CN111925841A - 使用植物油制造生物乳化燃料的设备和方法 - Google Patents
使用植物油制造生物乳化燃料的设备和方法 Download PDFInfo
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- CN111925841A CN111925841A CN201911327084.9A CN201911327084A CN111925841A CN 111925841 A CN111925841 A CN 111925841A CN 201911327084 A CN201911327084 A CN 201911327084A CN 111925841 A CN111925841 A CN 111925841A
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- oil
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- tank
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- -1 housestone Chemical compound 0.000 claims description 9
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- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 6
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- 239000011777 magnesium Substances 0.000 claims description 6
- 239000000395 magnesium oxide Substances 0.000 claims description 6
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- 238000005259 measurement Methods 0.000 claims description 4
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- 230000000694 effects Effects 0.000 description 6
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- 238000005984 hydrogenation reaction Methods 0.000 description 1
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- 229910052744 lithium Inorganic materials 0.000 description 1
- 230000033116 oxidation-reduction process Effects 0.000 description 1
- 150000002926 oxygen Chemical class 0.000 description 1
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Abstract
提供了一种使用植物油的生物乳化燃料制造设备和方法,该设备包括:油箱单元,其被配置为通过使用凝结剂和离心倾析器来精炼从油入口引入的植物油;水箱单元,其被配置为通过使用水箱催化剂来预处理从水入口引入的水;混合油单元,其连接至油箱单元和水箱单元,并且被配置为通过使用列式混合器来产生混合油;以及电离催化剂单元,其连接至混合油单元,并且被配置为通过使用电离催化剂组将混合油转化为生物乳化燃料。
Description
技术领域
本文描述的各种实施方式总体上涉及一种使用植物油制造生物乳化燃料的设备和方法。
背景技术
近年来,化石燃料的耗尽和温室气体的产生已经成为全球性问题。
