TWI473671B - A waste disposal methods of the renewable energy - Google Patents
A waste disposal methods of the renewable energy Download PDFInfo
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- TWI473671B TWI473671B TW101128649A TW101128649A TWI473671B TW I473671 B TWI473671 B TW I473671B TW 101128649 A TW101128649 A TW 101128649A TW 101128649 A TW101128649 A TW 101128649A TW I473671 B TWI473671 B TW I473671B
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Description
本發明是有關於一種再生能源的方法，特別是指一種針對處理廢棄物時而可一併產出再生能源的方法。The present invention relates to a method for regenerating energy, and more particularly to a method for producing renewable energy together when treating waste.
因生活水準之提高也使得現代人對環保議題產生高度的重視，台灣雖然不產鋁曠，每年卻有上萬噸的廢棄鋁製品進入回收再利用系統，廢鋁渣的主要來源為鋁罐、鋁門窗等廢棄回收廢鋁材，經過熔煉後變成鋁錠，作為再生原料後所產生的廢棄殘渣。Due to the improvement of living standards, modern people attach great importance to environmental protection issues. Although Taiwan does not produce aluminum bismuth, there are tens of thousands of tons of waste aluminum products entering the recycling system every year. The main source of waste aluminum slag is aluminum cans. Waste aluminum scraps such as aluminum doors and windows are smelted and turned into aluminum ingots, which are used as waste residues after reclaiming raw materials.
目前世界各國無一致的鋁渣處理方法，所以多半仍以掩埋方式來處理廢棄鋁渣。以台灣為例，掩埋廢棄鋁渣的價格因廢棄鋁渣越來越多且合法掩埋場稀少，價格也相對跟著水漲船高，造成不肖廠商為了節省處理費用，直接將未經處理過的廢棄鋁渣隨意丟棄或任意掩埋，對環境產生嚴重的汙染。掩埋在地底的廢棄鋁渣多年後毒性也不會消失，且掩埋的廢棄鋁渣與水接觸之後進行化學反應會產生惡臭。At present, there is no consistent aluminum slag treatment method in the world, so most of the waste slag is still disposed of by landfill. Taking Taiwan as an example, the price of buried aluminum slag is more and more due to the waste of aluminum slag and the legal landfill is scarce. The price is also relatively high, which causes the unscrupulous manufacturers to directly treat untreated waste aluminum slag in order to save processing costs. Discard or arbitrarily bury, causing serious pollution to the environment. The toxicity of the waste aluminum slag buried in the ground will not disappear after many years, and the chemical reaction of the buried waste aluminum slag after contact with water will produce malodor.
現行廢棄鋁渣回收處理方法，舉以我國公告第233312號發明專利案為例，是將鋁渣經過溼式球磨、篩分、氣提除氨、濃泥沈降等處理過程後，可以充分的提升殘留金屬鋁的品位，使其能回爐熔煉，此部分雖能對於廢棄鋁渣部分再利用，但是在處理過程中並無針對浸泡廢棄鋁渣的水做更妥善的資源回收再利用，因處理過程中廢棄鋁渣浸泡 於水中會釋出氨氣及甲烷。氨氣有阿摩尼亞刺鼻惡臭味，人體吸入會有嗆咳、呼吸道不適等症狀，且氨氣為急性氣體若為高濃度大量外洩，現場通風況狀不良，可能造成化學性肺炎、肺水腫等，後果足以致命，而空氣中的甲烷濃度達25%~30%時，人體會出現窒息前症狀，頭暈、呼吸增快、脈速、乏力、注意力不集中、共濟失調、精細動作障礙，甚至窒息。The current method for recycling waste aluminum slag, taking the invention patent case No. 233312 of our country as an example, is to fully enhance the aluminum slag after being subjected to wet ball milling, sieving, gas stripping, ammonia removal, and mud sedimentation. The grade of residual metal aluminum can be smelted back to the furnace. Although this part can be reused for the waste aluminum slag part, there is no better resource recovery and reuse for the water soaked in the waste aluminum slag during the treatment, due to the treatment process. Soaked aluminum slag Ammonia and methane are released in the water. Ammonia gas has the odor of Amonia irritating, and the human body may have symptoms such as cough and respiratory discomfort, and ammonia gas is an acute gas. If it is a large concentration, it will leak out, and the ventilation condition may be bad, which may cause chemical pneumonia. Pulmonary edema, the consequences are fatal, and when the concentration of methane in the air reaches 25% to 30%, the body will have symptoms before asphyxia, dizziness, rapid breathing, pulse rate, fatigue, inattention, ataxia, Fine movement disorders, even suffocation.
