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CN101773796A - Method for emulsifying tri-component emulsion containing diesel, methanol and water - Google Patents

Method for emulsifying tri-component emulsion containing diesel, methanol and water Download PDF

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CN101773796A
CN101773796A CN 201010126397 CN201010126397A CN101773796A CN 101773796 A CN101773796 A CN 101773796A CN 201010126397 CN201010126397 CN 201010126397 CN 201010126397 A CN201010126397 A CN 201010126397A CN 101773796 A CN101773796 A CN 101773796A
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venturi tube
diesel oil
methanol
aqueous solution
water
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CN101773796B (en
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吴东垠
姚季
申琪
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Xian Jiaotong University
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Xian Jiaotong University
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Abstract

本发明公开了一种柴油、甲醇和水三组元乳化液乳化方法,将待乳化的柴油从文丘里管的入口段引入该文丘里管,柴油进入文丘里管前的压力大于0.48MPa,并流经文丘里管的收缩段到达喉部,再流向扩散段;将甲醇和水以1∶1~1∶2比例和总质量含量控制在1%~3%之间乳化剂混合后形成的甲醇水溶液,该甲醇水溶液在进入文丘里管前的压力大于0.18MPa,从文丘里管喉部引入文丘里管内,并与流经该处的柴油混合,柴油与甲醇水溶液以质量流量比9∶1~1∶1混合,形成乳化液,最后经扩散段流出,本发明可以使甲醇水溶液在短时间内快速均匀地分散到柴油中,避免局部乳化的不均匀现象,从而减少了破乳的不利因素,延长乳化液的保存期。

Figure 201010126397

The invention discloses a three-component emulsion emulsification method of diesel oil, methanol and water. The diesel oil to be emulsified is introduced into the Venturi tube from the inlet section of the Venturi tube. The pressure of the diesel oil before entering the Venturi tube is greater than 0.48MPa, and It flows through the constriction section of the Venturi tube to the throat, and then flows to the diffusion section; methanol and water are mixed in a ratio of 1:1 to 1:2 and the total mass content is controlled between 1% and 3%. Aqueous solution, the pressure of the aqueous methanol solution before entering the Venturi tube is greater than 0.18MPa, introduced into the Venturi tube from the throat of the Venturi tube, and mixed with the diesel oil flowing through the place, the mass flow ratio of diesel oil and methanol aqueous solution is 9:1~ 1:1 mixing to form an emulsion, and finally flow out through the diffusion section. The invention can quickly and evenly disperse the methanol aqueous solution into the diesel oil in a short time, avoiding the uneven phenomenon of local emulsification, thereby reducing the unfavorable factors of demulsification. Extend the shelf life of the emulsion.

Figure 201010126397

Description

一种柴油、甲醇和水三组元乳化液乳化方法 A kind of emulsification method of three-component emulsion of diesel oil, methanol and water

技术领域technical field

本发明涉及一种乳化方法,具体地说是涉及一种利用文丘里管形成柴油、甲醇和水三组元乳化液的乳化方法。The invention relates to an emulsification method, in particular to an emulsification method using a Venturi tube to form a three-component emulsion of diesel oil, methanol and water.

背景技术Background technique

液体的乳化问题不仅与生活息息相关,在工农业生产也有广泛的应用,如农药的配制、原油开采、医药、能源等各领域都有广泛的应用。乳化液作为一种替代燃料技术,具有节能、燃烧效率高、明显减少尾气污染等优点。The problem of liquid emulsification is not only closely related to life, but also widely used in industrial and agricultural production, such as the preparation of pesticides, crude oil extraction, medicine, energy and other fields. As an alternative fuel technology, emulsion has the advantages of energy saving, high combustion efficiency, and obvious reduction of exhaust pollution.

