201105786 .六、發明說明： 【發明所屬之技術領域】 从,·、，發明為，供—種燃料之系統，尤指-種可高燃率的完全燃燒、 ，省此源、減量釋出二氧化碳及有害氣體排放、儲運油水不分離且無 須更動現有設備及具錢體保魏力的製造環娜料之系統。 【先前技術】 按’一般，料油係指包括（但不限於）煤油、汽油、柴油、重油 於具有高發熱值及成本之經濟因素考量，因此被產業選用於燃 例如銷爐之燃燒作業）。由於燃料油燃燒（如重油燃燒）， 九生許多硫氧化物及氮氧化物，而該硫氧化物及氮氧化物之遇上水 =’ ^容㈣成酸雨，因此造成空氣與環境污染。此外，由 有限’燃熱耗費也形成1紅之成本巨大支&。 ^ ㈣ϊϊν產業界逐漸開發具備節能以及降低燃料油污染。其中又以 ^合水分獲得重視。但是由於油水難以互溶為普遍習知。 因〖生，’而石油產品是由非極性化合物烴類組成。 、，曰:蜀妝肖纟化作業使二者成為混合液。❿乳化係指油水混合體之 ^狀，’既不溶化，又不沉殿之狀態，因此可以使得互不相溶的油 7方^激烈地攪拌或添加乳化雜，此時，有_ 另一 ^中’而互概合成為均勻狀態之乳濁液。 政於 葬物知道’乳化之均勻除了憑藉化學之乳化劑之外，亦可以瑪 、.致化=其效果，因此往往「乳化」與「均質」為關係密切。 裝置」8 4 1 7 γ號之「高剪切柴油乳化 體與固定體裝;也，大，觸 ，但:=能夠與水產生乳化、均質等混合作用 離之運送、储存後仍然會使油質回到尚未均質L::; 果不佳’並且於常溫下因黏度高，輪送必須具備力: 201105786 ^燃燒不完全，鋪會有結：!、、積碳錄況 二氧氣，但相對的會提高排放煙S度，』 ，2及硫化氣體’甚至因燃燒不完全， “ί以/ ϊ如何解決上述習用之問題與缺失，即為本發明之發明人 與仗事此订業之相關廠商所亟欲研究改善之方向所在者。 【發明内容】 方坪二二明之念:鑑於上述缺失，乃搜集相關資料，經由多 • 事此行業累積之多年經驗，經由不斷試作及 高鱗的完全燃燒、節省能源、減量釋出二氧 發不分離且無須更動現有設備及具』 、-主要二^:=斗系統係包括有-乳化劑產生單元 ，水早兀-供油早疋，魏化劑產生單元係接設有 路ΐΓΐ—第—流量控制單71，而該供水單⑽接設有 传官路上係設有—第二流量控制單心該第二管路 與該第二管路連接處之後係 -第一 ’上述之第一流量控制單元係包括有 制if i括有一第二流量計及—與該第二流量^相 ⑼量;=對應的第三幫浦，且於ί第⑽ϊ: 見拌早兀處係界疋有一取樣單元及一儲存 ΐίΐϊί流^制單元進行控制，俾控 過=置計之偵、測並同時配合操作該幫浦，使 透 桃罝以達到最佳流量輸出化，當乳化劑經由第一管路進行第二 201105786 水混合後則藉由該第一混合授拌 後硬化’响再流人第三管路奴第完整包覆水 k時油即將水與乳化兩丨士敕勺芦 /、口攪拌早兀與油進行結合， 瞬間產生氣爆，經氣2，進人銷爐透過高溫燃燒使其 藉由上述技術，可針對制、成數百個被更細化的微粒， ’轉動體與固定體之間仍然;有相;=裝^^之因孔徑較大 此細緻化之效果有限，且，縱使疋線狀切割’因 合作用，但經過一段時問，沾:肊夠，、水產生乳化、均質等混 此-段時間與距離之運送、_存彳仍然會逐漸分離，因 狀態而效衫佳，並錄常、=使^_尚未均質處理之 >備，而若燃燒不完全，鋼度須=加熱保溫設 ，對於環境的影響辦燒’妈目對的會提高排放煙氣溫度 完全，產細聯=====燒不 油包覆乳化劑及水量作動以形成必要物質，而當 氣爆把原包覆的油霧化成數百個生氣爆經 燒，達到節省能源、減量釋出二氧化碳 【實施方式】 設^第τ11，於該第-管 2的第-幫浦122,而該乳化劑產 201105786 ‘ 一供水單元2〇，係接設有一與該第一管路 2 土，於該第二管路2 !上係設有一第二流量控制第;J路 流篁控制單元22係包括有一第二流量計2 21及一鱼|繁-、^土一 $1相互操作對應的第二f浦2 2 2，且該第二管^ 官路11相接處之後係設有一第一混合攪拌單元2 供: 2 0係進-步可為水槽；及 早^ 3 ’而雜水單元 二，油f元3Q，係接t與該第二管路21 1，該第三管路3 i係接設有一第三流量控制單，之^ = 3 控制單元3 2係包括有-第三流量計321及_料==， 1相互操作對應的第三幫浦3 2 2，而該第三管路2 2 1連接處之後係設有一第二混合授拌單元^ y§'一'首路 攪拌單元3 3處係界定有一取樣單元34及存單通=第^現合 油單元3 0係進一步可為油槽。 儲存早疋3 5，再該供 又者，上述該第二管路2丄於第二流量控 — 1 1相接處之間係設有一第一安全回产輩元9 ，、 督路 於第三流量控制單元3 1 安全回流單元3 6，而為有效精確控制設有-苐二 流量控制單元2 2及第三流量控制單元3 =，制早Μ 2、第二 量控制單元12、第二流量控制單元2 ^ $輸出，因此，該第-流 電性連接一主控單元4 0 ’使該第一、第二流量控制單元3 2係 制單元2 2及第三流量控制單元3 2亦#，制單元12、第二流量控 ，以達到自動化油水不分離之進步性。N °τ同步相互自動分配所需流量 請同時配合參㈣二圖及第三圖 動作示意圖及燃料結合分解細化之流7^，係為本發明較佳實施例之 控單元4 0亦控制該第一流量控制圖，由圖中可清楚看出，該主 及第三流量控制單元3 2進行^制八^*、1 2、第二流量控制單元2 2 量之數值時，該主控單元4 〇^制^第^量，當使用者輸入欲輸出流 〜流量計121偵測通過該第—管路 幫浦12 2，並同時透過第 流量計121偵測到該第—管路1 1的乳化劑5 0，若當該第一 控單元4 0亦控制該第一幫浦} ? ^過過多的乳化劑5 0時則該主 丨 進行調節，另外，該水槽内的水 201105786 二！I Li，°玄第二幫浦2 2 2進行抽取，同時透過第二流量計2 2 1進 =旦3單元4 0同時對水槽内的水6 0進行控溫），若該第二 ΐ ί ί ^、i ί _第二管路2 1内通過過多的水6 0時則通知第二 ，而U 5 m同時藉由第一安全回流單元2 4進行調節回流 混合授拌單^ 3、t =由第一管路1 1及第二管路2 1流入第一 包覆於内，速混合攪拌，使乳化劑5 0硬化後將水6 〇 [51Β 士 - 第二机置汁3 2 1的搭配控制油7 0的流量’且 3早ί4〇控制油7〇的溫度，俾當油7〇通過該第三管路 jit?二同樣，第三幫浦3 2 2進行調節，以及由第二= 乳化劑5 0、水=即回流’而後’藉由第二混合授拌單元3 3進行 化劑5 ◦(乳化劑5 ^當結合完畢後油7 ◦即包覆乳 間產生氣爆，經氣爆◦)，再經由鍋爐高溫燃燒使其瞬 而因此使氫跟氧i彳:八=覆=成品細化成數百個被更細化的油7 〇， 存入該儲存單元3 =透過取樣早兀3 4進行取樣，而同時將油7 0 ⑼s動需求做壓力之控制，如：水 ，較大，使第ί = 交小的壓力抽取’而油7 〇因黏 過主控單元4 0二=須加;！'能f由7 〇抽取，因此，透 測進行第二、第三幫浦: f二流赠22 1、32 1的谓 管路2 1、3 1内油壓力’俾使第二、第三 必要流量處理。 7〇之机罝件以順利依所需設定進行 於：疋以纟發明之製造環保燃料之系統為可改善制之技術關鍵在 二流流量控制單元1 2、第 控制流量功能，而並且藉由第2 3其達到全自動化的 元3 3進行極速混合，使乳㈣早702 3及第二混合齡單 使礼化劑5〇、水6〇及油7〇得以進行包覆 201105786 現合’再進入鍋爐由高溫燃燒使其瞬間產生氣爆，經氣爆把原包覆的 油7 0霧化成數百個被更細化的微粒達到高燃率的完全燃燒，以達到 節省能源、減量釋出二氧化碳及有害氣體排放、儲運油7；〇水6 〇不 分離且無須更動現有設備及具有爐體保護能力之實用進步性。 