为了解决这些问题,由本发明人提交的韩国专利101328151号(标题为“燃料制造方法”)描述了一种用于制造能被雾化并展示出高适用性和高稳定性的乳化燃料的方法和设备。在该方法和设备中,将水和诸如柴油、煤油或重油之类的油燃料供应到施加有磁场的空间内。在该空间中,水和油燃料被雾化并彼此混合,使得产生乳化燃料。
然而,在此类常规燃料制造方法和设备中,由于燃料呈乳状剂形式,因此可以发生水-油分离并且可以留下水成分。结果,闪点将大大增加,而热值将降低,从而导致无法大大减少化石燃料的消耗。
为了试图解决该问题,本发明人提交了韩国专利101581235号(标题为“用于制造重整燃料的设备及其制造方法”)。在该方法和设备中,通过向水箱施加超声波或电场使水雾化,并且通过从酶箱供应酶来分解过氧化氢。因此,允许水和油容易地彼此混合而不分离。因此,可以抑制呈乳状剂形式的重整燃料的上述问题,诸如闪点的增加和热值的降低。
然而,这种用于制造重整燃料的常规设备和方法涉及复杂的工艺,并且难以管理酶箱中的酶。此外,由于设备具有适于施加超声波和电场的复杂结构,所以制造成本高并且不容易修理和维护该设备。
另外,在生产和销售实际系统的过程中,存在一个现实的问题,即难以制造与每个国家添加到燃料中的不同添加剂相对应的催化剂。
发明内容
鉴于前述问题,示例实施例提供了一种使用植物油而不是使用包含在每个国家的不同添加剂的化石燃料来制造生物乳化燃料的设备和方法。
根据说明性实施例的第一方面,提供了一种生物乳化燃料制造设备,其包括油箱单元,其被配置为通过使用凝结剂和离心倾析器来精炼从油入口引入的植物油;水箱单元,其被配置为通过使用水箱催化剂来预处理从水入口引入的水;混合油单元,其连接至油箱单元和水箱单元,并且被配置为通过使用列式混合器来产生混合油;以及电离催化剂单元,其连接至混合油单元,并且被配置为通过使用电离催化剂组将混合油转化为生物乳化燃料。
根据说明性实施例的第二方面,提供了一种生物乳化燃料制造方法,该方法包括:通过使用凝结剂使植物油中的杂质固化并由离心倾析器分离出固化的杂质来制备精炼油;通过使用水箱催化剂对水箱中供应的水进行预处理来制备预处理水;通过使从油箱引入的精炼油和从水箱引入的预处理水穿过列式混合器来产生混合油;以及在电离催化剂单元中,通过使用电离催化剂组将从混合油箱引入的混合油转化为生物乳化燃料。
根据本发明的上述问题解决方法,使用植物油的生物乳化燃料在燃烧中产生的热量高于通过常规化石燃料的乳化燃料的热量。
此外,使用植物油的生物乳化燃料由于其乳化燃料的特性而具有减少的污染物排放。
与使用化石燃料的乳化燃料相比,通过确保充足的植物油供应源,使用植物油的生物乳化燃料具有显著降低生产成本的优点。
附图说明
在下面的详细描述中,由于各种变化和修改将从以下详细描述中变得显而易见,因此实施例仅作为示例说明而描述。在不同附图中使用相同的附图标记表示相似或相同的零件。
图1是根据示例实施例的生物乳化燃料制造设备的工艺流程图,以说明如何通过本发明生产生物乳化燃料。图1分为图1(a)、图1(b)和图1(c)来显示详细实体。
图2是根据示例实施例的油箱的示意性侧视图;
图3是根据示例实施例的水箱的示意性侧视图;
图4是根据示例实施例的混合油箱的示意性侧视图;
图5是根据示例实施例的电离催化剂单元的示意性侧视图;以及
图6是用于描述根据示例实施例的生物乳化燃料制造方法的流程图。
具体实施方式
在下文中,将详细描述示例实施例,使得本领域技术人员可以容易地实现发明构思。然而,应注意,本公开不限于说明性实施例和示例,而是可以以各种其他方式实现。在附图中,省略了与描述不直接相关的部件以提高附图的清楚性,并且贯穿全文相同的附图标记表示相同的部件。
贯穿全文,用来表明一个元件相对于另一个元件的位置的术语“在……上”既包括一个元件与另一元件相邻的情况,也包括在这两个元件之间存在任何其他元件的情况。
贯穿全文,在文件中使用的术语“包括(comprises)或包括(includes)”和/或“包括(comprising)或包括(including)”是指除了所描述的部件、步骤、操作和/或元件之外,并不排除一个或多个其他部件、步骤、操作和/或元件的存在或添加,除非上下文另行指明。术语“大约或近似”或“基本上”旨在具有以可容许误差接近于指定的数值或范围的意义,并且旨在防止为了理解本公开所公开的精确或绝对数值被任何不合理的第三方非法地或不公平地使用。贯穿全文,术语“……的步骤”并不表示“用于……的步骤”。