由此可知，廢棄鋁渣在處理過程中，若沒有妥善的處理不僅會造成環境的污染，對於人體健康更會造成很嚴重的傷害，而浸泡廢棄鋁渣所產生的廢水、氨氣及甲烷若能在回收處理時作更有效的利用，除了能確實改善造成空氣污染及人體健康的問題外，更可達到環保、節能及資源有效利用等功效，確實值得深入探討與改善。It can be seen that if the waste aluminum slag is not properly treated during the treatment, it will not only cause environmental pollution, but also cause serious damage to human health, and the waste water, ammonia gas and methane generated by soaking waste aluminum slag. It can be used more effectively in recycling. In addition to improving the problems of air pollution and human health, it can also achieve environmental protection, energy conservation and efficient use of resources. It is indeed worth exploring and improving.
因此，本發明之目的，即在提供一種廢棄物處理再生能源方法，該方法包含以下步驟。Accordingly, it is an object of the present invention to provide a method of treating waste energy from waste, the method comprising the following steps.
首先，收集廢棄鋁渣並置入一第一處理槽中，接著，將該第一處理槽中注水以使該廢棄鋁渣與水進行化學反應，並靜置一段時間。然後，自該第一處理槽中將該廢棄鋁渣與水分離，最後，將分離後的水收集在一起以作為燃料等再生利用物。First, the waste aluminum slag is collected and placed in a first treatment tank, and then the first treatment tank is filled with water to chemically react the waste aluminum slag with water and allowed to stand for a while. Then, the waste aluminum slag is separated from the water from the first treatment tank, and finally, the separated water is collected together to be used as a fuel or the like.
本發明之功效在於既有的廢棄鋁渣處理過程中將廢棄鋁渣與水浸泡後分離，並將分離後的水收集在一起，可作為燃料能源及再生利用物使用，不但能減少浸泡廢棄鋁渣 所產生的廢水處理費用，及所衍生的隨意傾倒導致環境污染問題，更能確實的將浸泡廢棄鋁渣所產生的廢水更完善、更安全及更有效的回收再利用，進而達到資源永續利用及環保之訴求等優點。The utility model has the advantages that the waste aluminum slag is separated from the water after being treated in the waste aluminum slag treatment process, and the separated water is collected together, which can be used as a fuel energy source and a recycled material, thereby not only reducing the waste aluminum for immersion Slag The waste water treatment costs incurred and the resulting random dumping lead to environmental pollution problems, and the wastewater generated by soaking waste aluminum slag can be more accurately, safely and effectively recycled, thereby achieving sustainable use of resources. And the advantages of environmental protection.
有關本發明之相關申請專利特色與技術內容，在以下配合參考圖式之二個較佳實施例的詳細說明中，將可清楚的呈現。The details of the related patents and the technical contents of the present invention will be apparent from the following detailed description of the preferred embodiments of the accompanying drawings.
在進行詳細說明之前，應注意的是，類似的元件是以相同的元件編號來表示。Before the detailed description, it should be noted that similar elements are denoted by the same element numbers.
參閱圖1，為本發明廢棄物處理再生能源方法之第一較佳實施例，適用於將一廢棄鋁渣2浸泡於水3中以進行化學反應，該廢棄物處理再生能源系統包含一第一處理槽11、一第二處理槽12，及一抽風管14。1 is a first preferred embodiment of a method for treating waste energy from waste according to the present invention, which is suitable for immersing a waste aluminum slag 2 in water 3 for chemical reaction, and the waste treatment and regeneration energy system includes a first The processing tank 11, the second processing tank 12, and an exhaust duct 14.