再者，於儲運中油水不分離，可比照傳統燃料油使用，且完全燃 ^結焦、積碳狀況減低’提高職效率，延長觸壽命，而因燃燒 元%配同時降低了排放煙氣溫度，有效利用能量。 ί ’ ίί上所述僅為本發明之較佳實施例而已，非因此即拘限本發 明之專利犯圍，故舉凡獅本發縣明書及圖式内 ^201105786 .6. Description of the invention: [Technical field to which the invention pertains] The system for supplying fuel, especially for a complete combustion with high combustion rate, saving this source and reducing the release of carbon dioxide And the system of manufacturing harmful materials, such as harmful gas emissions, storage and transportation of oil and water, and no need to change existing equipment and money to protect Wei Li. [Prior Art] According to 'general oil, oil, including but not limited to kerosene, gasoline, diesel, heavy oil, is considered as an economic factor with high calorific value and cost, so it is selected by the industry for burning combustion such as pin furnace.) . Due to the burning of fuel oil (such as heavy oil combustion), nine kinds of sulfur oxides and nitrogen oxides are produced, and the sulfur oxides and nitrogen oxides are in contact with water, which causes acid rain, thus causing air and environmental pollution. In addition, the cost of a red fuel is also limited by the limited 'burning heat'. ^ (4) ϊϊν industry gradually developed energy conservation and reduced fuel oil pollution. Among them, the importance of water is obtained. However, it is common to know that oil and water are difficult to dissolve. Because of the birth, the petroleum product consists of non-polar hydrocarbons.曰:蜀 蜀 纟 作业 作业 作业 作业 作业 作业 作业 作业 作业 作业 作业 作业 作业❿ Emulsification refers to the shape of the oil-water mixture, which is neither dissolved nor in the state of the temple. Therefore, the mutually incompatible oil can be stirred or added with emulsified impurities. At this time, there is _ another ^ In the middle of each other, the emulsion is synthesized into a uniform state. In the funeral, it is known that the uniformity of emulsification is not only the chemical emulsifier, but also the effect of emulsification. It is often closely related to "emulsification" and "homogeneity". "8 4 1 7 γ" "High shear diesel emulsion and fixed body; also, large, touch, but: = can be mixed with water to produce emulsification, homogenization, etc. The quality is not yet homogenized L::; The fruit is not good' and because of the high viscosity at normal temperature, the rotation must have the force: 201105786 ^The burning is not complete, the shop will have a knot:!,, carbon deposits, two oxygen, but relative Will increase the emission S degree, 』, 2 and vulcanized gas 'even because the combustion is not complete, " ί / ϊ how to solve the above problems and lack of use, that is, the inventor of the invention is related to this order The manufacturer is eager to study the direction of improvement. [Summary of the Invention] Fang Ping Er Er Ming's thoughts: In view of the above-mentioned shortcomings, it is to collect relevant information, and through the years of experience accumulated in this industry, through continuous trials and high-level complete combustion, energy saving, and reduction of dioxin emissions No separation and no need