201243244 六、發明說明： 【發明所屬之技術領域】 本發明是有關於一種燃油處理設備，特別是指一種提 供燃燒器使用之燃油的燃油乳化裝置。 【先前技術】 一般燃油（重油、柴油、渣油）乳化燃燒技術是以“ 微爆”理論為基礎，該技術是在燃油中（重油、柴油、浩 油）加入乳化劑，將水以很小的顆粒分散於油中，形成油 包水型（W/0)乳狀液（不大於5um的顆粒占82%以上）。 用高壓泵將乳化油經一次霧化以霧狀噴入燃燒爐時，表面 的油一旦燃燒，油内的水珠即被加熱氣化，體積急劇膨脹 ，瞬間把油滴爆開（形成二次霧化），產生“微爆效應”。 由於二次霧化使油滴碎裂成更細小的霧狀油滴，此時油滴 比表面積大，可與空氣中的氧充分接觸燃燒，縮短燃燒時 間，從而使重油燃燒更完全，火焰更明亮，提高了熱效率 ，消除了黑煙，達到節油的目的。乳化水在燃燒過程中形 成的水蒸氣，在高溫下與燃燒中的碳發生化學反應，生成 水煤氣，水煤氣再燃燒，增加了燃燒放熱量，並可消除黑 煙 防止結焦’還能將原有的結焦清除，且燃燒中產生 的大量水蒸氣是三元子氣體，可進一步加強熱傳導和熱輻 射’改善傳熱效果。 重質燃料油在工業爐、窯爐、船用鍋爐等熱能動力設 備上使用廣泛，但因其含有大量的膠質，瀝青質，在與氧 充分接觸前受熱（65(TC )裂解而生成炭黑（析炭）。當空 3 201243244 氣不足或混合JC Λ：Ζ1 η 士 害設備正常；Γ二炭黑來不及燃燒而引起冒黑煙，妨 的能源短缺和㈣失和隨著世界性 發節約能源的各:方：:的來臨，國内外都在尋求和開 料代替重污= 城市以油代煤，以清潔燃 木-料的發展趨勢很快。因此，改 油的燃燒質量，不彳g 、 置貨燃枓 十生產企業具有很大的經濟效 量具有重大的社會意義。燃心二 減排技術’它不僅節約能源，而且能減 θ :、低煙氣中硫化物、氮氧化合物和煙塵的含 置。 高的燃燒效率是高熱效率的前提，全自動比例辦燒裝 =加，燃燒效率達到99%以上，但這種燃燒器結 可較尚’因而並未得到廣泛的運用。乳化燃油 ^燃油的燃燒效率，節省燃料，乳化油的微爆效應 產生的超霧化作用是在燃燒過程中實現的，並不需要好的 霧化6又備’⑨就為普通燃油燃燒器燃燒效率的提高提供了 ^好的條件。實際上也為普通燃燒器找到了使用市場:使 得加熱爐在燃燒系統的投f上可以達到節資增效的目的。 隨著技術的發展和進步’各國都不僅對燃燒爐的熱效 率設計提出了嚴格的規定，而且要求其在燃燒上達到三廢 排放標準’在滿足熱負荷的前提下，儘量佔用較少的空間 。乳化油的燃燒不僅能利用其微爆效應強化爐内燃燒，而 且微爆效應產生的爐内較強的搜動和擾流增強了爐内的對 流換熱效果。過熱水蒸氣能夠增大輻射室㈣氣的濃度， 201243244 強化了輻射換熱’使得爐膛單位體積的熱流密度增大，提 向了單位鋼材的熱負荷能力’這樣就可以減少爐體的換熱 面積’從而減少輻射室和對流室的鋼材耗量，從結構上帶 動燃燒爐的革新與改進，降低爐子的造價。另外，在燃燒 過程中摻入的水在爐内氣化吸熱，使火焰中心局部溫度下 降且趨於均勻，實現低溫燃燒，有利於減少氮氧化物和硫 氧化物的生成，達到環保的要求。高溫下，水蒸氣與未完 全燃燒的炭粒發生水煤氣反應。水煤氣反應雖不增加燃料 的可燃成分，但可提高可燃成分的燃燼率，使實際發熱量 k加油霧中水蒸氣的存在，產生大量的氫氧離子，可以 加快co的燃燒，從而減小過剩空氣係數。這樣，因空氣加 熱和由煙道氣帶走的熱量都相應減少。料，水變成蒸汽 後會產生:種汽提效應，能除去c〇2、N2等惰性氣體在油 商表面开乂成的氣膜，加快燃燒過程和熱的傳導，提高傳熱 效率。同時’上述反應減少了火焰中的炭粒，提高了進料 的燃燒效率，從而達到了節能的目的。 目别’雖然國内外對燃油摻水乳化技術的應用研究較 多，但對乳化後的燃油物性變化影響因素的系統研究卻很 少。因此’對乳化燃油的實際應用缺少理論性指導 液的物性不僅盥遠螬相古a 狀 -連、，相有關’而且與分散相、分散相的加 入置以及》散相的分散性和微粒粒徑.有關。 —在工業生產和科學研究中，必須用一定的 = ㈣合方式或分散手段直= 狀液的穩定性。 I礼 201243244 乳化油常用的乳化方式主要有以下幾種方式： 1·多層I網式乳化：該方法在實際應用中較為常見，但 由於對/由資、油溫要求較高，故在實際生產中運行並不理 想。 2·機械㈣乳化：該方法通過在—定溫度下將油水授摔 而使其混合均句，達到乳化之效果，仙頻率不高（不高 於5〇〇HZ)㈣器轉速一般不超過3000r/min，導致乳化 顆粒大小不-，分散不均句，易於分層，㈣進—步加強 改進。 3.電超聲波乳化：該方法具有較高的穩定性，且在高頻 ( 20000Hz左右）震蘯下可產生強制壓縮乳化顆粒細小均句 ，不易分層。但該法需要高頻振盪源，故實踐中不常用。 4·脊片。肖超聲乳化：油和水按__定比例通過喷嘴高速喷 士迎面衝擊固定在支座上的簧片’使之產生振動發射出 超聲波’以迫使油水激烈分散。其頻率大、約5GGGHZ，乳化 效果較機械搜拌好，但簧片壽命短，實踐中採用也較少。 5·靜態乳化益.乳化器内有特殊的乳化單元，且結構簡 "’、何運動邛件，因此被廣泛的運用於各種工業裝置中 〇 _ 髙剪切乳化機：高剪切分散乳化就是高效、快速 、均句地將—個相或多個相(液體、固體、氣體)進入到另一 互^目溶的連續相（通常液體）的過程。而在通常情況下各個 不相'合的。當外部能量輸入時’兩種物料重組成為 " 由於轉子间速旋轉所產生的高切線速度和高頻機 201243244 械效應帶來的強勁動能’使物料在定、轉子狹窄的間隙中 受到強烈的機械及液力剪切、離心擠壓、液層摩擦、撞擊 撕裂和湍流等综合作用，形成懸浮液（固/液），乳液（液體 /液體）和泡珠（氣體/液體）。從而使不相溶的固相、液相 、氣相在相應成熟工藝和適量添加劑的共同作用下，〜瞬間 均勻精細的分散乳化’經過南頻的循環往復，最終得到穩、 定的高品質產品。因此，也廣泛的被運用。 以上幾種乳化方式，在實踐中均有運用，但由於裝置 結構的複雜性及運行維護的高要求性，致使其應用都受到 一定的限制’而無法大量的推廣。 【發明内容】 囚此，不發明之目的，即在提供一種不需要添加乳化 劑且可達到良好的燃燒效果的燃油乳化裝置。 於是，本發明的燃油乳化裝置包含一燃油管路、一供 水管路、-混合槽、一第一乳化裝置、一第二乳化裝置及 儲存槽D亥混合槽連結該燃油管路與該供水管路，並具 有—可將混合後的燃油與水送出的引出管路，該第一減 裝置可將該燃油與水進 缺物土 弟_人礼化，並具有一與該引出 官路相連通的第一入口 $ γ # 細及弟一出口端，該第二乳化裝 置可將該燃油與水逸杆笛—一 第一二人乳化，並具一與該第一出口 %相連通的第二入口媿 ,U . —可排出混合油液的第二出口端 該儲存槽與該第二出口 ,^相連通，用於儲放混合油液。 再利用該第―、二乳j昆合槽先將燃油與水混合後， 裝置依序進行第一、二次乳化，則 7 201243244 可使燃油與水充分乳化，並可達到良好燃燒效果。 【實施方式】 有關本發明之前述及其他技術内容、特點與功效，在 以下配合參考圖式之一個較佳實施例的詳細說明中，將可 清楚的呈現。 如圖1所示，本發明燃油乳化裝置之較佳實施例，包 含一燃油管路10、一供水管路20、一混合槽30、一調節閥 4〇、一預乳化裝置50、一第一乳化裝置60、一第二乳化裝 置70及一儲存槽。 該燃油管路1 〇用於供導送燃油（重油、柴油、渣油） ，且依導送方向在該燃油管路1〇上安裝有一油過濾器u、 一電磁調節閥12及一流量計13。 該供水管路20用於供導送水，且依導送方向在該供水 f路20上安裝有一電加熱器24、一球閥21、一電磁調節 閥22及一流量計23 〇 該混合槽30連結於該燃油管路1 〇與該供水管路2〇， 且相鄰於該流量計13、23，並具有一可將混合後的燃油與 水送出的引出管路31。該引出管路31末端分設有一第一流 道3 11及一第二流道312，該第一流道；311連通至該預乳化 裝置50,該第二流道312連通至該第一乳化裝置60。該第 二流道312又設有一第一分流管313、一第二分流管314、 —分別接通至該第一、二'分流管313、314的歧管315及多 數分別設置在該第一、二分流管313、314與該等歧管315 的手動閥316。