在下文中,将会参照附图详细地描述示例实施例,该附图形成该实施例的一部分。
首先,将详细阐述根据示例实施例的生物乳化燃料制造设备10(在下文中称为“本生物乳化燃料制造设备10”)。
参照图1(a)、图1(b)和图1(c),将说明本生物乳化燃料制造设备10的构造。
如图1所示,本生物乳化燃料制造设备10包括油箱单元100、水箱单元200、混合油单元300和电离催化剂单元400。
可以通过供油泵110向油箱单元100供应植物油。所提供的油临时储存在油箱120中。由供应商提供的油本身通常在其中包含多种杂质,这些杂质会在燃烧过程中降低发动机或发电机的性能。为了消除油中包含的杂质,油箱单元100可以包括凝结剂供给装置130,该凝结剂供给装置130被配置为将凝结剂提供到油箱120中,然后凝结剂使油中的杂质固化。油箱120内的油通过输油泵140被输送到离心倾析器150。离心倾析器150内部高速旋转,以在油上产生离心力,从而从油中分离出固化的杂质。由离心倾析器150产生的精炼油被临时传送并储存在集油箱160中,然后通过精炼油输送泵180输送到精炼油箱170中。
水箱单元200被配置为通过使用水箱催化剂来预处理引入其中的水。可以从供水泵210向水箱单元200供应水。
混合油单元300连接到油箱单元100和水箱单元200。混合油单元300产生混合油,该混合油单元300被配置为通过使用列式混合器360将从油箱单元100输送的精炼油与来自水箱单元200的预处理水进行物理混合。
更具体地,将精炼油箱170内的精炼油通过高压油泵310输送至列式混合器360。此外,同时通过高压水泵320将水箱220内的预处理水输送至列式混合器360。箱170、220与列式混合器360之间的每条管道包括控制阀330a、330b,控制阀330a、330b被配置为分别控制进入列式混合器360的油和水的量。精炼油与预处理水的混合比通过调节控制阀330a、330b来确定。精炼油和预处理水之间的优选比通常设置为1:1,但根据操作条件可以为6:4或7:3。另外,箱170、220与列式混合器360之间的每条管道还包括压力计340a、340b和流量计350a、350b,以监测进入列式混合器360中的每种精炼油和预处理水的压力和流量。来自压力计340a、340b和流量计350a、350b的数据被发送到主控制器(图中未示出),从而以精确的方式自动调节比率。
由列式混合器360物理混合的混合油被输送到混合油箱370并暂时储存在那儿。
电离催化剂单元400连接到混合油单元300。电离催化剂单元400被配置为通过使用电离催化剂组从混合油中产生生物乳化燃料作为最终产品。
参照图2,将更详细地说明根据示例实施例的油箱120。
油箱120包括油入口管线121、油加热器122、油位测量器123、通气孔124、油搅拌器125和油出口管线126。
油入口管线121通过供油泵110将油从外部递送到油箱120中。
设置油加热器122,以维持由凝结剂供给装置130供给的凝结剂的理想温度,从而有效地固化油内的杂质。作为非限制性示例,油箱120内的理想温度可以是例如大约50°C。
油位测量器123被配置为测量油箱120内的油位。
由油位测量器123获得的油位信息可以发送到主控制器(未示出)。主控制器通过检查油位信息并控制供油泵110的操作来调节油箱120内的油位。
设置通气孔124以防止油箱120内的压力升高。通气孔124可以由导管来实现,通过该导管油箱内的空气被排尽。
油搅拌器125被配置为搅拌油箱120内的油。举例来说,油搅拌器125可以是油搅拌马达,其可以安装在油箱120的上部中央部分。当油箱120内的油被油搅拌器125搅拌时,整个油的温度分布被恒定地保持。
油出口管线126将包含通过凝结剂固化的杂质的油输送到离心倾析器150中。例如,可以通过设置在油箱120下部的油出口控制阀127将油输送到油出口管线126中。
油的预处理的完成可以由主控制器确定。此外,主控制器还可以控制油出口控制阀127的打开和关闭。
参照图3,将详细说明根据示例实施例的水箱220。
水箱220包括水入口管线221、水位测量器222、水箱催化剂筒223、水搅拌器224和水出口管线225。
水入口管线210通过供水泵210将水从外部输送到水箱220中。
