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CN100513534C - Modified fuel oil and production thereof - Google Patents

Modified fuel oil and production thereof Download PDF

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CN100513534C
CN100513534C CNB2004100662751A CN200410066275A CN100513534C CN 100513534 C CN100513534 C CN 100513534C CN B2004100662751 A CNB2004100662751 A CN B2004100662751A CN 200410066275 A CN200410066275 A CN 200410066275A CN 100513534 C CN100513534 C CN 100513534C
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oil
water
weight
diesel
parts
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CN1746273A (en
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张景云
王力民
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Beijing Sino Union science and Technology Development Co Ltd
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SHANGHAI REFINING MICROPOWDER SMELTING MACHINERY CO Ltd
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Abstract

本发明提供了一种改性燃料油及其生产方法。所述改性燃料油含有:(a)10-70重量份数的重油;(b)30-90重量份数的柴油;且重油和柴油的总量为100重量份,和(c)水,并且水与重油加柴油的总油之间的重量比为5∶95-30∶70;其中,98%的水以0.1-3微米的水滴形式存在,并且95%以上的水滴的粒径小于2微米。本发明的改性燃料油稳定性好,雾化非常好,燃烧充分,污染极小,是一种成本低廉的洁净燃料。The invention provides a modified fuel oil and a production method thereof. The modified fuel oil contains: (a) 10-70 parts by weight of heavy oil; (b) 30-90 parts by weight of diesel oil; and the total amount of heavy oil and diesel oil is 100 parts by weight, and (c) water, And the weight ratio between water and the total oil of heavy oil plus diesel oil is 5:95-30:70; wherein, 98% of the water exists in the form of water droplets of 0.1-3 microns, and more than 95% of the water droplets have a particle size of less than 2 Micron. The modified fuel oil of the invention has good stability, very good atomization, sufficient combustion and minimal pollution, and is a clean fuel with low cost.

Description

一种改性燃料油及其生产方法 A kind of modified fuel oil and its production method

技术领域 technical field

本发明涉及环境保护和燃料加工领域,更具体地涉及一种改性燃料油及其生产方法。The invention relates to the fields of environmental protection and fuel processing, and more specifically relates to a modified fuel oil and a production method thereof.

背景技术 Background technique

柴油是一类重要的燃料,由于其热值高,使用方便,除作为车船发动机的燃料之外,还广泛用作中小锅炉、加热炉和中小工业窑炉的燃料,用量非常大。但是柴油价格较高,特别是近年来,石油价格高企,柴油价格也水涨船高,大大增加了企业成本,因此,降低燃料成本成为人们迫切追求的目标。Diesel is an important fuel. Due to its high calorific value and ease of use, it is widely used as fuel for small and medium boilers, heating furnaces and small and medium industrial kilns in addition to being used as fuel for vehicle and ship engines. The consumption is very large. However, the price of diesel oil is relatively high, especially in recent years, the price of oil has been high, and the price of diesel oil has also risen, which has greatly increased the cost of enterprises. Therefore, reducing fuel costs has become an urgent goal for people.

重油是一类应用非常广泛的液体燃料,主要来自石油炼制后的渣油,经加入适量的轻质油调和而成,用作工业锅炉、加热炉和工业窑炉的燃料。其粘度适中,燃烧性能好,发热量大,价格比柴油低很多。人们曾经试图用重油代替柴油,以降低企业的燃料费用。Heavy oil is a kind of widely used liquid fuel. It mainly comes from the residual oil after petroleum refining, which is blended by adding an appropriate amount of light oil. It is used as fuel for industrial boilers, heating furnaces and industrial kilns. Its viscosity is moderate, its combustion performance is good, its calorific value is large, and its price is much lower than that of diesel. Attempts have been made to replace diesel with heavy oil to reduce fuel costs for businesses.

然而,重油不能直接在柴油锅炉上燃烧,原因是:第一,重油粘度远大于柴油的粘度,必须将重油加热,使其温度升高到适宜雾化的程度,在进入喷嘴前温度一般在100-140℃之间,这就要求油罐和管线有伴热的设施,但是一般柴油燃烧系统没有伴热设施,所以难于输送和雾化;第二,重油中含有较多的残碳、沥青质、胶质和机械杂质,它们的存在容易导致过滤网和喷油嘴堵塞,也容易使燃烧不充分,导致污染物排放超标。However, heavy oil cannot be directly burned on diesel boilers for the following reasons: first, the viscosity of heavy oil is much higher than that of diesel oil, and the heavy oil must be heated to raise its temperature to a level suitable for atomization. The temperature before entering the nozzle is generally at 100 Between -140°C, this requires oil tanks and pipelines to have heat-tracing facilities, but the general diesel combustion system does not have heat-tracing facilities, so it is difficult to transport and atomize; second, heavy oil contains more residual carbon and asphaltenes , colloid and mechanical impurities, their existence can easily lead to clogging of filter screens and fuel injectors, and can also easily cause insufficient combustion, resulting in excessive pollutant emissions.

人们曾经将重油和柴油简单地混合,制备成混和油,在柴油锅炉或工业加热炉上燃用,但是效果不理想。最主要的缺点是雾化不良,燃烧不充分,产生积碳,污染物排放多,也发生喷油嘴堵塞现象,所以简单的重油和柴油的混和油难于推广应用。People used to simply mix heavy oil and diesel oil to prepare blended oil and burn it on diesel boilers or industrial heating furnaces, but the effect was not satisfactory. The main disadvantages are poor atomization, insufficient combustion, carbon deposits, high pollutant emissions, and clogging of fuel injectors. Therefore, simple blends of heavy oil and diesel oil are difficult to popularize and apply.

美国专利4,400,177报导利用超声波乳化技术能将重油和柴油的混合物制备成稳定性良好的乳化燃料,但是没有给出乳化油中水的粒径和乳化燃料油稳定性的数据。另外,超声波乳化技术的能耗大,难于实现工业化大规模生产。US Patent No. 4,400,177 reports that the mixture of heavy oil and diesel oil can be prepared into emulsified fuel with good stability by ultrasonic emulsification technology, but the particle size of water in the emulsified oil and the data of the stability of the emulsified fuel oil are not given. In addition, ultrasonic emulsification technology consumes a lot of energy, making it difficult to achieve industrialized mass production.

综上所述,为了有效地降低燃料成本,本领域迫切需要开发新的成本低廉且燃烧洁净的燃料油以及其制备方法。To sum up, in order to effectively reduce fuel costs, there is an urgent need in this field to develop new low-cost and clean-burning fuel oils and their preparation methods.