該第二分流管314還具有一可連通至該混合201243244 VI. Description of the Invention: [Technical Field] The present invention relates to a fuel processing apparatus, and more particularly to a fuel emulsification apparatus for providing fuel for use in a burner. [Prior Art] General fuel (heavy oil, diesel, residual oil) emulsified combustion technology is based on the "micro-explosive" theory, which is to add emulsifier in the fuel (heavy oil, diesel, Hao oil), the water is very small The particles are dispersed in the oil to form a water-in-oil (W/0) emulsion (particles of no more than 5 um account for more than 82%). When the emulsified oil is sprayed into the combustion furnace by atomization by a high-pressure pump, once the oil on the surface is burned, the water droplets in the oil are heated and vaporized, and the volume is rapidly expanded, and the oil droplets are suddenly exploded (formed twice). Atomization), resulting in a "micro-explosion effect." Due to the secondary atomization, the oil droplets are broken into finer misty oil droplets. At this time, the oil droplets have a large specific surface area and can be fully contacted with oxygen in the air to burn, shortening the burning time, thereby making the heavy oil burn more completely, and the flame is more complete. Bright, improved thermal efficiency, eliminated black smoke, and achieved fuel economy. The water vapor formed by the emulsified water in the combustion process chemically reacts with the burning carbon at a high temperature to generate water gas, the water gas is reburned, the combustion heat is increased, and the black smoke is prevented from coking, and the original The coke is removed, and a large amount of water vapor generated in the combustion is a ternary gas, which further enhances heat conduction and heat radiation to improve the heat transfer effect. Heavy fuel oil is widely used in thermal power equipment such as industrial furnaces, kiln furnaces, and marine boilers. However, because it contains a large amount of colloid and asphaltenes, it is heated (65(TC) to form carbon black before being fully contacted with oxygen ( Carbonation). When the air 3 201243244 gas is insufficient or mixed JC Λ: Ζ1 η The equipment is normal; the Γ2 carbon black is too late to burn, causing black smoke, the energy shortage and (4) loss and the world's energy saving : Fang:: The coming, both domestic and foreign are seeking and cutting materials instead of heavy pollution = city to replace coal with oil, to clean the wood-materials development trend is very fast. Therefore, change the quality of oil burning, not g, set It is of great social significance to have a large economic efficiency of the fuel-burning production enterprise. It is not only energy-saving but also reduces θ: low sulfur content of sulfides, nitrogen oxides and soot. High combustion efficiency is the premise of high thermal efficiency. The automatic ratio is burned = plus, and the combustion efficiency is over 99%, but this burner knot can be compared. Therefore, it has not been widely used. Emulsified fuel ^ fuel Burning Efficiency, fuel saving, super-atomization caused by the micro-explosion effect of emulsified oil is realized in the combustion process, and does not require good atomization 6 and '9 is provided for the improvement of the combustion efficiency of ordinary fuel burners ^ Good conditions. In fact, the market has been found for ordinary burners: the heating furnace can achieve the purpose of saving money and increasing efficiency in the investment system of the combustion system. With the development and advancement of technology, all countries are not only on the combustion furnace. The thermal efficiency design puts forward strict regulations and requires it to meet the three waste discharge standards in combustion. Under the premise of satisfying the heat load, it takes up as little space as possible. The combustion of the emulsified oil can not only enhance the combustion in the furnace by using its micro-explosion