甲醇/水含量较少时是油包水(Water-in-Oil-O/W)型乳化液,分散相为“水”相(水或是醇与水的混合物),连续相为“油”。相比油/水乳化液,柴油、甲醇和水乳化液的能量密度较高,除了具有闪点温度低的优点之外,还可以消除在低温使用时的结冰现象。由于醇是含氧燃料,柴油机燃用甲醇、水和柴油乳化液具有明显降低烟度的作用,其烟度下降值最大可达50%左右。When the methanol/water content is low, it is a water-in-oil-O/W emulsion, the dispersed phase is the "water" phase (water or a mixture of alcohol and water), and the continuous phase is "oil" . Compared with oil/water emulsions, diesel oil, methanol and water emulsions have higher energy densities. In addition to the advantages of low flash point temperatures, they can also eliminate icing when used at low temperatures. Since alcohol is an oxygen-containing fuel, diesel engines fueled with methanol, water and diesel emulsion can significantly reduce smoke, and the maximum smoke reduction value can reach about 50%.

目前常用的高速搅拌乳化设备机械转速高,消耗动力大,且间歇性工作,一次乳化的量较少,由于乳化方式的限制,乳化工作需要在专门乳化站完成,然后将乳化燃油提供给燃油设备。而且乳化装置存在着结构复杂、维护费用高和乳化效果不理想等缺陷。本发明涉及的乳化设备结构简单、操作维护方便,而且还具有处理能力大、乳化效果好等优点。At present, the commonly used high-speed stirring and emulsifying equipment has a high mechanical speed, consumes a lot of power, and works intermittently. The amount of emulsification at one time is small. Due to the limitation of the emulsification method, the emulsification work needs to be completed in a special emulsification station, and then the emulsified fuel is provided to the fuel oil equipment. . Moreover, the emulsification device has defects such as complex structure, high maintenance cost and unsatisfactory emulsification effect. The emulsification equipment involved in the invention has the advantages of simple structure, convenient operation and maintenance, large processing capacity, good emulsification effect and the like.

发明内容Contents of the invention

本发明根据目前的乳化装置所具有的缺陷,提出一种新型的乳化装置。该装置利用文丘里管原理,使柴油、甲醇和水达到乳化的目的。所述的文丘里管包括入口段、收缩段、喉部、扩散段和出口段,入口段与柴油进口管路相连,扩散段与出口段相连,在文丘里管的喉部设置甲醇和水(甲醇水溶液)的入口;According to the defects of the current emulsification device, the present invention proposes a novel emulsification device. The device utilizes the Venturi tube principle to emulsify diesel, methanol and water. Described Venturi tube comprises inlet section, constriction section, throat, diffusion section and outlet section, and inlet section is connected with diesel oil inlet pipeline, and diffusion section is connected with outlet section, and methyl alcohol and water ( Methanol solution) inlet;

将待乳化的柴油从文丘里管的入口段引入该文丘里管,柴油进入文丘里管前的压力大于0.48MPa,并流经文丘里管的收缩段到达喉部,再流向扩散段;将甲醇和水以1∶1~1∶2比例和总质量含量控制在1%~3%之间乳化剂混合后形成的甲醇水溶液,该甲醇水溶液在进入文丘里管前的压力大于0.18Mpa,从文丘里管喉部引入文丘里管内,并与流经该处的柴油混合,柴油与甲醇水溶液以质量流量比9∶1~1∶1的比例混合,形成乳化液,最后经扩散段流出。The diesel oil to be emulsified is introduced into the Venturi tube from the inlet section of the Venturi tube, the pressure of the diesel oil before entering the Venturi tube is greater than 0.48MPa, and flows through the constriction section of the Venturi tube to the throat, and then flows to the diffusion section; the methanol The methanol aqueous solution formed by mixing the emulsifier with water in a ratio of 1:1 to 1:2 and the total mass content controlled between 1% and 3%. The pressure of the methanol aqueous solution before entering the Venturi tube is greater than 0.18Mpa. The throat of the inner tube is introduced into the Venturi tube and mixed with the diesel oil flowing through it. The diesel oil and methanol aqueous solution are mixed at a mass flow ratio of 9:1 to 1:1 to form an emulsion, and finally flow out through the diffusion section.

乳化剂是指司班Span和吐温Tween的混合液。Emulsifier refers to the mixture of Span and Tween.