发明内容 Contents of the invention

本发明的目的就是提供一种成本低廉且燃烧洁净的改性燃料油以及其制备方法。The object of the present invention is to provide a modified fuel oil with low cost and clean combustion and a preparation method thereof.

在本发明的第一方面,提供了一种改性燃料油,它含有:In a first aspect of the present invention, a modified fuel oil is provided, which contains:

(a)10-70重量份数的重油;(a) heavy oil of 10-70 parts by weight;

(b)30-90重量份数的柴油;和(b) 30-90 parts by weight of diesel; and

(c)水,(c) water,

其中,重油和柴油的总量为100重量份,并且水与重油加柴油的总油之间的重量比为5:95-30:70;98%以上的水以粒径0.1-3微米的水滴形式存在,并且油中固体颗粒物的平均粒度为1-5微米。Wherein, the total amount of heavy oil and diesel oil is 100 parts by weight, and the weight ratio between water and the total oil of heavy oil and diesel oil is 5:95-30:70; more than 98% of the water is in the form of water droplets with a particle size of 0.1-3 microns form, and the average particle size of the solid particles in the oil is 1-5 microns.

在另一优选例中,95%以上的水以粒径小于2微米的水滴形式存在。In another preferred example, more than 95% of the water exists in the form of water droplets with a particle size of less than 2 microns.

在另一优选例中,固体颗粒的平均粒度为1-3微米。In another preferred example, the average particle size of the solid particles is 1-3 microns.

在另一优选例中,水与重油加柴油的总油之间的重量比为8:92-20:80。In another preferred example, the weight ratio of water to the total oil of heavy oil plus diesel oil is 8:92-20:80.

在另一优选例中,所述的重油选自:4号至7号的燃料油,180号重油、380号重油、250号重油、渣油、非石油来源的煤焦油、页岩油、植动物来源的油类、废油及其混合物。In another preferred example, the heavy oil is selected from: No. 4 to No. 7 fuel oil, No. 180 heavy oil, No. 380 heavy oil, No. 250 heavy oil, residual oil, coal tar from non-petroleum sources, shale oil, plant Oils of animal origin, waste oils and mixtures thereof.

在另一优选例中,所述的柴油选自下组:船用柴油、10号至负50号的轻柴油、及其混合物。In another preferred example, the diesel oil is selected from the group consisting of marine diesel oil, light diesel oil from No. 10 to No. 50, and mixtures thereof.

在另一优选例中,所述的水选自淡水、工业废水、pH值4-6弱酸性水、pH值8-11的弱碱性水、或硬水。In another preferred embodiment, the water is selected from fresh water, industrial wastewater, weakly acidic water with a pH value of 4-6, weakly alkaline water with a pH value of 8-11, or hard water.

在另一优选例中,所述的燃料油在20℃下放置6个月以上,油水不分离;或在80℃放置3个月以上油水不分离。In another preferred example, when the fuel oil is stored at 20°C for more than 6 months, the oil and water will not separate; or at 80°C for more than 3 months, the oil and water will not separate.

在另一优选例中,还含有0.01-10重量份数的选自下组的添加剂:乳化剂、脱硫剂。In another preferred embodiment, it also contains 0.01-10 parts by weight of additives selected from the group consisting of emulsifiers and desulfurizers.

在本发明的第二方面,提供了一种改性燃料油的制备方法,该方法包括以下步骤:In the second aspect of the present invention, a kind of preparation method of modified fuel oil is provided, the method comprises the following steps:

(i)将(a)10-70重量份数的重油、(b)30-90重量份数的柴油、和(c)水混合,形成原料混合物,其中重油和柴油的总量为100重量份,并且水与重油加柴油的总油之间的重量比为5:95-30:70,(i) (a) 10-70 parts by weight of heavy oil, (b) 30-90 parts by weight of diesel oil, and (c) water are mixed to form a raw material mixture, wherein the total amount of heavy oil and diesel oil is 100 parts by weight , and the weight ratio between water and the total oil of heavy oil plus diesel oil is 5:95-30:70,

(ii)将原料混合物进行研磨,使燃料中的98%以上的水以粒径0.1-3微米的水滴形式存在,并且95%以上的水滴的粒径小于2微米而固体颗粒物的平均粒度为1-5微米,从而获得改性燃料油;(ii) Grinding the raw material mixture so that more than 98% of the water in the fuel exists in the form of water droplets with a particle diameter of 0.1-3 microns, and the particle diameter of more than 95% of the water droplets is less than 2 microns and the average particle size of the solid particles is 1 -5 microns to obtain modified fuel oil;

或者该方法包括步骤:Or the method includes the steps:

将(a)10-70重量份数的重油(b)30-90重量份数的柴油和(c)水送入研磨设备进行研磨,其中重油和柴油的总量为100重量份,并且水与重油加柴油的总油之间的重量比为5:95-30:70,使燃料中98%以上的水以粒径0.1-3微米的水滴形式存在,并且95%以上的水滴的粒径小于2微米而固体颗粒的平均粒度为1-5微米,从而获得改性燃料油。(a) heavy oil of 10-70 parts by weight (b) diesel oil of 30-90 parts by weight and (c) water are sent into grinding equipment for grinding, wherein the total amount of heavy oil and diesel oil is 100 parts by weight, and water and The weight ratio between heavy oil and diesel oil is 5:95-30:70, so that more than 98% of the water in the fuel exists in the form of water droplets with a particle size of 0.1-3 microns, and more than 95% of the water droplets have a particle size smaller than 2 microns and the average particle size of solid particles is 1-5 microns, thereby obtaining modified fuel oil.

具体实施方式 Detailed ways

本发明人经过深入而广泛的研究发现:将重油、柴油和水混合形成的原料混合物,经超细研磨和均质后,当98%以上的水以粒径0.1-3微米的水滴形式存在,并且95%以上的水滴的粒径小于2微米,同时,形成了一种以油为连续相、水为分散相的新型结构的燃料油。在这种燃料油中,由于粒子微细,分布均匀,所以燃料油乳液非常稳定。又由于油包裹着超细的水滴,因此易于分散雾化,使燃烧非常完全,故该燃料油是一种清洁燃料。在此基础上完成了本发明。The inventor has found through in-depth and extensive research that: the raw material mixture formed by mixing heavy oil, diesel oil and water, after ultrafine grinding and homogenization, when more than 98% of the water exists in the form of water droplets with a particle size of 0.1-3 microns, And the particle size of more than 95% of the water droplets is less than 2 microns, and at the same time, a fuel oil with a new structure is formed with oil as the continuous phase and water as the dispersed phase. In this kind of fuel oil, the fuel oil emulsion is very stable because the particles are fine and evenly distributed. And because the oil is surrounded by ultra-fine water droplets, it is easy to disperse and atomize, so that the combustion is very complete, so the fuel oil is a clean fuel. The present invention has been accomplished on this basis.