effect. Moreover, the strong search and turbulence in the furnace caused by the micro-explosion effect enhances the convective heat transfer effect in the furnace. The superheated steam can increase the concentration of the radiation chamber (4), and 201243244 strengthens the radiation heat transfer to make the furnace unit volume The heat flux density is increased, and the heat load capacity of the unit steel is raised, so that the heat exchange area of the furnace body can be reduced, thereby reducing the radiation chamber and the convection chamber. The steel consumption drives the innovation and improvement of the furnace from the structure, and reduces the cost of the furnace. In addition, the water mixed in the combustion process vaporizes and absorbs heat in the furnace, so that the local temperature of the flame center decreases and tends to be uniform. Low-temperature combustion is beneficial to reduce the formation of nitrogen oxides and sulfur oxides and meet the requirements of environmental protection. At high temperatures, water vapor reacts with incompletely combusted carbon particles. The water gas reaction does not increase the combustible composition of the fuel, but can be improved. The burning rate of the combustible component causes the actual calorific value k to increase the presence of water vapor in the oil mist, generating a large amount of hydroxide ions, which can accelerate the combustion of the co, thereby reducing the excess air coefficient. Thus, due to air heating and by the flue gas zone The heat of the walk is reduced accordingly. After the water turns into steam, it will produce: a stripping effect, which can remove the gas film opened by the inert gas such as c〇2 and N2 on the surface of the oil merchant, and accelerate the combustion process and heat conduction. Improve heat transfer efficiency. At the same time, the above reaction reduces the carbon particles in the flame and improves the combustion efficiency of the feed, thereby achieving the purpose of energy saving. Although there are many researches on the application of fuel-in-water emulsification technology at home and abroad, there are few systematic studies on the factors affecting the change of fuel physical properties after emulsification. Therefore, the practical application of the emulsified fuel lacks the theoretical property of the liquid. It is not only related to the phase, but also related to the dispersed phase, the dispersed phase, and the dispersion and particle size of the dispersed phase. Path. Related. - In industrial production and scientific research, the stability of the liquid must be determined by a certain = (four) combination or dispersion means. I ceremony 201243244 The emulsification methods commonly used in emulsified oil are mainly as follows: 1. Multi-layer I mesh emulsification: This method is more common in practical applications, but due to the high requirements for the oil supply and oil temperature, it is actually produced. Running in the middle is not ideal. 2. Mechanical (4) Emulsification: This method achieves the effect of emulsification by mixing oil and water at a constant temperature to achieve the effect of emulsification. The frequency of the fairy is not high (not higher than 5〇〇HZ). (4) The rotational speed of the device generally does not exceed 3000r. /min, resulting in emulsified particle size is not -, uneven dispersion of the sentence, easy to stratify, (four) step by step to strengthen and improve. 3. Electro-acoustic emulsification: This method has high stability, and it can produce small-scale uniform squeezing of forced-compressed emulsified particles under high frequency (about 20,000 Hz) shock, which is not easy to stratify. However, this method requires a high-frequency oscillation source, so it is not commonly used in practice. 