該第一處理槽11是用以容納所收集的廢棄鋁渣2與水3，該第二處理槽12設置於該第一處理槽11之一側，並包括一連接該第一處理槽11與該第二處理槽12的連接管120。The first processing tank 11 is configured to receive the collected waste aluminum slag 2 and water 3. The second processing tank 12 is disposed on one side of the first processing tank 11 and includes a first processing tank 11 connected thereto. The connecting tube 120 of the second processing tank 12.
在該第一較佳實施例中，本發明之廢棄物處理再生能源系統更包含有一燃燒室13。但實際實施時，也可以不須要該燃燒室13存在，該燃燒室13可以是需要常時燃燒的場所，例如焚化爐、鍋爐等平時就需要以火進行大量燃燒的設備。In the first preferred embodiment, the waste treatment and regenerative energy system of the present invention further includes a combustion chamber 13. However, in actual practice, the combustion chamber 13 may not be required to exist. The combustion chamber 13 may be a place where combustion is required at all times, for example, an incinerator, a boiler, or the like, which requires a large amount of combustion by fire.
值得一提的是，該燃燒室13是設置於該第二處理槽12 之一側。該抽風管14包括一抽風端141、一相反於該抽風端141之排放端142，及一設置於該抽風管14中並介於該抽風端141與該排放端142間的抽風扇143，其中，該抽風端141是設置於該第一處理槽11上方，該排放端142是設置於該燃燒室13。It is worth mentioning that the combustion chamber 13 is disposed in the second processing tank 12 One side. The exhaust duct 14 includes a draft end 141, a discharge end 142 opposite to the exhaust end 141, and a suction fan 143 disposed in the exhaust duct 14 and interposed between the exhaust end 141 and the discharge end 142, wherein The exhaust end 141 is disposed above the first processing tank 11, and the discharge end 142 is disposed in the combustion chamber 13.
配合參閱圖2，依據上述廢棄物處理再生能源系統的硬體配置，本發明廢棄物處理再生能源方法包含下列步驟。首先，進行步驟901，收集廢棄鋁渣2並將該廢棄鋁渣2置入該第一處理槽11中。在該第一較佳實施例中，該廢棄鋁渣中主要材質是選自於金屬鋁、氧化鋁、氮化鋁、碳化鋁、氯化鋁、二氧化矽，及此等之組合。Referring to FIG. 2, according to the hardware configuration of the waste disposal and renewable energy system, the waste treatment and regeneration energy method of the present invention comprises the following steps. First, in step 901, the waste aluminum slag 2 is collected and the waste aluminum slag 2 is placed in the first treatment tank 11. In the first preferred embodiment, the main material of the waste aluminum slag is selected from the group consisting of aluminum metal, aluminum oxide, aluminum nitride, aluminum carbide, aluminum chloride, cerium oxide, and the like.
接著，進行步驟902，在該第一處理槽11中注水3，使水3能夠淹過該廢棄鋁渣2，以將該廢棄鋁渣2與水3進行化學反應，並浸置一段時間。在該第一較佳實施例中，所添加的水3與該廢棄鋁渣2之重量比為3：1，通常以1噸重的廢棄鋁渣2即須要以3噸的水3來浸泡，且該廢棄鋁渣2浸置於水3中的時間為3小時以上至數天之久。Next, in step 902, water 3 is injected into the first treatment tank 11, so that the water 3 can be flooded through the waste aluminum slag 2 to chemically react the waste aluminum slag 2 with the water 3, and immersed for a while. In the first preferred embodiment, the weight ratio of the added water 3 to the waste aluminum slag 2 is 3:1, and usually 1 ton of waste aluminum slag 2 needs to be immersed in 3 tons of water 3 And the time during which the waste aluminum slag 2 is immersed in the water 3 is from 3 hours or more to several days.
然後，進行步驟903，由於該廢棄鋁渣2屬於非親水性材料，堆置在水3中的廢棄鋁渣2並不會溶解於水中，因此，在浸置過程中須持續攪拌該第一處理槽11中的廢棄鋁渣2一段時間，以使該廢棄鋁渣2能充分與水3進行化學反應。Then, in step 903, since the waste aluminum slag 2 is a non-hydrophilic material, the waste aluminum slag 2 stacked in the water 3 does not dissolve in the water, and therefore, the first treatment tank must be continuously stirred during the immersion process. The waste aluminum slag 2 in 11 is used for a period of time so that the waste aluminum slag 2 can sufficiently chemically react with the water 3.