如本文所用,术语“本发明的燃料油”、“本发明的燃料组合物”、“本发明的改性燃料油”、“本发明的改性燃料油组合物”可互换施用,都指含有重油、柴油和水,且98%以上(更佳地99%以上,最佳地99.9%以上)水滴的粒径为0.1-3微米的油包水型混合物。As used herein, the terms "fuel oil of the present invention", "fuel composition of the present invention", "modified fuel oil of the present invention", "modified fuel oil composition of the present invention" are used interchangeably and refer to The water-in-oil mixture contains heavy oil, diesel oil and water, and more than 98% (more preferably more than 99%, most preferably more than 99.9%) of the water droplets have a particle size of 0.1-3 microns.

本发明的燃料油可代替柴油,它基本上是由重油、柴油和水按一定比例组成的一种油包水型乳化混合燃料油,作为柴油锅炉和工业加热炉及工业窑炉的燃料,其成本远低于相应的柴油。Fuel oil of the present invention can replace diesel oil, and it is basically a kind of water-in-oil emulsified mixed fuel oil composed of heavy oil, diesel oil and water in a certain proportion, as fuel for diesel boilers, industrial heating furnaces and industrial kilns. The cost is much lower than the corresponding diesel.

本发明所述的改性燃料油是一种油包水型乳化燃料油,它的一个重要特点是乳化燃料中水滴极细,98%以上的水滴的粒径在0.1-3微米范围,95%以上的水滴的粒径小于2微米。The modified fuel oil of the present invention is a kind of water-in-oil emulsified fuel oil. One of its important features is that the water droplets in the emulsified fuel are extremely fine, and more than 98% of the water droplets have a particle size in the range of 0.1-3 microns, and 95% The particle size of the above water droplets is less than 2 microns.

本发明所述改性燃料油的另一个重要特点是其中的固体残碳和机械杂质粒度极细,平均粒径在1-5微米(更佳地为1-4微米),大部分(90%以上)在1-3微米之间。Another important feature of the modified fuel oil of the present invention is that solid carbon residue and mechanical impurity particle size are very fine wherein, the average particle diameter is at 1-5 micron (beer 1-4 micron), most (90% above) between 1-3 microns.

重油heavy oil

可用于本发明的重油没有特别限制,代表性的例子包括(但并不限于):我国燃料油行业标准(SH/T0356-1996)中的4号至7号各牌号的燃料油,也可以是进口的180号、380号重油及其它牌号的进口重油,还可以是国产250号重油,渣油。还可以是非石油来源的煤焦油、页岩油和植物、动物来源的油类,还可以是上述各种油的废油及上述各种油的混合物等。The heavy oil that can be used in the present invention is not particularly limited, representative example includes (but not limited to): the fuel oil of No. 4 to No. 7 grades in my country's fuel oil industry standard (SH/T0356-1996), also can be Imported No. 180, No. 380 heavy oil and imported heavy oil of other brands can also be domestic No. 250 heavy oil and residual oil. It can also be non-petroleum source coal tar, shale oil, vegetable and animal source oils, waste oil of the above-mentioned various oils and mixtures of the above-mentioned various oils, etc.

在本发明所述的燃料油中,以重量份数表示,重油的用量通常为在10~70重量份数之间,较佳地40~60重量份数之间。当重油的用量小于上述范围(10重量份)时,成本下降得不明显,当重油的用量大于上述范围(70重量份)时,可能导致燃料油粘度过高。In the fuel oil of the present invention, expressed in parts by weight, the amount of heavy oil is usually between 10-70 parts by weight, preferably between 40-60 parts by weight. When the amount of heavy oil is less than the above range (10 parts by weight), the cost reduction is not obvious, and when the amount of heavy oil is greater than the above range (70 parts by weight), the viscosity of the fuel oil may be too high.

柴油diesel fuel

可用于本发明的柴油没有特别限制,包括各种常规的轻柴油,代表性的例子包括(但并不限于):船用柴油、国家标准GB/252-94中的10号及其以下牌号的轻柴油(如10号至负50号的轻柴油)。它们也可以是蒸馏柴油,还可以是催化裂化生产的柴油。The diesel oil that can be used in the present invention is not particularly limited, including various conventional light diesel oils, representative examples include (but not limited to): marine diesel oil, No. 10 in the national standard GB/252-94 and the light oil of the following brands Diesel oil (such as light diesel oil from No. 10 to minus No. 50). They can also be distilled diesel or diesel produced by catalytic cracking.

在本发明所述的燃料油中,以重量份数表示,柴油的用量通常为在30~90重量份数之间,较佳地40~60重量份数之间。当柴油的用量小于上述范围(30重量份)时,燃料油的粘度会偏大,当柴油的用量大于上述范围(90重量份)时,成本的下降不明显。In the fuel oil of the present invention, expressed in parts by weight, the amount of diesel oil used is generally between 30-90 parts by weight, preferably between 40-60 parts by weight. When the amount of diesel oil is less than the above range (30 parts by weight), the viscosity of the fuel oil will be too high, and when the amount of diesel oil is greater than the above range (90 parts by weight), the cost reduction is not obvious.

此外,在优选例中,改性燃料油中重油和柴油的重量比例可以在10:90-70:30之间,一般在40:60-60:40之间。In addition, in a preferred example, the weight ratio of heavy oil and diesel oil in the modified fuel oil can be between 10:90-70:30, generally between 40:60-60:40.

water

可用于本发明的水没有特别限制,代表性的例子包括(但并不限于):淡水,包括河水、湖泊水、自来水、井水、地下水和其他来源的淡水,也可以是含有有机物的工业废水,还可以是pH值4-6弱酸性水或pH值8-11的弱碱性水或含有微量无机物的硬水。Water that can be used in the present invention is not particularly limited, and representative examples include (but are not limited to): fresh water, including river water, lake water, tap water, well water, ground water, and other sources of fresh water, and industrial wastewater containing organic matter , It can also be weakly acidic water with a pH value of 4-6 or weakly alkaline water with a pH value of 8-11 or hard water containing trace amounts of inorganic substances.