4 · spine. Xiao phacoemulsification: oil and water are slid into the yoke at a high speed by a nozzle at a high speed to impact the reeds fixed on the support to generate vibrations to emit ultrasonic waves to force the oil to be strongly dispersed. The frequency is large, about 5GGGHZ, and the emulsification effect is better than mechanical search, but the reed has a short life and is used less in practice. 5. Static Emulsifying Benefits. The emulsifier has special emulsifying units, and the structure is simple ", and sports parts, so it is widely used in various industrial devices. 〇 髙 Shear emulsifier: high shear dispersion emulsification It is a process of efficiently, quickly, and uniformly bringing one phase or phases (liquid, solid, gas) into another continuous phase (usually liquid). In the usual case, each does not match. When external energy is input, 'the two materials are reorganized into " The high tangential speed due to the inter-rotor speed rotation and the strong kinetic energy brought by the high-frequency machine 201243244 mechanical effect make the material strong in the narrow gap between the stator and the rotor. Mechanical and hydraulic shearing, centrifugal extrusion, liquid layer friction, impact tearing and turbulence combine to form a suspension (solid/liquid), an emulsion (liquid/liquid) and a bead (gas/liquid). Therefore, the incompatible solid phase, liquid phase, and gas phase are uniformly and finely dispersed and emulsified under the action of the corresponding mature process and an appropriate amount of additives, and the cycle is reciprocated through the south frequency to finally obtain a stable and high quality product. . Therefore, it is widely used. The above emulsification methods are used in practice. However, due to the complexity of the structure of the device and the high requirements for operation and maintenance, the application is subject to certain restrictions, and it cannot be widely promoted. SUMMARY OF THE INVENTION This object is not for the purpose of providing a fuel emulsification device which does not require the addition of an emulsifier and which achieves a good combustion effect. Therefore, the fuel emulsifying device of the present invention comprises a fuel line, a water supply line, a mixing tank, a first emulsifying device, a second emulsifying device, and a storage tank D-mixing tank connecting the fuel line and the water supply pipe. The road has a lead-out pipe that can send the mixed fuel and water, and the first reducing device can enter the fuel and the water into the body of the person, and has a connection with the lead-out road. The first inlet $ γ #细和弟一出口端, the second emulsifying device can emulsify the fuel with the water escaped flute - a first two persons, and has a second connected to the first outlet % The inlet port, U. - can discharge the second outlet end of the mixed oil. The storage tank is in communication with the second outlet, for storing the mixed oil. After the first and second emulsification are carried out by using the first and second milk j Kunhe tanks, the first and second emulsifications are carried out in sequence, and the 2012 201244 can fully emulsify the fuel and water, and achieve good combustion effect. The above and other technical contents, features, and advantages of the present invention will be apparent from the following detailed description of the preferred embodiments. As shown in FIG. 1 , a preferred embodiment of the fuel emulsifying device of the present invention comprises a fuel line 10 , a water supply line 20 , a mixing tank 30 , a regulating valve 4 , a pre-emulsification device 50 , and a first The emulsifying device 60, a second emulsifying device 70 and a storage tank. The fuel line 1 is used for guiding fuel (heavy oil, diesel, residual oil), and an oil filter u, an electromagnetic regulating valve 12 and a flow meter are installed on the fuel line 1〇 according to the guiding direction. 