to change existing equipment and equipment 』, - Main two ^: = bucket system includes emulsifier production unit, water early 兀 - oil supply early, Weihua agent production unit is connected with roller ΐΓΐ - - a flow control unit 71, and the water supply sheet (10) is provided with a relay line system - a second flow control unit, the second line is connected to the second line, and the first is the first The flow control unit includes a second flow meter having a second flow meter and a second flow meter corresponding to the second flow rate, and a third pump corresponding to the second flow rate (=), and at the (10)ϊ: The sampling unit and a storage unit are controlled, and the detection and measurement are performed together with the pump, so that the pump can be operated to achieve optimal flow output, when the emulsifier passes through the first tube. After the road is mixed with the second 201105786 water, The first mixed after mixing and hardening 'sounding reflowing the third line slaves completely covered with water k when the oil is about to combine water with emulsified two gentleman's spoon, reed, and the mouth is stirred early and the oil is combined to instantly produce a gas explosion. Through gas 2, entering the furnace through high-temperature combustion, through the above technology, can be made into hundreds of finer particles, 'there is still between the rotating body and the fixed body; there is phase; ^ Due to the larger aperture, the effect of this refinement is limited, and even if the 疋-line cutting is used for cooperation, after a period of time, the smear: suffocate, the water is emulsified, homogenized, etc. - time and distance The transportation, _ storage will still gradually separate, due to the state of the effect of the best, and record, = ^ ^ not yet homogenized treatment, and if the combustion is not complete, the steel must = heating insulation, for the environment The impact of the burning of the 'mother's eye will increase the exhaust gas temperature completely, the production of thin joint ===== burning oil-free emulsifier and water to act to form the necessary substances, and when the gas bursts the original coated oil Atomization into hundreds of angry explosions to save energy and reduce carbon dioxide emissions [Implementation The first τ11 is in the first pump 122 of the first tube 2, and the emulsifier is produced in the 201105786' water supply unit 2〇, and the first pipeline 2 is connected to the second pipeline. 2! The upper system is provided with a second flow control unit; the J-way flow control unit 22 includes a second flow meter 2 21 and a second fish 2 2 2 corresponding to each other. And the first mixing unit 2 is provided with a first mixing and stirring unit 2 for: 20 0-step can be a sink; early ^ 3 ' and a water unit 2, oil f 3 3, The second pipe 3 i is connected with a third flow control unit, and the third control unit 3 2 includes a third flow meter 321 and a material = =, 1 corresponds to the third pump 3 2 2 corresponding to each other, and the third line 2 2 1 is connected with a second mixing and mixing unit ^ y ' ' a 'first mixing unit 3 3 Defining a sampling unit 