在本发明所述的燃料油中,以重量份数表示,水的用量通常在5-30重量份数之间,较佳地8-20重量份数之间。此外,水与油(重油加柴油)重量的比例在5:95-30:70之间,一般在8:92-20:80之间。当水用量小于上述范围(5重量份)时,燃料油的雾化性能改善不大,易导致燃烧不完全;当水用量大于上述范围(30重量份)时,乳化油将由油包水型转化为水包油型,乳化油变得不稳定。In the fuel oil of the present invention, expressed in parts by weight, the amount of water used is usually between 5-30 parts by weight, preferably between 8-20 parts by weight. In addition, the weight ratio of water to oil (heavy oil plus diesel oil) is between 5:95-30:70, generally between 8:92-20:80. When the amount of water is less than the above range (5 parts by weight), the atomization performance of fuel oil will not be improved much, which will easily lead to incomplete combustion; when the amount of water is greater than the above range (30 parts by weight), the emulsified oil will be converted from water-in-oil For the oil-in-water type, the emulsified oil becomes unstable.

额外成分extra ingredients

在本发明的改性燃料油中还可加入各种常规的添加剂,例如乳化剂、脱硫剂、稳定剂等。这些添加剂的用量可以为常规用量,通常为0.01-10重量份数,较佳地为0.1-5重量份数。Various conventional additives, such as emulsifiers, desulfurizers, stabilizers, etc., can also be added to the modified fuel oil of the present invention. These additives can be used in conventional amounts, usually 0.01-10 parts by weight, preferably 0.1-5 parts by weight.

例如,本发明改性燃料油的制备方法中,还可以使用乳化剂。乳化剂是有机长链极性分子,一端是亲水的化学基团,例如下列基团,但是不限于这些基团:羧基、氨基、酰胺基、磺酸基、羟基、醚基等。一端是亲油的长链化学基团,如烷基和芳香基等。乳化剂还可以是高分子化合物,包括(但并不限于):聚氧化乙烯、聚甲醛、聚乙烯醇、羧甲基纤维素、甲基纤维素、明胶、聚丙烯酰胺、聚丙烯酸及其酯类等。这些乳化剂可以单独使用,也可以经选择两种或以上配合使用。乳化剂用量通常为0.01-1重量份数。For example, in the preparation method of the modified fuel oil of the present invention, an emulsifier can also be used. Emulsifiers are organic long-chain polar molecules with a hydrophilic chemical group at one end, such as, but not limited to, the following groups: carboxyl, amino, amide, sulfonic acid, hydroxyl, ether, etc. One end is a lipophilic long-chain chemical group, such as an alkyl group and an aromatic group. The emulsifier can also be a polymer compound, including (but not limited to): polyethylene oxide, polyoxymethylene, polyvinyl alcohol, carboxymethyl cellulose, methyl cellulose, gelatin, polyacrylamide, polyacrylic acid and its esters class etc. These emulsifiers can be used alone or in combination of two or more selected ones. The amount of emulsifier is usually 0.01-1 parts by weight.

脱硫剂可以是石灰石、白云石和石灰以及其他含有钙或镁的有机或无机物质或这些物质的混合物。本发明中所述的脱硫剂可以是未经过超细研磨的(如平均粒度大于20微米的脱硫剂),但优选的脱硫剂是经过超细研磨的,或市售的超细碳酸钙等,其平均粒度在20微米以下的脱硫剂,这样可以进一步提高除硫效果。还也可以使用石灰浆作为脱硫剂。The desulfurizer can be limestone, dolomite and lime and other organic or inorganic substances containing calcium or magnesium or a mixture of these substances. The desulfurizing agent described in the present invention can be not through superfine grinding (as the desulfurizing agent with average particle size greater than 20 microns), but the preferred desulfurizing agent is through superfine grinding, or commercially available superfine calcium carbonate etc., The desulfurizer whose average particle size is below 20 microns can further improve the desulfurization effect. Lime slurry can also be used as a desulfurizer.

此外,虽然可以在本发明的改性燃料油中添加其他燃料物质(如汽油、超细煤粉末等),但是从成本和安全角度考虑,通常不必进一步添加其他燃料。In addition, although other fuel substances (such as gasoline, ultra-fine coal powder, etc.) can be added to the modified fuel oil of the present invention, it is usually not necessary to further add other fuels from the perspective of cost and safety.

制备方法Preparation

本发明还提供了改性燃料油的生产方法。The invention also provides a production method of the modified fuel oil.

本发明所述的改性燃料油的生产方法包括步骤:The production method of modified fuel oil of the present invention comprises steps:

(i)将(a)10-70重量份数的重油、(b)30-90重量份数的柴油、(c)适量的水以及(d)任选的额外成分(如乳化剂)混合,形成原料混合物,(i) mixing (a) 10-70 parts by weight of heavy oil, (b) 30-90 parts by weight of diesel oil, (c) an appropriate amount of water and (d) optional additional ingredients (such as emulsifiers), to form a raw material mixture,

(ii)将原料混合物进行研磨,使燃料中的98%以上的水以0.1-3微米的水滴形式存在,并且95%以上的水滴的粒径小于2微米,从而获得改性燃料油。(ii) Grinding the raw material mixture so that more than 98% of the water in the fuel exists in the form of water droplets of 0.1-3 microns, and more than 95% of the water droplets have a particle size of less than 2 microns, thereby obtaining modified fuel oil.

在另一优选例中,该方法包括步骤:将(a)10-70重量份数的重油(b)30-90重量份数的柴油,(c)适量的水以及(d)任选的额外成分(如乳化剂)依次或同时送入研磨设备进行研磨,使燃料中的98%以上的水以0.1-3微米的水滴形式存在,并且95%以上的水滴的粒径小于2微米,从而获得改性燃料油。In another preferred embodiment, the method comprises the steps of: (a) 10-70 parts by weight of heavy oil (b) 30-90 parts by weight of diesel oil, (c) an appropriate amount of water and (d) optional additional Components (such as emulsifiers) are sent to the grinding equipment sequentially or simultaneously for grinding, so that more than 98% of the water in the fuel exists in the form of water droplets of 0.1-3 microns, and more than 95% of the water droplets have a particle size of less than 2 microns, thereby obtaining Modified fuel oil.

研磨的方法没有特别限制,可以是本领域现有的超细研磨或粉碎方法,只要其能使燃料中的水粒子(即水滴)、固体颗粒(包括固体残碳和机械杂质)的粒径达到所需尺寸。The method of grinding is not particularly limited, it can be an existing ultrafine grinding or crushing method in the art, as long as it can make the particle diameter of water particles (i.e. water droplets) and solid particles (comprising solid carbon residue and mechanical impurities) in the fuel reach desired size.