13. The water supply line 20 is used for guiding water, and an electric heater 24, a ball valve 21, an electromagnetic regulating valve 22 and a flow meter 23 are connected to the water supply path 20 according to the guiding direction. The mixing tank 30 is connected. The fuel line 1 is connected to the water supply line 2 and adjacent to the flow meters 13, 23, and has a lead-out line 31 for sending the mixed fuel and water. A first flow path 3 11 and a second flow path 312 are respectively disposed at the end of the lead-out line 31. The first flow path 311 is connected to the pre-emulsifying device 50, and the second flow path 312 is connected to the first emulsifying device 60. . The second flow channel 312 is further provided with a first shunt tube 313, a second shunt tube 314, a manifold 315 connected to the first and second 'shunt tubes 313 and 314, respectively, and a plurality of the first shunt tubes 313 and 314 respectively disposed at the first The two shunt tubes 313, 314 and the manual valve 316 of the manifolds 315. The second shunt tube 314 also has a connectable to the mixing
S 8 201243244 一的超聲波射流乳化器317β另外，該引出管路3 、加C泵32及二併聯設置的過濾器33。 —該預礼化裝置5G具有-與該第-流道311相連通 流前乳化器51及：超聲波後乳化器52,該等後乳化器5 f匕m置出且分別與該前乳化器51呈串聯設置，該等後乳 化裔2的出口端與該混合槽30連通。 °亥第一礼化裝置60具有—與該引出管路31的 ★ 道312相連通的第—入口端61及-與該第-入口端 反的第-出…2。本實施例的第一乳化裝置 目 射流乳化器63。 又 …該第一礼化裝i 7〇具一與該第一出口端Μ相連通的 第 端71及一可排出混合油液的第二出口端72。本實 轭例的第一礼化裝置7〇具有一超聲波乳化器73、—射流言 剪=乳化器74及-流量計75，該超聲波乳化器73與該: 流高剪切乳化器74可採串聯或併聯設置。 該調節閥40設置在該第一乳化裝置6〇與該第二乳化 裝置7〇之間’該調節閥4〇可透過該第-分流管313連通 至該第二乳化裝置70。 上述該第一乳化裝置60、該第二乳化裝置70及該預乳 化裝置50可採用多層遽網式乳化器、機械義乳化器、電 超聲波乳化器、簧片哨超生波乳化器、靜態乳化器、射流 鬲剪切乳化器或任二種以上的組合。 再如圖1所示，本發明的乳化作業流程為：燃油自該燃 油管路10導入之前已預先加熱且達到預期的流動性， 201243244 該燃油管路10導入後，會依序經過該油過濾器u、電磁調 節閥12、流量計13進入該混合槽3〇中，同時，水自該供 水管路20導入後，經該電加熱器24加熱至燃油同等溫度 後依次經過該球閥21、該電磁調節閥22、該流量計23進 入該混合槽30，且透過該電磁調節閥12、22和流量計13 、23，可按照一可程式邏輯控制器（pLC)【圖未示】中所設 定之油水混合比例值分別調節進油量與進水量。 接著，當燃油經由該燃油管路1〇、水經由該供水管路 20導送至該混合槽3〇混合後，燃油與水混合物可自該引出 管路31排出，且利用該加壓泵32循環加壓及該過濾器η 過濾後，會再分成兩路。一路經過該第一流道3ιι及該預乳 化裝置50的前乳化器51及該等後乳化器52進行預乳化後 進入該混合槽3G中，如此循環，可達到油水龍合、初步 乳化效果》另一路則經過該第二流道312進入該第一乳化 裝置60進行乳化，隨後，再透過該調節閥4〇的開度來調 節燃油與水混合物的淥量，且燃油與水混合物會再進入該 第一乳化裝置70的超聲波乳化器73進一步乳化，可直接 輸導至該儲存槽8G或供現場使用。或者，燃油與水混合物 可依序經過該超聲波乳化$ 73 &該射流高剪切乳化器74 乳化後進入儲存槽80或經該燃油出口 81供現場使用。 當該調節閥40發生故障或檢修時可通過該等手動閥 316調節來實現手動控制。 另外’在該預乳化裝置50的前乳化器51、該第—乳 化裝置60 、該超聲波乳化器73後分別設置一聲強檢測裝 10 201243244 置90 ’可以瞭解燃油乳化效果。 设備停機後，排盡設備及管路内餘油後關閉一設於該 燃油官路10的控制閥1〇3，再由一設於該控制閥1〇3與該 油過濾器11之間的蒸汽吹掃口 101接入蒸汽，並利用蒸汽 對設備及管路進行清洗吹掃至該儲存槽80内，再將儲存槽 80内積水經-排污口 82排出。使得設備及管路内無殘留燃 油。 且設備進出口之間設置一旁路1〇2，亦即在該燃油管路 10與該第二出Π端72之間設置該旁路1G2，則可在該燃油 乳化裝置檢修或更換時，不影響燃燒設備正常的運作。 本發明的功效為： 一、 利用該預乳化裝置50、該第一乳化裝置6〇、該第 -乳化裝置7G的設置，以及流體本身的射流動力，產生高 強度的聲波和超聲波在流體中傳播，聲強達到一定強度時 ’在流體中產生空化效應’令重油的分子鏈發生裂解和重 組’與水產生乳化作用，㈣水為分散相、油為連續相的 油包水型W/0㈣浮而不分離的乳域。乳化油中水顆粒 分佈均勻、粒度細、性能穩H乏用於重油、渣油及煤 焦油的掺水乳化需添加任何添加劑。亦即，經過三合 一高效燃油乳化技術處理的燃油乳化顆粒細 可達_上，細度料比㈣，嶋效果就= ，在鬲的燃燒效率就是高的熱效率的前提下，三合一的乳 化燃油能使加熱爐的燃盡效率達到99%以上。 二、 乳化後的燃油燃燒時’由於是油包水的顆粒，會 201243244 產生人霧化即微爆效應，達到良好的燃燒效果。火焰溫 度升尚、火焰變短、燃燒完全，調整參數更寬。提高了燃 燒器（例如鍋爐）的整體熱效率，節油率提高，更降低了煙氣 中有害氣體的排放，完全達到環境排放標準。 三、 適用於燃燒重油、渣油或煤焦油的大多數工業鍋 爐、工業爐寞、柴油發電機組，可在線乳化及製備。 四、 燃油粘度越高，摻水率越高，節油降汙效果越大 。最大摻水率達30%，最大節油率達25%，明顯降低一氧 化碳co，硫氧化物S0x，氮氧化物Ν〇χ排放，降低了有害 殘留物，減少對機體的腐触。乳化燃油的燃燒狀態與錢 相比，火焰短而強度大，呈白熾狀態，燃燒速度加快，爐 體内無混濁煙塵現象，燃燒充分並且穩定，爐尾積灰大大 減少。 五、 礼化燃油所具有的充分燃燒特性，使積碳和結焦 現象明顯下降，可起到保護爐體、延長爐子使用的壽命*， 降低維護保養工作的勞動強度，並且不會造成機械設備的 任何腐飯。 六、 使用乳化燃油不需改變原有供油系統和燃燒裝置 ’只需對個別X藝溫度及配.風條件進行適當調整即可，且 可根據使用環境和油品情況隨時調節處理量及加水量，適 用於不同油品^ 七、 該第二乳化裝置7〇的超聲波乳化器73及該射流 髙剪切乳化器74可透過閥門實現串聯或各自單獨工作，從 而貫現不停機檢修或更換零件。