該廢棄鋁渣2在浸泡水3的過程中，因該廢棄鋁渣2中的氮化鋁與水3接觸進行化學反應，進而釋出氨氣與甲 烷，其化學反應式為AlN+3H2OAl(OH)3+NH3。部分的氨氣與甲烷能直接溶於水3中，其它則變為氣泡發散出去。In the process of soaking the water 3, the waste aluminum slag 2 is chemically reacted by contacting the aluminum nitride in the waste aluminum slag 2 with the water 3, thereby releasing ammonia gas and methane, and the chemical reaction formula is AlN+3H2O. Al(OH)3+NH3. Part of the ammonia and methane can be dissolved directly in the water 3, and the others become bubbles.
接著，進行步驟904，由於該抽風管14之抽風端141是設置於該第一處理槽11上方，而該排放端142是設置於該燃燒室13，所以當啟動該抽風扇143轉動時，可收集該第一處理槽11中所散發出的氨氣與甲烷並導入該燃燒室13中，而由於氨氣與甲烷屬於可燃性氣體具有助燃效果，故可直接供該燃燒室13使用。Then, in step 904, since the exhaust end 141 of the exhaust duct 14 is disposed above the first processing tank 11, and the discharge end 142 is disposed in the combustion chamber 13, when the driving fan 143 is started to rotate, The ammonia gas and the methane emitted in the first treatment tank 11 are collected and introduced into the combustion chamber 13, and since the ammonia gas and the methane are combustible gases having a combustion-supporting effect, they can be directly used for the combustion chamber 13.
在此，應注意的是，該第一處理槽11中的水3與該廢棄鋁渣2進行激烈的化學反應，會產生大量的氨氣與甲烷，部分的氨氣與甲烷會溶解於水中，其它部分則被該抽風管14抽取至該燃燒室13中進行燃燒，而該燃燒室13可以是焚化爐或鍋爐等這種需要常時燃燒的設備。由於氨氣與甲烷是屬於助燃性的氣體，所以導入該燃燒室13中可以輔助燃燒。Here, it should be noted that the water 3 in the first treatment tank 11 undergoes a vigorous chemical reaction with the waste aluminum slag 2, and a large amount of ammonia gas and methane are generated, and part of the ammonia gas and methane are dissolved in the water. The other portion is extracted into the combustion chamber 13 by the exhaust pipe 14 for combustion, and the combustion chamber 13 may be an apparatus such as an incinerator or a boiler that requires constant combustion. Since ammonia gas and methane are combustion-supporting gases, introduction into the combustion chamber 13 can assist combustion.
再者，由於氨氣有阿摩尼亞刺鼻惡臭味，人體吸入會有嗆咳、呼吸道不適等症狀，且氨氣為急性氣體若為高濃度大量外洩，現場通風況狀不良，可能造成化學性肺炎、肺水腫等，後果足以致命，本發明將大部分的氨氣與甲烷導入該燃燒室13中燃燒正可一併解決空氣汙染的問題。In addition, because ammonia has the odor of Amonia irritating, the human body may have symptoms such as cough and respiratory discomfort, and the ammonia gas is an acute gas. If the concentration is high, the ventilation condition is poor. The cause of chemical pneumonia, pulmonary edema, etc., is fatal. The present invention solves the problem of air pollution by introducing most of the ammonia gas and methane into the combustion chamber 13 for combustion.
然後，進行步驟905，自該第一處理槽11中將該廢棄鋁渣2與水3分離，分離的方式可以是藉由該連接管120將該第一處理槽11中的水3導引至該第二處理槽12中， 而使該廢棄鋁渣2與水3分離在兩個處理槽中，或是將該廢棄鋁渣2撈起至該第二處理槽12中。Then, in step 905, the waste aluminum slag 2 is separated from the water 3 from the first treatment tank 11, and the separation may be performed by guiding the water 3 in the first treatment tank 11 to the water through the connection pipe 120. In the second processing tank 12, The waste aluminum slag 2 and the water 3 are separated into two treatment tanks, or the waste aluminum slag 2 is picked up into the second treatment tank 12.