水位测量器222被配置为测量水量,即,水箱220内的水位。
由水位测量器222获得的水位信息可以发送到主控制器。主控制器通过检查水位信息并控制供水泵210的操作来调节水箱220内的水位。
水箱催化剂筒223在其中储存水箱催化剂。使水箱催化剂与水接触,从而进行水的预处理。举例来说,水箱催化剂筒223可以设置在水箱220内的中央部分,例如下部中央部分处。
这里,水箱催化剂可以包括第一水箱催化剂,其包含电气石矿物,诸如电气石原石;以及第二水箱催化剂,其包含二氧化硅、硅酸盐矿物和卤素矿物中的至少一种。
举例来说,第二水箱催化剂可以是包含二氧化硅、硅酸盐矿物和卤素矿物的球形催化剂,其直径为但不限于约1 cm。
水箱单元100内的水可以通过第一水箱催化剂和第二水箱催化剂变成氢水,并且还可以消除在水中溶解的氧。
更具体地说,电气石矿物具有压电效应和热电效应。电气石矿物还具有作为吸附偏光器的效应、电磁辐射效应、远红外线效应、电离效应等。当将电气石矿物放入水中时就开始放射电磁波。当电气石矿物与水分子接触时,可以放松水分子的耦合。如上所述,通过水箱催化剂与水箱单元100中的水之间的接触来产生预处理水。预处理水的pH可以为约7.5,并且ORP(氧化-还原电位)可以维持在大约90到大约100。
水搅拌器224被配置为搅拌水箱220内的水。作为非限制性示例,水搅拌器224可以是水搅拌马达,其安装在水箱220的上部中央部分处。当水被水搅拌器224搅拌时,可以增强水和水箱催化剂之间的接触。
水出口管线225将预处理水递送到稍后将描述的混合油单元300中。例如,预处理水可以通过设置在水箱220下部处的水出口控制阀226输送到水出口管线225中。
水的预处理的完成可以由主控制器确定。此外,主控制器还可以控制水出口控制阀226的打开和关闭。
参照图1(b),将更详细地说明将精炼油和预处理水输送到混合油单元300中的过程以及将精炼油和预处理水混合的过程。
通过倾析器150产生的精炼油通过精炼油泵180输送并暂时储存到精炼油箱170中。然后,精炼油箱170中的精炼油通过高压油泵310以加压方式输送到列式混合器360中。精炼油的量由控制阀330a确定。精炼油穿过压力计340a和流量计350a,所述压力计340a和流量计350a沿着管道管线安装在精炼油箱170和列式混合器360之间。
水箱220内的预处理水通过高压水泵320以加压方式输送到列式混合器360中。预处理水的量由控制阀330b确定。预处理水穿过压力计340b和流量计350b,所述压力计340b和流量计350b沿着管道管线安装在水箱220和列式混合器360之间。
压力计340a、340b和流量计350a、350b分别被配置为测量水、精炼油和预处理水的压力和流量。主控制器可以通过使用基于压力计340a、340b和流量计350a、350b的测量的值或类似物来调节精炼油与预处理油之间的比率。
期望地,供应到列式混合器360中的精炼油与预处理水之间的比率可以为大约1:1,但是可以根据操作条件被调节为6:4或7:3。
列式混合器360形成为Y形。即,来自精炼油箱170的管道管线和来自水箱220的管道管线结合到列式混合器360作为单个管线。列式混合器360可在其内表面上具有多个突起,从而对内部的介质产生紊流。在列式混合器内汇合的精炼油和预处理水在它们穿过时被有效地物理混合在一起。
参照图4,将详细描述根据示例实施例的混合油箱370。
根据示例实施例的混合油箱370被配置为储存来自列式混合器360的混合油。
为此目的,混合油箱370包括混合油搅拌器371、混合油加热器372和混合油位测量器373。
混合油搅拌器371被配置为搅拌引入混合油箱370中的混合油,使得有效地保持物理混合状态。举例来说,混合油搅拌器371可以包括在其上部的马达;以及被配置为将油和水混合的叶片。叶片可以以但不限于约250 rpm旋转以均匀地混合油和水。
例如,混合油可以在混合油箱370中停留约5分钟或更短的时间,在此期间,混合油可以通过混合油搅拌器371的搅拌操作更均匀地混合。
混合油加热器372可以被配置为将混合油的温度保持在预设范围内,以允许混合油箱370内部的温度恒定。期望地,混合油的温度可以被保持在例如从约25°C至约35°C的范围内。
混合油位测量器373被配置为测量混合油的油位。由主控制器连续监测混合油位测量器373的测量结果。主控制器可以基于该测量结果来控制混合油的流入和流出。