The ultrasonic jet emulsifier 317β of S 8 201243244 is additionally provided with the lead line 3, the C pump 32 and the filter 33 arranged in parallel. The pre- ritualizing device 5G has a pre-flow emulsifier 51 and an ultrasonic post-emulsifier 52 connected to the first flow path 311, and the post-emulsifier 5 f匕m is disposed and respectively associated with the pre-emulsifier 51 Arranged in series, the outlet end of the post-emulsion 2 is in communication with the mixing tank 30. The first ritual device 60 has a first inlet end 61 that communicates with the dao 312 of the outlet line 31 and a first-out end 2 that is opposite the first inlet end. The first emulsifying device of the present embodiment is a jet emulsifier 63. Further, the first attire i 7 has a first end 71 that communicates with the first outlet end 及 and a second outlet end 72 that discharges the mixed oil. The first ritual device 7 of the present yoke example has an ultrasonic emulsifier 73, a jet flow slash = an emulsifier 74 and a flow meter 75, and the ultrasonic emulsifier 73 and the flow high shear emulsifier 74 can be used. Set in series or in parallel. The regulating valve 40 is disposed between the first emulsifying device 6 and the second emulsifying device 7'. The regulating valve 4 is communicated to the second emulsifying device 70 through the first shunt 313. The first emulsifying device 60, the second emulsifying device 70 and the pre-emulsion device 50 may be a multi-layer mesh emulsifier, a mechanical emulsifier, an electric ultrasonic emulsifier, a reed whistle ultrasonic emulsifier, and a static emulsifier. , a jet mashing emulsifier or a combination of two or more. As shown in FIG. 1 , the emulsification operation flow of the present invention is that the fuel is preheated and reaches the expected fluidity before being introduced from the fuel line 10, 201243244. After the fuel line 10 is introduced, the oil is filtered through the oil line 10 in sequence. The electromagnetic regulator valve 12 and the flow meter 13 enter the mixing tank 3, and at the same time, after the water is introduced from the water supply line 20, the electric heater 24 is heated to the same temperature of the fuel, and then passes through the ball valve 21 in sequence. The electromagnetic regulating valve 22 and the flow meter 23 enter the mixing tank 30, and the electromagnetic regulating valves 12 and 22 and the flow meters 13 and 23 can be set according to a programmable logic controller (pLC) [not shown]. The oil-water mixing ratio value adjusts the oil input amount and the water intake amount, respectively. Then, after the fuel is transferred to the mixing tank 3 via the fuel line 1 and the water is supplied to the mixing tank 3, the fuel and water mixture can be discharged from the outlet line 31, and the pressurizing pump 32 is utilized. After the cycle pressurization and filtration of the filter η, it is divided into two paths. The pre-emulsifier 51 and the post-emulsifier 52 of the pre-emulsifying device 50 are pre-emulsified and then enter the mixing tank 3G. All the way through the second flow path 312 into the first emulsifying device 60 for emulsification, and then through the opening of the regulating valve 4 来 to adjust the amount of fuel and water mixture, and the fuel and water mixture will enter the The ultrasonic emulsifier 73 of the first emulsifying device 70 is further emulsified and can be directly transported to the storage tank 8G or used for field use. Alternatively, the fuel and water mixture may be passed through the ultrasonic emulsification $73 & the jet high shear emulsifier 74 is emulsified into the storage tank 80 or passed through the fuel outlet 81 for field