本发明所涉及的乳化方法,区别于传统的乳化方法。本发明将甲醇水溶液连续而均匀地添加到连续流动的柴油中而得到乳化液,该过程是将柴油与甲醇水溶液按比例定量乳化的动态过程,可以使甲醇水溶液在短时间内快速均匀地分散到柴油中,避免局部乳化不均匀现象,从而可减少破乳的不利因素,延长乳化液的保存期。The emulsification method involved in the present invention is different from the traditional emulsification method. In the present invention, the methanol aqueous solution is continuously and uniformly added to the continuously flowing diesel oil to obtain an emulsion. This process is a dynamic process of quantitatively emulsifying the diesel oil and the methanol aqueous solution in proportion, and the methanol aqueous solution can be quickly and uniformly dispersed in a short period of time. In diesel oil, avoid partial emulsification unevenness, thereby reducing the unfavorable factors of demulsification and prolonging the shelf life of the emulsion.

附图说明Description of drawings

图1为本发明的工作原理示意图Fig. 1 is the working principle schematic diagram of the present invention

图2为利用本发明生产乳化液的工艺流程示意图Fig. 2 is the technological process schematic diagram that utilizes the present invention to produce emulsion

图中的标号分别表示:1、3物料泵;2、柴油管路;4、调节阀;5、甲醇水溶液入口;6、文丘里管;7、管路;8、物料缸(柴油);9、物料缸(甲醇水溶液);10、成品缸The labels in the figure respectively represent: 1, 3 material pump; 2, diesel pipeline; 4, regulating valve; 5, methanol aqueous solution inlet; 6, Venturi tube; 7, pipeline; 8, material cylinder (diesel); 9 , material cylinder (methanol aqueous solution); 10, finished product cylinder

具体实施方式Detailed ways

参照附图所示,图1中所示的文丘里管为一经典的文丘里管,包括入口段A、收缩段B、喉部C、扩散段D和出口段E,入口段A与柴油管路2相连,扩散段D与出口段E相连,喉部C与管路7相连。在柴油管路2中设有物料泵1,在管路7中设有物料泵3和调节阀4。图2为生产乳化液的工艺流程示意图,包括物料泵1和3、调节阀4、文丘里管6、物料缸(柴油)8、物料缸(甲醇水溶液)9、成品缸10以及连接各部分的管路,其中物料缸(柴油)8、物料泵1与文丘里管6的入口段A通过管路依次相连,物料缸(甲醇水溶液)9、物料泵3、调节阀4与文丘里管6的喉部C通过管路依次相连,成品缸10与文丘里管6的出口段E通过管路相连。Referring to the accompanying drawings, the Venturi tube shown in Figure 1 is a classic Venturi tube, including an inlet section A, a constriction section B, a throat C, a diffusion section D and an outlet section E, and the inlet section A and the diesel pipe The road 2 is connected, the diffusion section D is connected with the outlet section E, and the throat C is connected with the pipeline 7. A material pump 1 is provided in the diesel pipeline 2 , and a material pump 3 and a regulating valve 4 are provided in the pipeline 7 . Fig. 2 is a schematic diagram of the technological process for producing the emulsion, including material pumps 1 and 3, regulating valve 4, Venturi tube 6, material cylinder (diesel) 8, material cylinder (methanol aqueous solution) 9, finished product cylinder 10 and connecting parts The pipeline, wherein the material cylinder (diesel) 8, the material pump 1 and the inlet section A of the Venturi tube 6 are connected sequentially through the pipeline, and the material cylinder (methanol water solution) 9, the material pump 3, the regulating valve 4 and the Venturi tube 6 The throat C is connected in sequence through pipelines, and the finished cylinder 10 is connected with the outlet section E of the Venturi tube 6 through pipelines.