在本发明的一个优选例中,是将重油、柴油和水按一定的比例加入到上海精微粉溶机械设备有限公司生产的旋转脉动超细微粒粉溶机(以下简称“混和超细研磨机”)(中国专利申请号:01109394.3)中进行混合超细研磨成为燃料油,使燃料中的水滴、固体残碳和机械杂质粒径(或粒度)达到所需的尺寸。In a preferred example of the present invention, heavy oil, diesel oil and water are added in a certain proportion to the rotating pulse ultrafine particle powder dissolving machine (hereinafter referred to as "mixing ultrafine grinding machine") produced by Shanghai Fine Powder Dissolving Machinery Equipment Co., Ltd. ) (Chinese Patent Application No.: 01109394.3) is mixed and superfinely ground to become fuel oil, so that the particle size (or particle size) of water droplets, solid residual carbon and mechanical impurities in the fuel can reach the required size.

当原料组合物被研磨至水滴和固体粒子粒径非常微小时,改性燃料油中的油、有机质、水等微小粒子就可非常均匀地分布,状态稳定,粘度低、具有很好的流动性,可用于现有的柴油锅炉。When the raw material composition is ground to a very small particle size of water droplets and solid particles, the oil, organic matter, water and other tiny particles in the modified fuel oil can be very uniformly distributed, the state is stable, the viscosity is low, and it has good fluidity , can be used in existing diesel boilers.

本发明的生产方法可以是连续式的,也可以是间歇式的。优选方式是连续式的。一种优选的生产方法是将重油、柴油和水按所需要的配比经过计量装置同时送入混合超细研磨机中进行混合超细研磨,流水作业,可实现连续化生产。此外,根据需要,可以将物料多次研磨,也可以将两台或多台混合超细研磨设备串联使用,可以得到更细、混合更加均匀的改性燃料油。The production method of the present invention can be continuous or batch. The preferred mode is continuous. A preferred production method is to simultaneously send heavy oil, diesel oil and water into a mixing ultra-fine grinding machine through a metering device according to the required ratio for mixing and ultra-fine grinding, and flow operation can realize continuous production. In addition, according to the needs, the material can be ground multiple times, or two or more sets of mixing ultra-fine grinding equipment can be used in series to obtain finer and more uniformly mixed modified fuel oil.

此外,改性燃料油的生产还可以是分步进行,例如先将重油和水进行混合研磨乳化,制备成乳化重质燃料油,再将这种乳化油和柴油混合研磨均质,制备成本发明所述的改性燃料油;或者先将柴油和水制成乳化柴油,然后再将乳化柴油与重油混合研磨均质,制备成改性燃料油;还可以是先将重油和柴油混合研磨均质,制成混合油,然后再加水研磨乳化,制成改性燃料油;还可以是同时将重油、柴油和水加入到研磨乳化机中进行混合研磨均质乳化,制备成改性燃料油。分步混合超细研磨生产改性燃料油也可以是连续式的,也可以是间歇式的。优选方式是连续式的,因为生产效率比较高。In addition, the production of modified fuel oil can also be carried out step by step, for example, heavy oil and water are mixed, ground and emulsified to prepare emulsified heavy fuel oil, and then the emulsified oil and diesel oil are mixed and ground to homogeneously prepare the present invention The modified fuel oil; or firstly make diesel oil and water into emulsified diesel oil, and then mix and grind the emulsified diesel oil and heavy oil to make a modified fuel oil; it is also possible to first mix and grind the heavy oil and diesel oil , to make mixed oil, and then add water to grind and emulsify to make modified fuel oil; it is also possible to add heavy oil, diesel oil and water to a grinding emulsifier at the same time for mixing, grinding and homogeneous emulsification to prepare modified fuel oil. The production of modified fuel oil by step-by-step mixing and superfine grinding can also be continuous or intermittent. The preferred method is continuous, because the production efficiency is relatively high.

由于燃料油特别是重油在较低的温度下粘度高,流动性差,所以生产时的物料温度可以高于室温,控制在30-90℃范围,最好在50-80℃范围。Because fuel oil, especially heavy oil, has high viscosity and poor fluidity at relatively low temperatures, the material temperature during production can be higher than room temperature and controlled within the range of 30-90°C, preferably within the range of 50-80°C.

本发明的主要优点在于:The main advantages of the present invention are:

(a)本发明的改性燃料油质地非常均匀,局部没有高粘性的小团块,其粘度大大低于原料重油,接近混合燃料中的柴油的粘度,大颗粒残碳和固体杂质少,不堵过滤网,不堵喷油嘴。(a) The modified fuel oil of the present invention is very uniform in texture, and there are no small agglomerates with high viscosity locally. Its viscosity is much lower than that of raw material heavy oil, close to the viscosity of diesel oil in the mixed fuel, and there are few large particles of residual carbon and solid impurities. Block the filter, not block the fuel injector.

(b)本发明的改性燃料油燃烧快速充分,火焰短,火焰温度高,提高了锅炉、工业窑炉和工业加热炉的热效率,具有节省燃料的作用。(b) The modified fuel oil of the present invention burns quickly and fully, has short flame and high flame temperature, improves the thermal efficiency of boilers, industrial kilns and industrial heating furnaces, and has the effect of saving fuel.

(c)本发明中的改性燃料油稳定性非常好,在室温下放置6个月以上油水不分离,80℃放置3个月以上油水不分离。(c) The modified fuel oil in the present invention has very good stability, and the oil and water do not separate when placed at room temperature for more than 6 months, and when placed at 80° C. for more than 3 months.

(d)由于是乳化燃料,雾化非常好,燃烧完全,氮氧化合物、一氧化碳、挥发性有机化合物和因燃烧不完全形成的炭粒子等污染物排放少,能够达到国家规定的柴油锅炉大气污染物排放标准,是一类清洁燃料。在燃料中硫的含量比较高的情况下,通过加入适量脱硫剂,二氧化硫的排放能够达到国家规定的柴油锅炉大气排放标准。(d) Because it is an emulsified fuel, the atomization is very good, the combustion is complete, and the pollutants such as nitrogen oxides, carbon monoxide, volatile organic compounds and carbon particles formed due to incomplete combustion are less, and it can meet the air pollution of diesel boilers stipulated by the state. It is a kind of clean fuel. When the sulfur content in the fuel is relatively high, by adding an appropriate amount of desulfurizer, the emission of sulfur dioxide can meet the national emission standards for diesel boilers.