接著，進行步驟906，重覆前述步驟901~904，將所收集的水3拿來重覆浸泡該廢棄鋁渣2，由於水3被重複浸泡該廢棄鋁渣2，所以水2中所溶解的氨氣與甲烷濃度會愈來愈高。Then, in step 906, the above steps 901 to 904 are repeated, and the collected water 3 is repeatedly immersed in the waste aluminum slag 2, and since the water 3 is repeatedly immersed in the waste aluminum slag 2, the water 2 is dissolved. Ammonia and methane concentrations will increase.
然後，進行步驟907，當水3中所溶解的氨氣與甲烷達到預定濃度時，即可成為氨水，此時，即可將該等氨水3收集在一起便可作為燃料使用。在該第一較佳實施中，是先將水3，收集在一起然後再進行過濾，以去除水3中的鋁渣屑及其他雜質。在此，應注意的是，該第一較佳實施例中是採用逆滲透過濾方式進行過濾，但實際實施時，也可以採用其他過濾方式，並不以此為限。Then, in step 907, when the ammonia gas and the methane dissolved in the water 3 reach a predetermined concentration, the ammonia water can be obtained. At this time, the ammonia water 3 can be collected and used as a fuel. In this first preferred embodiment, water 3 is first collected and then filtered to remove aluminum slag and other impurities from water 3. Here, it should be noted that in the first preferred embodiment, the reverse osmosis filtration method is used for filtering, but in actual implementation, other filtering methods may also be adopted, and are not limited thereto.
最後，進行步驟908，由於氨水的沸點為33.35度，常溫之下容易產生自燃現象，危險性極高，若將收集到的水3使用低溫處理則可避免發生自燃現象，以確保安全性。在該第一較佳實施中，我們將收集後的水3進行低溫處理，而進行低溫處理的方式可以是將氨水結成冰塊，使其性質穩定以便輸送至該燃燒室13作為燃料使用，或是運送至它處。Finally, in step 908, since the boiling point of the ammonia water is 33.35 degrees, spontaneous combustion is likely to occur at normal temperature, and the danger is extremely high. If the collected water 3 is treated with low temperature, spontaneous combustion can be avoided to ensure safety. In the first preferred embodiment, we perform the low temperature treatment of the collected water 3, and the low temperature treatment may be performed by forming the ammonia water into ice cubes to stabilize the properties for delivery to the combustion chamber 13 for use as a fuel, or It is shipped to it.
依據上述說明可知，由於該廢棄鋁渣2與水3進行化學反應後溫度會變的很高，而該第一處理槽11中分離出的水是流入該第二處理槽12中儲存，所以將水分離出來是安全性較高且節省人力的方法。又因浸泡該廢棄鋁渣2的水3 用量非常可觀，如1噸的廢棄鋁渣2就需要用到3噸的水3來做浸泡，本發明將收集後的水3重覆浸泡該廢棄鋁渣2，不僅可節省水費、達到資源有效利用的功能，又可更進一步使水3中氨的濃度增高，讓普通水3變成氨水，並進一步就近作為該燃燒室13的燃料使用。According to the above description, since the temperature of the waste aluminum slag 2 and the water 3 is highly reacted, the water separated in the first treatment tank 11 flows into the second treatment tank 12, so Separation of water is a safe and labor-saving method. And by soaking the water of the waste aluminum slag 2 The dosage is very considerable. For example, 1 ton of waste aluminum slag 2 requires 3 tons of water 3 for immersion. According to the present invention, the collected water 3 is repeatedly immersed in the waste aluminum slag 2, thereby saving water and resources. The function of effective use further increases the concentration of ammonia in the water 3, turns the ordinary water 3 into ammonia water, and further uses it as a fuel for the combustion chamber 13.