参照图5,将详细描述根据示例实施例的电离催化剂单元400。
混合油泵405被配置为将混合油箱370中的混合油输送到下面将详细描述的电离催化剂单元400。例如,混合油泵405可以被配置为将常规量的混合油连续地供应到电离催化剂单元400。此外,混合油泵405可以由但不限于摆线泵来实现。
电离催化剂单元400可以包括一个或多个电离催化剂组410,并且每个电离催化剂组410可以包括多个电离催化剂筒411。
在设置有多个电离催化剂组410的构造中,这些电离催化剂组410可以彼此串联或并联连接,以允许混合油反复穿过电离催化剂。例如,电离催化剂组410可以串联连接或以串联和并联结合的方式连接。
举例来说,参照图1(c)和图5,十二个电离催化剂筒411以串联和并联结合的方式连接。更具体地,可以设置四个电离催化剂组410,每个电离催化剂组具有三个电离催化剂筒411。如图1(c)所示,这四个电离催化剂组410可以以串联和并联结合的方式连接。
如上所述,当多个电离催化剂组410串联连接时,通过控制安装在电离催化剂组410前面的开闭控制阀406,使混合油反复穿过电离催化剂组410。
以这种方式,通过多次穿过电离催化剂组410,可以将混合油以更高的效率转化为生物乳化燃料。
同时,电离催化剂可以包括、但不限于氧化铝、硅胶、锗、氧化镁、镁、氧化钛、户室石(Tomuro stone)、沸石、锂矿石和钒作为主要组分。举例来说,电离催化剂筒411可以以装有球形催化剂的导管的形式来实现,该球形催化剂包含、但不限于氧化铝、硅胶、锗、氧化镁、镁、氧化钛、户室石、沸石、锂矿石和钒作为主要组分。例如,球形催化剂的直径可以为例如大约1 cm。
取决于将哪种催化剂材料添加到电离催化剂的上述主要组分中,多个电离催化剂筒411可以分为三种。
即,结合在每个电离中的多个电离催化剂筒411可以包括第一电离催化剂筒411a、第二电离催化剂筒411b和第三电离催化剂筒411c。
举例来说,参照图1(c)和图5,电离催化剂单元400可以包括以串联和并联结合的方式连接的四个电离催化剂组410,并且每个电离催化剂组410包括三个电离催化剂筒411a、411b和411c。
可允许混合油按照第一电离催化剂筒411a、第二电离催化剂筒411b、然后是第三电离催化剂筒411c的顺序穿过电离催化剂组410。
举例来说,参照图5,混合油可以两次穿过电离催化剂组410。即,在混合油可以依次穿过第一电离催化剂组410的第一电离催化剂筒411a、第二电离催化剂筒411b和第三电离催化剂筒411c之后,然后可以使混合油依次穿过第二电离催化剂组410的第一电离催化剂筒411a、第二电离催化剂筒411b和第三电离催化剂筒411c。
此外,第一电离催化剂筒411a用于使混合油中的油所含的碳进行电离。通过电离,可以促进水中的氢和油中的碳的吸附。
可以通过将铜离子、银离子、碳离子和电气石添加到基础催化剂材料中并且然后通过陶瓷化该混合物来制备容纳在第一电离催化剂筒411a中的电离催化剂,所述基础催化剂材料包括氧化铝、硅胶、锗、氧化镁、镁、氧化钛、户室石、沸石、锂矿石和钒。包括在第一电离催化剂筒411a中的电离催化剂可以被称为离子化催化剂。
第二电离催化剂筒411b用于使包含在混合油中的油中的碳组分和在混合油中的水中的氢组分耦合。例如,包含在混合油中的油中的碳组分可以为在穿过第一电离催化剂筒411a时被电离的碳。此外,混合油中的水中所含的氢组分可以为当如上所述对水箱中的水进行预处理时被电离的氢。
可以通过将氢离子、碳离子和活性氧簇添加到基础催化剂材料中并且然后通过陶瓷化该混合物来制备容纳在第二电离催化剂筒411a中的电离催化剂,所述基础催化剂材料包括氧化铝、硅胶、锗、氧化镁、镁、氧化钛、户室石、沸石、锂矿石和钒。包括在第二电离催化剂筒411b中的电离催化剂可以被称为氢化催化剂。
第三电离催化剂筒411c用于使已经穿过第一电离催化剂筒411a和第二电离催化剂筒411b的混合油稳定。
为了稳定混合油,第三电离催化剂筒411c可以用来涂覆在混合油穿过第二电离催化剂筒411b时获得的混合油的分子结构,从而允许维持该分子结构。