(e)本发明改性燃料油的制备方法的生产能力大,能够实现工业规模的生产。(e) The preparation method of the modified fuel oil of the present invention has a large production capacity and can realize industrial-scale production.

下面结合具体实施例,进一步阐述本发明。应理解,这些实施例仅用于说明本发明而不用于限制本发明的范围。下列实施例中未注明具体条件的实验方法,通常按照常规条件,或按照制造厂商所建议的条件。Below in conjunction with specific embodiment, further illustrate the present invention. It should be understood that these examples are only used to illustrate the present invention and are not intended to limit the scope of the present invention. For the experimental methods without specific conditions indicated in the following examples, the conventional conditions or the conditions suggested by the manufacturer are usually followed.

实施例1Example 1

(1)原料:重油-进口180号重油,(1) Raw materials: heavy oil - imported heavy oil No. 180,

         国产0号柴油,  Domestic No. 0 diesel oil,

         自来水。Tap water.

(2)配料配方(重量,吨):(2) Ingredients formula (weight, tons):

         180号重油-45,  No. 180 Heavy Oil - 45,

         0号柴油-45,Diesel No. 0 - 45,

         水-10。Water - 10.

(3)物料流量(公斤/小时):(3) Material flow rate (kg/hour):

         重油-1800,柴油-1800,水-400。Heavy oil - 1800, diesel - 1800, water - 400.

(4)物料温度(℃):(4) Material temperature (°C):

       重油-50,柴油-50,水-50。Heavy oil - 50, diesel - 50, water - 50.

(5)设备:混和超细研磨机(上海精微粉溶机械设备有限公司,CN01109394.3)。(5) Equipment: mixing ultrafine grinder (Shanghai Fine Powder Dissolution Machinery Equipment Co., Ltd., CN01109394.3).

(6)制备步骤:将180号重油和水按上面的温度和流量用液体输送泵同时送入上述的研磨乳化机,进行研磨乳化,制成乳化重油。再将柴油和制备好的乳化重油同时送入下一台串联的研磨乳化机,进行混合研磨,制备出改性燃料油,研磨乳化过程是连续作业。乳化重油的温度在50-60℃之间,流量在2200公斤/小时,柴油的温度在50℃,流量在1800公斤/小时。(6) Preparation step: send No. 180 heavy oil and water into the above-mentioned grinding and emulsifying machine at the same time according to the above temperature and flow rate with a liquid delivery pump, and carry out grinding and emulsification to make emulsified heavy oil. Then the diesel oil and the prepared emulsified heavy oil are simultaneously sent to the next grinding and emulsifying machine in series for mixing and grinding to prepare modified fuel oil. The grinding and emulsifying process is a continuous operation. The temperature of the emulsified heavy oil is between 50-60°C and the flow rate is 2200 kg/hour, the temperature of the diesel oil is 50°C and the flow rate is 1800 kg/hour.

(7)改性燃料油产品指标(7) Indicators of modified fuel oil products

外观:黑色流动性良好的液体,Appearance: black liquid with good fluidity,

密度(20℃)(公斤/立方米):921.7Density (20°C) (kg/m3): 921.7

运动粘度(40℃)(mm2/s):20Kinematic viscosity (40°C) (mm2/s): 20

闪点(闭口杯)(℃):≮80Flash point (closed cup) (°C): ≮80

灰分(重量%):<0.10Ash (weight%): <0.10

机械杂质(重量%):≤0.15Mechanical impurities (weight%): ≤0.15

稳定性-室温(20℃)放置6个月以上油水不分离,80℃放置3个月以上油水不分离。Stability - no separation of oil and water at room temperature (20°C) for more than 6 months, and no separation of oil and water at 80°C for more than 3 months.

改性燃料油中水滴粒径:0.1-3微米范围,95%小于2微米。Water droplet size in modified fuel oil: 0.1-3 microns, 95% less than 2 microns.

固体平均颗粒度:1-3微米。Solid average particle size: 1-3 microns.

[注:本发明中有关颗粒度分析使用激光粒度分析仪。该仪器光源为氦氖激光器,波长为0.6328μm,功率为2mW。样品用汽油稀释,汽油作为介质。利用粒子的对光的散射理论,粒子大小不同,散射角度也不同,在不同散射角度测定散射光的强度,用计算机处理,给出粒子的平均粒径尺寸和分布。此处的平均粒度取累积分布为50%的粒径,以下实施例同。][Note: the relevant particle size analysis in the present invention uses a laser particle size analyzer. The light source of the instrument is a helium-neon laser with a wavelength of 0.6328μm and a power of 2mW. The samples were diluted with gasoline, and gasoline was used as the medium. Using the light scattering theory of particles, the particle size is different, the scattering angle is also different, the intensity of scattered light is measured at different scattering angles, and the average particle size and distribution of the particles are given by computer processing. The average particle size here is taken as the particle size of 50% of the cumulative distribution, and the following examples are the same. ]

(8)燃烧性能:将制备好的改性燃料油在某企业4吨的柴油蒸汽锅炉上燃烧,不改变锅炉的设置和原有的燃烧器,控制改性燃料油的温度在40-50℃之间,过滤器不发生堵塞,喷嘴不发生堵塞,雾化很好,燃烧充分,火焰白亮,没有黑烟,运转1个月,喷油嘴和炉膛内没有积碳和积灰。(8) Combustion performance: Combust the prepared modified fuel oil on a 4-ton diesel steam boiler in a certain company, without changing the boiler settings and the original burner, and control the temperature of the modified fuel oil at 40-50°C During the period, the filter was not clogged, the nozzle was not clogged, the atomization was good, the combustion was sufficient, the flame was white and bright, and there was no black smoke. After one month of operation, there was no carbon and ash deposit in the fuel injector and the furnace.

实施例2Example 2

(1)原料:重油同实施例1,柴油同实施例1,水同实施例1。(1) raw material: heavy oil is with embodiment 1, and diesel oil is with embodiment 1, and water is with embodiment 1.

乳化剂-聚氧化乙烯月桂醇醚和山梨糖醇三硬脂酸酯。Emulsifiers - Polyoxyethylene Lauryl Ether and Sorbitan Tristearate.

(2)原料配方(重量,吨):重油-42.5,柴油-42.5,水-15。乳化剂用量为改性燃料油重量的0.3%(两种乳化剂按50:50配比)。(2) Raw material formula (weight, ton): heavy oil-42.5, diesel oil-42.5, water-15. The dosage of the emulsifier is 0.3% of the weight of the modified fuel oil (the ratio of the two emulsifiers is 50:50).