參閱圖3、4，為本發明廢棄物處理再生能源方法及其系統之第二較佳實施例，該第二實施例與該第一實施例大致相同，相同之處於此不再贅述，不同之處在於，該廢棄物處理再生能源系統之抽風端141是設置於該第一處理槽11的上方，而該排放端142是設置於該第二處理槽12中。3 and 4 are a second preferred embodiment of the method and system for recycling waste energy according to the present invention. The second embodiment is substantially the same as the first embodiment, and the same points are not described herein again. The exhaust end 141 of the waste treatment and regenerative energy system is disposed above the first treatment tank 11 , and the discharge end 142 is disposed in the second treatment tank 12 .
在該廢棄物處理再生能源方法之步驟904中，由於該抽風管14之抽風端141是設置於該第一處理槽11上方，而該排放端142是設置於該第二處理槽12中，所以當啟動該抽風扇143轉動時，可將該第一處理槽11中所散發出的氣體導入該第二處理槽12中。In the step 904 of the waste treatment and regenerative energy method, since the exhaust end 141 of the exhaust duct 14 is disposed above the first treatment tank 11, and the discharge end 142 is disposed in the second treatment tank 12, When the fan 143 is started to rotate, the gas emitted from the first processing tank 11 can be introduced into the second processing tank 12.
該第二處理槽12中的水3是由該第一處理槽11中所排放過來，藉由氨氣可溶解於水中的特性，該第一處理槽11散發出的氨氣及甲烷經由該第一處理槽11上方設置之抽風管14的抽風端141抽引至插設於該第二處理槽12水中的排放端142，並將所產生的氨氣及甲烷再度排入水3中，用以提高該第二處理槽12之水3中氨的濃度，當水3中氨及甲烷的濃度到達預定濃度時，即可作為燃料使用。The water 3 in the second treatment tank 12 is discharged from the first treatment tank 11, and the ammonia gas is dissolved in the water. The ammonia gas and methane emitted from the first treatment tank 11 pass through the first The exhaust end 141 of the exhaust duct 14 disposed above the processing tank 11 is drawn to the discharge end 142 inserted in the water of the second treatment tank 12, and the generated ammonia gas and methane are again discharged into the water 3 for The concentration of ammonia in the water 3 of the second treatment tank 12 is increased, and when the concentration of ammonia and methane in the water 3 reaches a predetermined concentration, it can be used as a fuel.
值得一提的是，本發明可將多餘的氨水收集後經由低 溫保存或結冰等方式運送來販賣，其中，高濃度的氨水可藉由稀釋後再使用於農業、工業及醫藥等行業，如農業上經稀釋後可用作化肥，工業用於製造肥料、人造纖維或塑膠等。有機工業用作胺化劑等。醫藥上用稀釋氨水對呼吸和迴圈起反射性刺激，用於醫治暈倒和昏厥，並作皮膚刺激藥和消毒藥。It is worth mentioning that the present invention can collect excess ammonia water after passing through low It can be transported and sold by means of warm preservation or icing. Among them, high-concentration ammonia can be diluted and used in agriculture, industry and medicine industries. For example, it can be used as fertilizer after dilution in agriculture, and it is used in industry for fertilizer production. Man-made fibers or plastics. The organic industry is used as an aminating agent and the like. The use of diluted ammonia in medicine is a reflective stimulus for breathing and circulation, used to treat fainting and fainting, and as a skin irritant and disinfectant.
綜合上述，有鑑於現代人對環保議題的高度重視，本案發明人研發出在處理廢棄鋁渣過程中所使用的水來作為能源使用，使資源再生利用，不但能解決無處堆置窘境，亦不會造成國家資源的浪費，並確實改善氨氣、甲烷與排放氨水所造成的空氣污染、環境汙染及人體健康等問題，更達到減量、節能及無害等功效，故確實可以達成本發明之目的。In view of the above, in view of the modern people's high attention to environmental issues, the inventor of this case developed the water used in the process of treating waste aluminum slag as energy use, so that resources can be recycled, which can not only solve the problem of nowhere to be stacked, but also It will not cause waste of national resources, and it will indeed improve the air pollution, environmental pollution and human health caused by ammonia, methane and ammonia discharge, and achieve the effects of reduction, energy saving and harmlessness. Therefore, it is indeed possible to achieve the purpose of the present invention. .