34 and a single pass = the first oil unit 30 can further be an oil sump. Store the early 疋 3 5, and then the supply, the second pipeline 2 is connected to the second flow control - 1 1 junction is provided with a first safe return generation 9 , The three flow control unit 3 1 is a safety return unit 3 6 , and for effective and precise control, the second flow control unit 2 2 and the third flow control unit 3 are provided, and the second quantity control unit 12 and the second quantity are provided. The flow control unit 2 ^ $ is output, therefore, the first-current electrical connection to a main control unit 40 0 causes the first and second flow control units 32 to control the unit 2 2 and the third flow control unit 3 2 #,Unit 12, the second flow control, in order to achieve the progress of automatic oil and water separation. The N ° τ synchronization automatically allocates the required flow rate to each other. The control unit and the fuel combination decomposition refinement flow are also supported by the control unit (4) and the third embodiment, and the control unit 40 of the preferred embodiment of the present invention also controls the flow. The first flow control chart, as can be clearly seen from the figure, when the main and third flow control units 32 perform the numerical values of the quantity of the second flow control unit 2, the main control unit 4 〇^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^ The emulsifier 50, if the first control unit 40 also controls the first pump}? ^ too much emulsifier 50, then the main raft is adjusted, in addition, the water in the sink 201105786 two! I Li, ° Xuan second pump 2 2 2 to extract, while passing through the second flow meter 2 2 1 into = 3 units 4 0 while controlling the water in the water tank 60, if the second ΐ ί ί ^, i ί _ The second pipe 2 1 passes the excess water 60 to notify the second, and the U 5 m is simultaneously adjusted by the first safety recirculation unit 24 to mix the mixing batch ^ 3, t = The first pipe 1 1 and the second pipe 2 1 flow into the first coating, and the mixture is stirred rapidly, so that the emulsifier 50 is hardened and the water is 6 〇 [51 - - second machine juice 3 2 1 The collocation control oil 7 0 flow 'and 3 early ί 4 〇 control oil 7 〇 temperature, 俾 when oil 7 〇 through the third pipe jit? II, the third pump 3 2 2 to adjust, and by the 2 = emulsifier 50, water = that is, reflux 'and then' by the second mixing and mixing unit 3 3 to carry out the agent 5 ◦ (emulsifier 5 ^ when the combination of oil 7 ◦ that is, the coating between the milk to produce gas explosion, After the gas explosion, the high temperature combustion of the boiler makes it instantaneous and thus makes the hydrogen and oxygen i: 8 = cover = the finished product is refined into hundreds of finer oils 7 〇, deposited in the storage unit 3 = through Sampling as early as 3 4 for sampling At the same time, the oil 7 0 (9) s dynamic demand control, such as: water, larger, so that the pressure of the first ί = small extraction ’ and the oil 7 黏 because of the adhesion of the main control unit 4 0 2 = must be added; 'Can f is extracted by 7 ,, therefore, the