(3)原料流量(公斤/小时):重油-1700,柴油-1700,水-600。(3) Raw material flow rate (kg/hour): heavy oil-1700, diesel-1700, water-600.

(4)原料温度(℃):同实施例1。(4) Raw material temperature (°C): same as Example 1.

(5)研磨乳化设备:同实施例1。(5) Grinding and emulsifying equipment: the same as in Example 1.

(6)制备程序:先将乳化剂与水混合,制成乳化剂浓度为2%的混合液,然后将这一乳化剂和水的混合液与重油混合研磨乳化,制成乳化重油,乳化重油再与柴油混合研磨制备成改性燃料油。(6) Preparation procedure: first mix the emulsifier with water to make a mixed solution with an emulsifier concentration of 2%, then mix the mixed solution of the emulsifier and water with heavy oil to grind and emulsify to make emulsified heavy oil, emulsified heavy oil It is then mixed with diesel oil and ground to prepare modified fuel oil.

(6)产品指标(6) Product indicators

    外观:黑色流动性良好的液体, Appearance: black liquid with good fluidity,

    密度(20℃,公斤/立方米):923.8Density (20°C, kg/m3): 923.8

    运动粘度(40℃,mm2/s):17Kinematic viscosity (40°C, mm2/s): 17

    闪点(闭口杯,℃):≮80  Flash point (closed cup, °C): ≮80

    灰分(重量%):<0.10Ash content (weight%): <0.10

    机械杂质(重量%):≤0.15  Mechanical impurities (weight%): ≤0.15

    稳定性:室温(20℃)下放置6个月以上油水不分离, Stability: Oil and water will not separate when placed at room temperature (20°C) for more than 6 months.

           80℃放置3个月以上油水不分离。  The oil and water will not separate when stored at 80°C for more than 3 months.

    乳液中水滴粒径:0.1-3微米范围(>99%),95%小于 The particle size of water droplets in the emulsion: 0.1-3 micron range (>99%), 95% is less than

                   1.8微米。1.8 microns.

    固体平均颗粒度:小于3微米  Average particle size of solids: less than 3 microns

(7)燃烧性能:将制备好的改性燃料油在某企业6吨的柴油蒸汽锅炉上燃烧,不改变锅炉的设置和原有的燃烧器,控制改性燃料油的温度在40-50℃之间,过滤器不发生堵塞,喷嘴不发生堵塞,雾化很好,燃烧充分,火焰白亮,没有黑烟,运转2个月,喷油嘴和炉膛内没有积碳和积灰。(7) Combustion performance: Combust the prepared modified fuel oil on a 6-ton diesel steam boiler in a certain company, without changing the boiler settings and the original burner, and control the temperature of the modified fuel oil at 40-50°C During the period, the filter was not clogged, the nozzle was not clogged, the atomization was good, the combustion was sufficient, the flame was white and bright, and there was no black smoke. After 2 months of operation, there was no carbon and ash deposit in the fuel injector and the furnace.

实施例3Example 3

(1)原料:重油-进口180号低硫重油(实测硫含量0.8%),柴油、水同实施例1,不用乳化剂。(1) Raw material: heavy oil-import No. 180 low-sulfur heavy oil (measured sulfur content 0.8%), diesel oil, water are the same as embodiment 1, without emulsifier.

      脱硫剂-活性超细轻质碳酸钙。  Desulfurizer - active superfine light calcium carbonate.

(2)原料配方(重量,吨):重油-36,柴油-54,水-10。含钙脱硫剂用量控制在钙与油中硫的化学计量比为1.5比1。(2) Raw material formula (weight, ton): heavy oil-36, diesel oil-54, water-10. The dosage of calcium-containing desulfurizer is controlled so that the stoichiometric ratio of calcium to sulfur in oil is 1.5 to 1.

(3)物料流量(公斤/小时):重油-1440,柴油-2160,水-400。(3) Material flow rate (kg/hour): heavy oil-1440, diesel-2160, water-400.

(4)物料温度:重油、柴油、水-80℃,碳酸钙-室温。(4) Material temperature: heavy oil, diesel oil, water -80°C, calcium carbonate - room temperature.

(5)乳化设备:同实施例1。(5) emulsification equipment: with embodiment 1.

(6)制备程序:先按实施例1的程序制备出无脱硫剂的改性燃料油,再加入脱硫剂与其混合研磨两遍,制备出含脱硫剂的改性燃料油。(6) Preparation procedure: first prepare modified fuel oil without desulfurizing agent according to the procedure in Example 1, then add desulfurizing agent and grind it twice to prepare modified fuel oil containing desulfurizing agent.

(7)产品指标(7) Product index

   外观:黑色粘性流体。Appearance: black viscous fluid.

   密度(20℃,公斤/立方米):965.1Density (20°C, kg/m3): 965.1

   运动粘度(40℃,mm2/s):35Kinematic viscosity (40°C, mm2/s): 35

   闪点(闭口杯,℃):≮80  Flash point (closed cup, °C): ≮80

   稳定性:室温(20℃)下放置6个月以上,油水不分离;Stability: oil and water will not separate when placed at room temperature (20°C) for more than 6 months;

           80℃放置3个月以上油水不分离。  The oil and water will not separate when stored at 80°C for more than 3 months.

   改性燃料油中的水滴粒径:0.5-3微米范围(>99.9%的 Water droplet size in modified fuel oil: 0.5-3 micron range (>99.9%

                          水),95%小于2微米。water), 95% less than 2 microns.

   固体平均颗粒度:小于3微米。  Average particle size of solids: less than 3 microns.

(8)燃烧性能:将制备好的改性燃料油在某企业6吨的柴油蒸汽锅炉上燃烧,不改变锅炉的设置和原有的燃烧器,控制改性燃料油的温度在40-50℃之间,过滤器不发生堵塞,喷嘴不发生堵塞,雾化很好,燃烧充分,火焰白亮,没有黑烟,运转1个月,喷油嘴和炉膛内没有积碳和积灰。(8) Combustion performance: Combust the prepared modified fuel oil on a 6-ton diesel steam boiler in a certain company, without changing the boiler settings and the original burner, and control the temperature of the modified fuel oil at 40-50°C During the period, the filter was not clogged, the nozzle was not clogged, the atomization was good, the combustion was sufficient, the flame was white and bright, and there was no black smoke. After one month of operation, there was no carbon and ash deposit in the fuel injector and the furnace.