use. Manual control can be achieved by adjustment of the manual valve 316 when the regulator valve 40 fails or is serviced. Further, in the pre-emulsifier 51 of the pre-emulsification device 50, the first emulsification device 60, and the ultrasonic emulsifier 73, a sound intensity detecting device 10 201243244 is disposed at 90' to understand the fuel emulsification effect. After the equipment is shut down, the control valve 1〇3 disposed on the fuel official road 10 is closed after draining the equipment and the residual oil in the pipeline, and then disposed between the control valve 1〇3 and the oil filter 11 The steam purge port 101 is connected to the steam, and the equipment and the pipeline are cleaned and purged into the storage tank 80 by steam, and the water accumulated in the storage tank 80 is discharged through the drain port 82. There is no residual fuel in the equipment and piping. And a bypass 1〇2 is arranged between the inlet and outlet of the device, that is, the bypass 1G2 is disposed between the fuel line 10 and the second outlet end 72, when the fuel emulsification device is repaired or replaced, Affect the normal operation of the combustion equipment. The efficacy of the present invention is as follows: 1. Using the pre-emulsification device 50, the first emulsifying device 6〇, the setting of the first emulsifying device 7G, and the jet flow force of the fluid itself, generating high-intensity sound waves and ultrasonic waves propagating in the fluid When the sound intensity reaches a certain intensity, the 'cavitation effect in the fluid' causes the molecular chain of the heavy oil to be cracked and recombined' to emulsify with water, (4) the water is the dispersed phase, and the oil is the continuous phase of the water-in-oil type W/0 (4) Floating but not separated milk fields. The water particles in the emulsified oil are evenly distributed, the particle size is fine, and the performance is stable. H is used for the emulsification of heavy oil, residual oil and coal tar. Any additive is added. That is to say, the fuel emulsified particles treated by the three-in-one high-efficiency fuel emulsification technology can reach _ upper, fineness ratio (four), and the 嶋 effect =, under the premise that the combustion efficiency of bismuth is high thermal efficiency, three-in-one Emulsified fuel can make the heating efficiency of the furnace reach over 99%. Second, when the emulsified fuel is burned, because it is a water-in-oil granule, it will produce a human atomization or micro-explosion effect in 201243244, achieving a good combustion effect. The flame temperature rises, the flame becomes shorter, the combustion is complete, and the adjustment parameters are wider. The overall thermal efficiency of the burner (such as a boiler) is increased, the fuel economy is increased, and the emission of harmful gases in the flue gas is further reduced, and the environmental discharge standard is fully achieved. 3. Most industrial boilers, industrial furnaces and diesel generator sets suitable for burning heavy oil, residual oil or coal tar can be emulsified and prepared online. Fourth, the higher the viscosity of the fuel, the higher the water mixing rate, and the greater the effect of fuel saving and pollution reduction. The maximum water mixing rate is 30%, and the maximum fuel saving rate is 25%, which significantly reduces carbon monoxide co, sulfur oxides S0x, and NOx emissions, which reduces harmful residues and reduces the corrosion of the body. Compared with the money, the emulsified fuel has a short flame and a strong intensity. It is in an incandescent state, the burning speed is increased, there is no turbidity and smoke in the furnace, the combustion is sufficient and stable, and the ash at the end of the furnace is greatly reduced. 