可以通过将钛粉末添加到基础催化剂材料中并且然后通过陶瓷化该混合物来制备容纳在第三电离催化剂筒411c中的电离催化剂,所述基础催化剂材料包括氧化铝、硅胶、锗、氧化镁、镁、氧化钛、户室石、沸石、锂矿石和钒。包括在第三电离催化剂筒411c中的电离催化剂可以被称为涂覆催化剂。
最后,如上所述,混合油在它穿过电离催化剂单元400时被转化为生物乳化燃料。
现在,通过参照图6,将详细说明根据本示例实施例的使用植物油制造生物乳化燃料的方法(在下文中,简称为“本生物乳化燃料制造方法”)。本生物乳化燃料制造方法涉及通过使用如上所述的本生物乳化燃料制造设备来产生生物乳化燃料。与在本重整燃料制造设备中描述的那些部件相同或相似的部件将被分配相同的附图标记,并且将简化或省略多余的描述。
本生物乳化燃料制造方法包括框S10,用于通过使用提供到油箱单元100中的凝结剂和离心倾析器将油与杂质分离来制备精炼油。
本重整燃料制造方法还包括框S20,用于通过使用提供到水箱单元200中的水箱催化剂对水进行预处理来制备预处理水。
在框S20中,水箱催化剂可包括含有电气石矿物的第一水箱催化剂;以及含有二氧化硅、硅酸盐矿物和卤素矿物中的至少一种的第二水箱催化剂。这与生物乳化燃料制造设备中描述的相同,因此,将省略其详细描述。
此外,本生物乳化燃料制造方法包括框S30,用于使用提供到混合油单元300中的列式混合器由从油箱单元100引入的精炼油和从水箱单元200引入的预处理水生产混合油。
在混合油单元300内,精炼油和预处理水通过在混合油箱中进行搅拌将进一步彼此混合。因此,可以均匀地保持混合油而不分离。
此外,本生物乳化燃料制造方法还包括框S40,用于使用提供到电离催化剂单元400中的电离催化剂将来自混合油单元300的混合油转化为生物乳化燃料。
如上所述,电离催化剂可以容纳在电离催化剂单元400中。电离催化剂单元400可以包括一个或多个电离催化剂组410,并且每个电离催化剂组410可以包括多个电离催化剂筒411。由于在本生物乳化燃料制造设备的描述中已经讨论了电离催化剂和电离催化剂单元400的构造/操作,因此将省略其详细描述。
为了说明的目的而提供了对说明性实施例的以上描述,并且本领域技术人员将理解,可以在不改变说明性实施例的技术概念和必要特征的情况下作出各种改变和修改。因此,很清楚,上述说明性实施例在所有方面都是说明性的,并且不限制本公开。例如,描述为单一类型的每个部件可以以分布式方式实现。同样,描述为分布的部件可以以组合方式实现。
本发明构思的范围由所附权利要求及其等同物限定,而不是由说明性实施例的详细描述限定。应当理解,从权利要求的含义和范围想到的所有修改和实施例及其等同物都包括在本发明构思的范围内。
Claims (13)
1.一种使用植物油的生物乳化燃料制造设备,其包括:
油箱单元,其被配置为精炼和储存引入所述油箱单元中的油;
水箱单元,其被配置为通过使用水箱催化剂对引入所述水箱单元中的水进行预处理;
混合油单元,其连接至所述油箱单元和所述水箱单元,并且被配置为通过将从所述油箱单元引入的精炼油与从所述水箱单元引入的预处理水混合来产生混合油;以及
电离催化剂单元,其连接至所述混合油单元,并且被配置为通过使用电离催化剂组将从所述混合油单元引入的所述混合油转化为生物乳化燃料。
2.根据权利要求1所述的生物乳化燃料制造设备,
其中,所述油箱单元还包括:
供油泵,其被配置为将所述油引入其中;
油箱,其被配置为通过所述供油泵接收所述油并暂时储存所述油;
凝结剂供给装置,其连接至所述油箱,并且被配置为将凝结剂提供到所述油箱中并固化所述油中的杂质;
输油泵,其被配置为输送所述油箱内的所述油和固化的杂质;
离心倾析器,其被配置为从所述输油泵接收所述油和固化的杂质,并通过将所述固化的杂质从所述油中分离出来产生所述精炼油;
精炼油输送泵,其被配置为从所述离心倾析器输送所述精炼油;以及
精炼油箱,其被配置为通过所述精炼油输送泵接收所述精炼油并暂时储存所述精炼油。
3.根据权利要求1所述的生物乳化燃料制造设备,
其中,所述水箱催化剂还包括:
第一油箱催化剂,其包含电气石矿物;以及
第二油箱催化剂,其包含二氧化硅、硅酸盐矿物和卤素矿物中的至少一种。
4.根据权利要求1所述的生物乳化燃料制造设备,
其中,所述混合油单元还包括:
高压油泵,其被配置为输送从所述油箱单元引入的所述精炼油;
高压水泵,其被配置为输送从所述水箱单元引入的所述预处理水;