本发明提供了一种乳化方法,该方法是将甲醇水溶液定量、均匀、而且连续地添加到连续流动的柴油中而得到乳化燃料的动态乳化方法,其中主要是利用了一个文丘里管6向柴油中添加甲醇水溶液而形成乳化燃料。图1中所示的文丘里管为一经典的文丘里管,包括入口段A、收缩段B、喉部C、扩散段D和出口段E,入口段A与柴油管路2相连,扩散段D与出口段E相连。在文丘里管的喉部设置甲醇水溶液的入口5,该甲醇水溶液入口与管路7相连。本发明的乳化方法的操作步骤为:将甲醇与水按配制要求的比例混合后注入物料缸9中,此时阀门4处于关闭状态。然后将柴油利用物料泵1从文丘里管的入口段A引入该文丘里管,并流经文丘里管的收缩段B到达喉部C,接着流向扩散段D;当柴油流出文丘里管,而且在喉部形成高速和负压区后,再开启物料泵3,将甲醇水溶液从文丘里管的喉部引入文丘里管,与流向扩散段的高速柴油接触,根据文丘里原理形成快速冲击和混合,使柴油、甲醇和水乳化,并流经扩散段D,最后进入出口段E,得到柴油、甲醇和水三组元乳化液。The invention provides an emulsification method, which is a dynamic emulsification method for obtaining emulsified fuel by adding methanol aqueous solution quantitatively, uniformly and continuously to continuously flowing diesel oil, wherein a Venturi tube 6-way diesel oil is mainly used Add methanol aqueous solution to form emulsified fuel. The Venturi tube shown in Figure 1 is a classic Venturi tube, including an inlet section A, a constriction section B, a throat C, a diffusion section D, and an outlet section E. The inlet section A is connected to the diesel pipeline 2, and the diffusion section D is connected to exit section E. An inlet 5 for aqueous methanol is provided at the throat of the Venturi tube, and the inlet for aqueous methanol is connected to a pipeline 7 . The operation steps of the emulsification method of the present invention are as follows: methanol and water are mixed according to the ratio required for preparation and then injected into the material cylinder 9, and the valve 4 is in a closed state at this time. Then the diesel oil is introduced into the Venturi tube from the inlet section A of the Venturi tube by the material pump 1, and flows through the constriction section B of the Venturi tube to reach the throat C, and then flows to the diffusion section D; when the diesel oil flows out of the Venturi tube, and After forming a high-speed and negative pressure zone at the throat, turn on the material pump 3, and introduce methanol aqueous solution from the throat of the Venturi tube into the Venturi tube, contact with the high-speed diesel oil flowing to the diffusion section, and form rapid impact and mixing according to the Venturi principle , to emulsify diesel oil, methanol and water, and flow through the diffusion section D, and finally enter the outlet section E to obtain a three-component emulsion of diesel oil, methanol and water.

根据本发明的方法,应控制柴油在进入文丘里管前的压力大于0.48MPa,优选为0.48Mpa~0.58Mpa,控制甲醇水溶液在进入文丘里管前的压力大于0.18Mpa,优选为0.18Mpa~0.6Mpa,在以上参数范围内可以有效实现柴油与甲醇水溶液的快速均匀混合。According to the method of the present invention, the pressure of diesel oil before entering the Venturi tube should be controlled to be greater than 0.48MPa, preferably 0.48Mpa~0.58Mpa, and the pressure of methanol aqueous solution before entering the Venturi tube should be controlled to be greater than 0.18Mpa, preferably 0.18Mpa~0.6 Mpa, within the range of the above parameters, the rapid and uniform mixing of diesel oil and methanol aqueous solution can be effectively realized.

在本发明中,可适量调节甲醇与水的比例和流量大小。本发明优化了甲醇与水的质量比以及柴油和甲醇水溶液的质量比:即控制柴油与甲醇水溶液质量比在9∶1~1∶1的范围内混合;甲醇与水的质量比应控制在1∶1~1∶2之间。同时,乳化剂的含量应控制在1%~3%之间。In the present invention, the ratio and flow of methanol to water can be appropriately adjusted. The present invention optimizes the mass ratio of methanol to water and the mass ratio of diesel oil to methanol aqueous solution: that is, the mass ratio of diesel oil to methanol aqueous solution is controlled to mix within the range of 9:1 to 1:1; the mass ratio of methanol to water should be controlled at 1 : between 1 and 1:2. At the same time, the content of emulsifier should be controlled between 1% and 3%.