second and third pumps are transmitted through the test: f second stream gives 22 1 , 32 1 means the pipeline 2 1 , 3 1 oil pressure '俾 makes the second and third necessary Traffic processing. The 7〇 罝 罝 以 以 以 以 以 依 依 依 依 依 依 依 依 依 依 依 依 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造2 3 It achieves full automation of the 3 3 for rapid mixing, so that the milk (four) early 702 3 and the second mixed age single ritual agent 5 〇, water 6 〇 and oil 7 〇 can be coated 201105786 now 're-enter The boiler is burned at a high temperature to instantly generate a gas explosion. The gas is blown to atomize the originally coated oil 70 into hundreds of finer particles to achieve complete combustion with high combustion rate, so as to save energy and reduce carbon dioxide emissions. And harmful gas emissions, storage and transportation of oil 7; 〇水6 〇 does not separate and does not need to change the existing equipment and the practical progress of the furnace protection ability. Moreover, in the storage and transportation, the oil and water are not separated, and can be used in comparison with the traditional fuel oil, and the complete combustion and coking, the carbon deposition condition is reduced, the utility efficiency is increased, the contact life is prolonged, and the exhaust gas temperature is reduced due to the combustion element%. Use energy. ί ’ ί ί ί ί ί ί ί ί ί ί ί ί ί ί ’ 上 上 上 上 上 上 上 上 上 上 上 上 上 上 上 上 上 上 上 上 上 上 上 上 上 上
及等效結構變化’均應同理包含於本發明之專利 了 ^日^。 利之申請要件’爰依法提出申請， ::ίίίΐΓ:ί本發明誠為-實用性優異之=為 發明人定當竭力配合，實感公便 201105786 【圖式簡單說明】 第一圖係為本發明較佳實施例之方塊圖。 第二圖係為本發明較佳實施例之動作示意圖。 第三圖係為本發明燃料結合分解細化之流程圖。 【主要元件符號說明】 乳化劑產生單元····10 第一管路.......11 第一流量控制單元···12 第一流量計......12 1 第一幫浦.......12 2 籲供水單元.......2 0 第二管路.......2 1 第二流量控制單元··· 2 2 第二流量計......2 2 1 第二幫浦.......2 2 2 第一混合攪拌單元··· 2 3 第一安全回流單元···24 供油單元.......3 0 第三管路.......3 1 第三流量控制單元··· 3 2 β第三流量計......3 2 1 第三幫浦.......3 2 2 第二混合攪拌單元··· 3 3 取樣單元.......3 4 儲存單元.......3 5 第二安全回流單元··· 3 6 主控單元.......4 0 乳化劑........5 0 水..........6 0And equivalent structural changes' should be included in the patent of the present invention. Application for the application of 'Levy', </ br> </ br /> </ br> </ br> </ br> </ br> </ br> </ br> </ br> </ br> </ br> </ br> </ br> </ br> A block diagram of an embodiment. The second drawing is a schematic view of the operation of the preferred embodiment of the present invention. The third figure is a flow chart of the fuel combination decomposition and refinement of the present invention. [Explanation of main component symbols] Emulsifier generating unit····10 First pipe....11 First flow control unit···12 First flow meter...12 1 first Pump ....12 2 Call the water supply unit.......2 0 Second line....2 1 Second flow control unit··· 2 2 Second flow meter ......2 2 1 Second pump... 2 2 2 First mixing unit··· 2 3 First safety recirculation unit···24 Oil supply unit..... ..3 0 Third pipe.......3 1 Third flow control unit··· 3 2 β third flow meter...3 2 1 Third pump..... ..3 2 2 Second mixing agitation unit··· 3 3 Sampling unit.......3 4 Storage unit.......3 5 Second safety reflow unit··· 3 6 Main control unit .......4 0 Emulsifier ........5 0 Water..........6 0