惟以上所述者，僅為本發明之二個較佳實施例而已，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內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內。However, the above is only the two preferred embodiments of the present invention, and the scope of the present invention is not limited thereto, that is, the simple equivalent change of the patent application scope and the description of the invention is Modifications are still within the scope of the invention.
11‧‧‧第一處理槽11‧‧‧First treatment tank
12‧‧‧第二處理槽12‧‧‧Second treatment tank
120‧‧‧連接管120‧‧‧Connecting tube
13‧‧‧燃燒室13‧‧‧ combustion chamber
14‧‧‧抽風管14‧‧‧Exhaust pipe
141‧‧‧抽風端141‧‧‧Exhaust end
142‧‧‧排放端142‧‧‧ discharge end
143‧‧‧抽風扇143‧‧‧fan
2‧‧‧廢棄鋁渣2‧‧‧Disposable aluminum slag
3‧‧‧水3‧‧‧ water
901~908‧‧‧步驟901~908‧‧‧Steps
圖1是本發明廢棄物處理再生能源方法及其系統之第一較佳實施例的系統配置圖；圖2是本發明廢棄物處理再生能源方法及其系統之第一較佳實施例的步驟流程圖；圖3是本發明廢棄物處理再生能源方法及其系統之第二較佳實施例的系統配置圖；及圖4是本發明廢棄物處理再生能源方法及其系統之第二較佳實施例的步驟流程圖。1 is a system configuration diagram of a first preferred embodiment of a method and a system for recycling waste energy of the present invention; and FIG. 2 is a flow chart of a first preferred embodiment of the method and system for recycling waste energy of the present invention Figure 3 is a system configuration diagram of a second preferred embodiment of the waste treatment and regenerative energy source method and system thereof of the present invention; and Figure 4 is a second preferred embodiment of the waste treatment and regenerative energy source method and system thereof of the present invention Step flow chart.
901~908‧‧‧步驟901~908‧‧‧Steps
Claims (9)
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| TWI614348B (en) * | 2015-01-12 | 2018-02-11 | Yi Hsing Huang | Aluminum slag stabilizer |
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4569723A (en) * | 1983-10-12 | 1986-02-11 | Lyon John P | Salt recovery from aluminum black dross |
| TW233312B (en) * | 1992-11-11 | 1994-11-01 | Ind Tech Res Inst | A recovery and stabilization process for secondary aluminum residue |
| TW332195B (en) * | 1994-09-29 | 1998-05-21 | Ind Thchnology Res Inst | Manufacturing method of ceramic face brick from recycled aluminum slag |
| TW200718481A (en) * | 2005-11-11 | 2007-05-16 | Yu-Huo Wu | Resource disposal method of secondary aluminum dross |
| KR20100113902A (en) * | 2009-04-14 | 2010-10-22 | 김재수 | Aluminum dross and carbone use water ammonia and acctylene gas process method |
| TW201038746A (en) * | 2009-04-16 | 2010-11-01 | Hung Yi Co Ltd | The method to hydrolyze and stabilize aluminum dross and aluminum dust |
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Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4569723A (en) * | 1983-10-12 | 1986-02-11 | Lyon John P | Salt recovery from aluminum black dross |
| TW233312B (en) * | 1992-11-11 | 1994-11-01 | Ind Tech Res Inst | A recovery and stabilization process for secondary aluminum residue |
| TW332195B (en) * | 1994-09-29 | 1998-05-21 | Ind Thchnology Res Inst | Manufacturing method of ceramic face brick from recycled aluminum slag |
| TW200718481A (en) * | 2005-11-11 | 2007-05-16 | Yu-Huo Wu | Resource disposal method of secondary aluminum dross |
| KR20100113902A (en) * | 2009-04-14 | 2010-10-22 | 김재수 | Aluminum dross and carbone use water ammonia and acctylene gas process method |
| TW201038746A (en) * | 2009-04-16 | 2010-11-01 | Hung Yi Co Ltd | The method to hydrolyze and stabilize aluminum dross and aluminum dust |
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