实施例1:生产柴油、甲醇和水三组元乳化液Embodiment 1: produce diesel oil, methyl alcohol and water three-component emulsion

本实例是利用本发明的乳化液配制方法生产一种柴油、甲醇和水的三相乳化液燃料。该乳化燃料的配制方案如下:This example is to utilize the emulsion preparation method of the present invention to produce a kind of three-phase emulsion fuel of diesel oil, methanol and water. The preparation scheme of this emulsified fuel is as follows:

柴油的质量分数约为70%,甲醇水溶液的质量分数约为29%。柴油在文丘里管的入口段速度为10m/s,喉口速度为40m/s,质量流量为10.048kg/s(36.17t/h);甲醇水溶液入口速度为34.88m/s,质量流量为4.29kg/s(15.4t/h)。乳化剂的含量约为1%。The mass fraction of diesel oil is about 70%, and the mass fraction of methanol aqueous solution is about 29%. The velocity of the diesel oil at the inlet section of the Venturi tube is 10m/s, the throat velocity is 40m/s, and the mass flow rate is 10.048kg/s (36.17t/h); the methanol aqueous solution inlet velocity is 34.88m/s, and the mass flow rate is 4.29 kg/s (15.4t/h). The content of emulsifier is about 1%.

具体的工艺流程参见图2所示。The specific process flow is shown in FIG. 2 .

准备工作:Preparation:

将柴油引入物料缸8中;配制甲醇水溶液(1∶1),然后加入适量的乳化剂,搅拌至均匀,引入物料缸9,待用。Introduce diesel oil into material tank 8; prepare methanol aqueous solution (1:1), then add an appropriate amount of emulsifier, stir until uniform, introduce into material tank 9, and set aside.

生产流程:Production Process:

开启物料泵1,当乳化柴油在进入文丘里管的压力约为0.5Mpa时,将柴油引入文丘里管6,待柴油流出文丘里的引出管时,而且在喉部形成高速和负压区后,开启物料泵3,将甲醇水溶液引入文丘里管的喉部5,甲醇水溶液在进入文丘里管前的压力约为0.5Mpa,同时利用流量调节阀4调节甲醇水溶液的流量大小,以含有甲醇、水和柴油的乳化液的总重量百分比计,使甲醇水溶液通过喉部时的质量分数为30%左右,在文丘里管的喉部,甲醇水溶液与高速柴油混合、乳化,混合均匀的乳化液打入成品缸10中。该过程中应该控制柴油与甲醇水溶液的流量比例,而且待柴油在文丘里管内形成流动并在喉部形成加速气流后,再开启物料泵3,将甲醇水溶液引入文丘里管的喉部5,与流向扩散段的高速柴油接触,根据文丘里原理形成快速冲击和混合,使柴油、甲醇和水乳化,并流经扩散段D,最后进入出口段E,得到柴油、甲醇和水三组元乳化液。该乳化方法的结果保证乳化燃料混合、乳化均匀,粒子大小分布均匀,稳定性好。Turn on the material pump 1. When the pressure of the emulsified diesel oil entering the Venturi tube is about 0.5Mpa, introduce the diesel oil into the Venturi tube 6. When the diesel oil flows out of the Venturi outlet tube, and after the high-speed and negative pressure zone is formed in the throat , open the material pump 3, the methanol aqueous solution is introduced into the throat 5 of the Venturi tube, the pressure of the methanol aqueous solution before entering the Venturi tube is about 0.5Mpa, and the flow regulating valve 4 is utilized to regulate the flow rate of the methanol aqueous solution to contain methanol, In terms of the total weight percentage of the emulsion of water and diesel oil, the mass fraction when the methanol aqueous solution passes through the throat is about 30%. Into the finished product cylinder 10. In this process, the flow ratio of diesel oil and methanol aqueous solution should be controlled, and after the diesel oil forms a flow in the venturi tube and an accelerated airflow is formed in the throat, the material pump 3 is turned on, and the methanol aqueous solution is introduced into the throat 5 of the venturi tube. The high-speed diesel oil flowing to the diffusion section contacts, forms rapid impact and mixing according to the Venturi principle, emulsifies diesel oil, methanol and water, flows through the diffusion section D, and finally enters the outlet section E to obtain a three-component emulsion of diesel oil, methanol and water . As a result of the emulsification method, the emulsified fuel can be mixed and emulsified uniformly, the particle size distribution is uniform, and the stability is good.