5. The full combustion characteristics of the liquefied fuel can significantly reduce the carbon deposition and coking phenomenon, which can protect the furnace body and prolong the service life of the furnace*, reduce the labor intensity of maintenance work, and will not cause mechanical equipment. Any sauteed rice. Sixth, the use of emulsified fuel does not need to change the original fuel supply system and combustion device 'just need to adjust the individual X art temperature and distribution wind conditions, and can adjust the processing volume according to the use environment and oil conditions at any time The amount of water is suitable for different oils. VII. The ultrasonic emulsifier 73 of the second emulsifying device 7 and the jet mashing emulsifier 74 can be connected in series through the valve or separately, so that the parts can be repaired or replaced without stopping. .
S 12 201243244 八、 處理量大，可達1T/H-50T/H。 九、 按照外燃條件，180#燃料油在摻水率為i5%-2〇%時 ’可降低燃油成本以上’配風量可下調左右。 十、全程以可程式邏輯控制器控制，操作方便。 惟以上所述者，僅為本發明之較佳實施例而已，當不 能以此限定本發明實施之範圍，即大凡依本發明申請專利 範圍及發明說明内容所作之簡單的等效變化與修飾，皆仍 屬本發明專利涵蓋之範圍内。 【圖式簡單說明】 圖1是一線路控制圖，說明本發明燃油乳化製置的— 較佳實施例。 13 201243244 【主要元件符號說明】S 12 201243244 VIII. Large processing capacity up to 1T/H-50T/H. IX. According to the external combustion conditions, 180# fuel oil can reduce the fuel cost when the water mixing rate is i5%-2〇%. Ten, the whole process is controlled by programmable logic controller, which is easy to operate. The above is only the preferred embodiment of the present invention, and the scope of the invention is not limited thereto, that is, the simple equivalent changes and modifications made by the scope of the invention and the description of the invention are All remain within the scope of the invention patent. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a line control diagram showing a preferred embodiment of the fuel emulsification system of the present invention. 13 201243244 [Description of main component symbols]
S 10… .....燃油管路 50…… •…預乳化裝置 11…… .....油過遽器 51…… •…前乳化器 12…… …··電磁調節閥 52…… •…後乳化器 13…… •…流量計 60…… •…第一乳化裝置 20 .... …··供水管路 61…… •…第入口端 21…… -----球閥 62…… •…第出口端 22…… •…電磁調節閥 63…… •…乳化器 23…… •…流量計 70…… •…第二乳化裝置 24…… -----電加熱器 71…… …·第二入口端 30…… ----混合槽 72…… •…第二出口端 31…… •…引出管路 73…… •…乳化器 311 ···. ·'···第一流道 74…… •…乳化器 312 ···· •…第二流道 75 ..·· •…流量計 313 ··.· •…第一分流管 80…… •…儲存槽 314 .... •…第二分流管 81…… …·乳化油出口 315 ..·· •…歧管 82…… ··.·排污口 316 ···· •…手動閥 90…… •…聲強檢測裝置 317 ·… •…乳化器 101 .··· •…蒸汽吹掃口 32…… •…加壓果 102 ···· •…旁路 33…… •…過渡器 103 .··. …·控制閥 40…… •…調節閥 14S 10... ..... fuel line 50... •...pre-emulsifying device 11.................. oil filter 51... •...pre-emulsifier 12............................................................... ... •...post-emulsifier 13...•...flow meter 60...•...first emulsifying device 20 .....···water supply line 61... •...inlet end 21... -----ball valve 62... •...outlet end 22... •...electromagnetic regulating valve 63...•...emulsifier 23... •...flow meter 70...•...second emulsifying device 24... -----electric heater 71...... .... 2nd inlet end 30... ---- mixing tank 72... •... second outlet end 31... •... lead-out line 73... •...emulsifier 311 ···. ·'· ··First flow path 74...•...Emulsifier 312 ····•...Second flow path 75 ..··•...Flow meter 313 ·····...First shunt tube 80... •...Storage tank 314 .... •...Second shunt tube 81............Emulsified oil outlet 315 ..··•...Manifold 82... ····Drain outlet 316 ···· •...manual valve 90... Sound intensity detecting device 317 ·... •... Chemist 101 .··· •... Steam Purge Port 32... •... Pressurized Fruit 102 ···· •...Bypass 33... •...Transitional Device 103 ........ Control Valve 40... ...regulation valve 14