列式混合器,其形成为Y形,并且被配置为通过所述高压油泵接收所述精炼油和通过所述高压水泵接收所述预处理水并产生所述混合油;以及
混合油箱,其被配置为接收和临时储存来自所述列式混合器的所述混合油。
5. 根据权利要求4所述的生物乳化燃料制造设备,
其中,所述精炼油穿过被配置为调节所述精炼油流的量的控制阀、被配置为测量其中压力的压力计和被配置为测量其中流量的流量计,所述控制阀、压力计和流量计都沿着管道管线安装在所述精炼油箱和所述列式混合器之间;以及
其中,所述预处理水穿过被配置为调节所述预处理水流的量的控制阀、被配置为测量其中压力的压力计和被配置为测量其中流量的流量计,所述控制阀、压力计和流量计都沿着管道管线安装在所述水箱和所述列式混合器之间。
6.根据权利要求5所述的生物乳化燃料制造设备,
其中,所述列式混合器在其内表面上包含多个突起,以对从所述精炼油箱引入的所述精炼油和从所述水箱引入的所述预处理水产生紊流。
7.根据权利要求5所述的生物乳化燃料制造设备,
其中,主控制器通过使用分别基于所述压力计和所述流量计的测量的控制值来调节所述精炼油与所述预处理油之间的比率。
8.根据权利要求1所述的生物乳化燃料制造设备,
其中,所述电离催化剂单元还包括:
混合油泵,其被配置为输送所述混合油;
一个或多个电离催化剂组,其被配置为通过所述混合油泵接收所述混合油;
其中,所述一个或多个电离催化剂组中的每一组包括多个电离催化剂筒;以及
其中,每个电离催化剂筒在其中容纳电离催化剂。
9.根据权利要求8所述的生物乳化燃料制造设备,
其中,所述电离催化剂组彼此串联连接或以串联和并联结合的方式彼此连接,以允许所述混合油依次从其中穿过,并且催化剂组的数目由安装在每个电离催化剂组前面的开闭控制阀选择。
10.根据权利要求9所述的生物乳化燃料制造设备,
其中,所述多个电离催化剂筒中的每个包括:
第一电离催化剂筒,其被配置为使所述混合油中的所述油中所含的碳电离;
第二电离催化剂筒,其被配置为使所述混合油中的所述油中所含的碳组分与所述混合油中的所述水中所含的氢组分耦合;以及
第三电离催化剂筒,其被配置为使已经穿过所述第一电离催化剂筒和所述第二电离催化剂筒的混合油稳定。
11.根据权利要求10所述的生物乳化燃料制造设备,
其中,允许所述混合油依次穿过所述第一电离催化剂筒、所述第二电离催化剂筒和所述第三电离催化剂筒。
12.根据权利要求11所述的生物乳化燃料制造设备,
其中,所述电离催化剂包含氧化铝、硅胶、锗、氧化镁、镁、氧化钛、户室石、沸石、锂矿石和钒作为基础催化剂材料。
13.一种使用植物油的生物乳化燃料制造方法,其包括:
通过使用提供到油箱单元中的凝结剂和离心倾析器将油与杂质分离来制备精炼油;
通过使用提供到水箱单元中的水箱催化剂对水进行预处理来制备预处理水;
使用提供到混合油单元中的列式混合器由从所述油箱单元引入的所述精炼油和从所述水箱单元引入的所述预处理水产生混合油;以及
利用提供到电离催化剂单元的电离催化剂组将来自所述混合油单元的所述混合油转化为生物乳化燃料。
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CN113050535A (zh) * | 2021-03-30 | 2021-06-29 | 武汉中油康尼科技有限公司 | 一种基于plc控制的自动精炼方法 |
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US11584894B2 (en) | 2021-04-23 | 2023-02-21 | James Chun Koh | Apparatus for bio emulsion fuel manufacturing from waste oils and method using the same |
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PH12019000338A1 (en) | 2021-02-08 |
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US20200362256A1 (en) | 2020-11-19 |
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