Claims (2)

1. a diesel oil, first alcohol and water method for emulsifying tri-component emulsion containing, it is characterized in that, the diesel oil for the treatment of emulsification is introduced this Venturi tube from the entrance of Venturi tube, diesel oil enters the preceding pressure of Venturi tube greater than 0.48MPa, and the contraction section of the Venturi tube of flowing through arrival throat, flow to diffuser again; The first alcohol and water is controlled at the methanol aqueous solution that forms after the emulsifier between 1%~3% with 1: 1~1: 2 ratio and gross mass content, the pressure of this methanol aqueous solution before entering Venturi tube is greater than 0.18Mpa, introduce in the Venturi tube from Venturi tube throat, and mix with the diesel oil at this place that flows through, diesel oil mixes with 9: 1~1: 1 ratio of mass flow ratio with methanol aqueous solution, form emulsion, after the diffuser outflow.
2. diesel oil according to claim 1, first alcohol and water method for emulsifying tri-component emulsion containing is characterized in that, emulsifying agent is meant the mixed liquor of Span of class of department and tween Tween.
CN2010101263970A 2010-03-18 2010-03-18 Method for emulsifying tri-component emulsion containing diesel, methanol and water Expired - Fee Related CN101773796B (en)

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Cited By (9)

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CN102703145A (en) * 2012-06-12 2012-10-03 昆明理工大学 Size mixing and conveying device and application method thereof
CN102921370A (en) * 2012-11-08 2013-02-13 广西华纳新材料科技有限公司 Venturi tube reactor
CN103111207A (en) * 2013-02-04 2013-05-22 西安交通大学 Square emulsion preparing device
CN104449915A (en) * 2014-11-10 2015-03-25 华玉叶 Emulsifying method for emulsion
CN104870375A (en) * 2012-10-23 2015-08-26 布鲁诺·皮罗内 Beverage adding device and method thereof
CN106582458A (en) * 2015-10-16 2017-04-26 世能华奇(北京)科技发展有限公司 Manufacturing method of mixed diesel, mixed diesel manufactured through method and manufacturing device
CN106698722A (en) * 2016-12-31 2017-05-24 杭州路弘科技有限公司 Oil-water separation device and application
CN109499410A (en) * 2019-01-11 2019-03-22 西安交通大学 A kind of venturi emulsion device for formulating of the perforation of the ejection structure containing venturi
WO2023019301A1 (en) * 2021-08-16 2023-02-23 The University Of Queensland Apparatus and method for forming emulsions for use in flotation

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CN102703145B (en) * 2012-06-12 2014-11-05 昆明理工大学 Size mixing and conveying device and application method thereof
CN102703145A (en) * 2012-06-12 2012-10-03 昆明理工大学 Size mixing and conveying device and application method thereof
US10206533B2 (en) 2012-10-23 2019-02-19 Bruno Pirone Additivation device for beverages and method thereof
CN104870375A (en) * 2012-10-23 2015-08-26 布鲁诺·皮罗内 Beverage adding device and method thereof
CN104870375B (en) * 2012-10-23 2017-08-08 布鲁诺·皮罗内 Beverage adding device and method
CN102921370A (en) * 2012-11-08 2013-02-13 广西华纳新材料科技有限公司 Venturi tube reactor
CN103111207A (en) * 2013-02-04 2013-05-22 西安交通大学 Square emulsion preparing device
CN104449915A (en) * 2014-11-10 2015-03-25 华玉叶 Emulsifying method for emulsion
CN106582458A (en) * 2015-10-16 2017-04-26 世能华奇(北京)科技发展有限公司 Manufacturing method of mixed diesel, mixed diesel manufactured through method and manufacturing device
CN106698722A (en) * 2016-12-31 2017-05-24 杭州路弘科技有限公司 Oil-water separation device and application
CN109499410A (en) * 2019-01-11 2019-03-22 西安交通大学 A kind of venturi emulsion device for formulating of the perforation of the ejection structure containing venturi
CN109499410B (en) * 2019-01-11 2024-02-02 西安交通大学 Venturi emulsion preparation device with Venturi injection structure and injection hole
WO2023019301A1 (en) * 2021-08-16 2023-02-23 The University Of Queensland Apparatus and method for forming emulsions for use in flotation

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