚、6份硝酸铜,超声15min后降温至35℃,再加入14份二羟甲基丁酸,600r/min速率下搅拌均匀,保温60min后冷却至室温,得到混合物二;
(3)将步骤(2)所得混合物二沉降3h后过滤灌装,即得所述环保燃油添加剂。
性能测试:
将实施例1~5和对比例1~2所得的燃油添加剂与汽油、柴油1:1000(体积比)加入轿车中正常行驶5000km后,对节油率和污染物排放量减少率进行测试;结果如下表:
其中污染物为一氧化碳、二氧化硫、碳氢化合物及氮氧化合物。
从上表中可以看出:实施例1~5制得的燃油添加剂污染物排放量减少率在58~79%之间,节油率在15.7~16.8%之间;对比例1中未添加二羟甲基丁酸,制得的燃油添加剂污染物排放量减少率为55%,节油率为12.9%;对比例2中未添加甲基丙烯酸羟丙酯,制得的燃油添加剂污染物排放量减少率为42%,节油率为15.8%。由此可知,本发明制得的燃油添加剂通过组分之间达到减少污染物排放量和提高节油率的效果,具有良好的市场应用前景。
Claims (7)
1.一种环保燃油添加剂的制备方法,其特征在于,包括以下步骤:
(1)按重量份计,将4~23份正丁醇、2~10份三乙醇胺、6~17份邻苯二甲酸二辛酯、48~62份碳酸二甲酯、15~28份聚异丁烯胺加入反应釜中,搅拌均匀,得到混合物一;
(2)将反应釜中的温度加热至40~55℃,向步骤(1)所得混合物一中加入2~15份甲基叔丁醚、3~9份硝酸铜,超声后降温至30~40℃,再加入2~16份二羟甲基丁酸和5~19份甲基丙烯酸羟丙酯,搅拌均匀,保温后冷却至室温,得到混合物二;
(3)将步骤(2)所得混合物二沉降后过滤灌装,即得所述环保燃油添加剂。
2.根据权利要求1所述的环保燃油添加剂的制备方法,其特征在于:所述步骤(1)中正丁醇、三乙醇胺、邻苯二甲酸二辛酯、碳酸二甲酯和聚异丁烯胺在30~40min内加完。
3.根据权利要求1所述的环保燃油添加剂的制备方法,其特征在于:所述步骤(1)中搅拌速率为500~800r/min。
4.根据权利要求1所述的环保燃油添加剂的制备方法,其特征在于:所述步骤(2)中超声时间为10~20min。
5.根据权利要求1所述的环保燃油添加剂的制备方法,其特征在于:所述步骤(2)中搅拌速率为400~800r/min。
6.根据权利要求1所述的环保燃油添加剂的制备方法,其特征在于:所述步骤(2)中保温时间为20~40min。
7.根据权利要求1所述的环保燃油添加剂的制备方法,其特征在于:所述步骤(3)中沉降时间为1~4h。
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101724474A (zh) * | 2008-10-14 | 2010-06-09 | 陈若歆 | M15~m100络合甲醇汽油制造模式与气体常温液化掺烧技术 |
CN101935563A (zh) * | 2009-06-29 | 2011-01-05 | 姚吉有 | 重柴油节能剂 |
CN104059713A (zh) * | 2014-06-28 | 2014-09-24 | 青岛乾祥环保技术有限公司 | 一种绿色节煤材料 |
CN104263432A (zh) * | 2014-09-16 | 2015-01-07 | 青岛市高科专利技术转移平台有限公司 | 一种低毒燃烧助剂 |
-
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Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101724474A (zh) * | 2008-10-14 | 2010-06-09 | 陈若歆 | M15~m100络合甲醇汽油制造模式与气体常温液化掺烧技术 |
CN101935563A (zh) * | 2009-06-29 | 2011-01-05 | 姚吉有 | 重柴油节能剂 |
CN104059713A (zh) * | 2014-06-28 | 2014-09-24 | 青岛乾祥环保技术有限公司 | 一种绿色节煤材料 |
CN104263432A (zh) * | 2014-09-16 | 2015-01-07 | 青岛市高科专利技术转移平台有限公司 | 一种低毒燃烧助剂 |
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