(9)除硫效率:与未加脱硫剂的改性燃料相比,烟气中二氧化硫初始排放浓度减少53%。(9) Sulfur removal efficiency: Compared with the modified fuel without adding desulfurizer, the initial emission concentration of sulfur dioxide in the flue gas is reduced by 53%.

实施例4-7Example 4-7

按照实施例1相同方法,制备以下配方的燃料油:According to the same method of embodiment 1, prepare the fuel oil of following formula:

  实施例4 实施例5 实施例6 实施例7 重油(kg) 10 70 40 60 柴油(kg) 90 30 60 40 水(kg) 5 20 8 15 乳化剂*(kg) 0 0.5 0.2 0.3 脱硫剂**(kg) 0 0 0 0 Example 4 Example 5 Example 6 Example 7 Heavy oil (kg) 10 70 40 60 Diesel (kg) 90 30 60 40 water (kg) 5 20 8 15 Emulsifier*(kg) 0 0.5 0.2 0.3 Desulfurizer**(kg) 0 0 0 0

*乳化剂为聚氧化乙烯月桂醇醚和山梨糖醇三硬脂酸酯(50:50)。*Emulsifiers are polyoxyethylene lauryl ether and sorbitan tristearate (50:50).

**脱硫剂为活性超细轻质碳酸钙。**The desulfurizer is active superfine light calcium carbonate.

结果同样获得了黑色粘性液体状的燃料油,而且在室温(20℃)下放置6个月以上,油水不分离;80℃放置3个月以上油水不分离。实施例4-7的各改性燃料油中的水滴粒径:0.5-3微米范围,95%小于2微米。固体平均颗粒度:1-3微米。As a result, black viscous liquid fuel oil was also obtained, and the oil and water did not separate when placed at room temperature (20° C.) for more than 6 months; the oil and water did not separate when placed at 80° C. for more than 3 months. The particle size of water droplets in each of the modified fuel oils of Examples 4-7: in the range of 0.5-3 microns, 95% of which are less than 2 microns. Solid average particle size: 1-3 microns.

在本发明提及的所有文献都在本申请中引用作为参考,就如同每一篇文献被单独引用作为参考那样。此外应理解,在阅读了本发明的上述讲授内容之后,本领域技术人员可以对本发明作各种改动或修改,这些等价形式同样落于本申请所附权利要求书所限定的范围。All documents mentioned in this application are incorporated by reference in this application as if each were individually incorporated by reference. In addition, it should be understood that after reading the above teaching content of the present invention, those skilled in the art can make various changes or modifications to the present invention, and these equivalent forms also fall within the scope defined by the appended claims of the present application.

Claims (11)

1. modified fuel oil is characterized in that it contains:
(a) heavy oil of 10-70 parts by weight;
(b) diesel oil of 30-90 parts by weight; With
(c) water,
Wherein, the total amount of heavy oil and diesel oil is 100 weight parts, and the weight ratio that water and heavy oil add between total oil of diesel oil is 5:95-30:70; Water more than 98% exists with the water droplet form of particle diameter 0.1-3 micron, and the mean particle size of solid particulate matter is the 1-5 micron in the oil, and wherein the water more than 95% exists with the water droplet form of particle diameter less than 2 microns.
2. modified fuel oil as claimed in claim 1 is characterized in that, the mean particle size of solid particulate is the 1-3 micron.
3. modified fuel oil as claimed in claim 1 is characterized in that, the weight ratio that water and heavy oil add between total oil of diesel oil is 8:92-20:80.
4. modified fuel oil as claimed in claim 1, it is characterized in that, described heavy oil is selected from: No. 4 to No. 7 oil fuel, the oils of the coal tar of No. 180 heavy oil, No. 380 heavy oil, No. 250 heavy oil, residual oil, non-petroleum sources, shale oil, plant origin, the oils of animal-origin, waste oil and composition thereof.
5. modified fuel oil as claimed in claim 1 is characterized in that, described diesel oil is selected from down group: marine diesel oil, No. 10 to negative No. 50 solar oil, and composition thereof.
6. modified fuel oil as claimed in claim 1 is characterized in that, described wet concentration is from alkalescent water or the hard water of fresh water, trade effluent, pH value 4-6 weakly acidic water, pH value 8-11.
7. modified fuel oil as claimed in claim 1 is characterized in that, described oil fuel is placed more than 6 months down at 20 ℃, and profit does not separate; Or place at 80 ℃ that profit does not separate more than 3 months.
8. modified fuel oil as claimed in claim 1 is characterized in that, also contains the additive of organizing under being selected from of 0.01-10 parts by weight: emulsifying agent, sweetening agent.
9. modified fuel oil as claimed in claim 1 is characterized in that, described oil fuel is by the heavy oil of (a) 10-70 parts by weight; (b) diesel oil of 30-90 parts by weight; (c) water is formed.
10. the preparation method of a modified fuel oil is characterized in that, this method may further comprise the steps:
(i) with the heavy oil of (a) 10-70 parts by weight, the diesel oil and (c) the water mixing of (b) 30-90 parts by weight, form raw mix, wherein the total amount of heavy oil and diesel oil is 100 weight parts, and water and heavy oil add weight ratio between total oil of diesel oil be 5:95-30:70 and
(ii) raw mix is ground, the above water of in the fuel 98% is existed with the water droplet form of particle diameter 0.1-3 micron, and the mean particle size of solid particulate matter is the 1-5 micron to the particle diameter of the water droplet more than 95% less than 2 microns, thereby obtains modified fuel oil.
11. the preparation method of a modified fuel oil, it is characterized in that, this method comprise with the diesel oil of heavy oil (b) the 30-90 parts by weight of (a) 10-70 parts by weight and (c) water send into grinding plant and grind, wherein the total amount of heavy oil and diesel oil is 100 weight parts, and the weight ratio that water and heavy oil add between total oil of diesel oil is 5:95-30:70, water more than 98% in the fuel is existed with the water droplet form of particle diameter 0.1-3 micron, and the mean particle size of solid particulate is the 1-5 micron to the particle diameter of the water droplet more than 95% less than 2 microns, thereby obtains modified fuel oil.
CNB2004100662751A 2004-09-10 2004-09-10 Modified fuel oil and production thereof Expired - Fee Related CN100513534C (en)

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CN101168684A (en) * 2007-11-01 2008-04-30 姜万兴 Emulsified oil
CN101805645A (en) * 2010-04-08 2010-08-18 浙江中赢节能环保科技有限公司 Emulsification, combustion and desulphurization process of industrial heavy fuel

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