TW538019B - Kitchen leftover fermentation and fermentation-free liquefying fertilizer treatment system - Google Patents
Kitchen leftover fermentation and fermentation-free liquefying fertilizer treatment system Download PDFInfo
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- TW538019B TW538019B TW89116915A TW89116915A TW538019B TW 538019 B TW538019 B TW 538019B TW 89116915 A TW89116915 A TW 89116915A TW 89116915 A TW89116915 A TW 89116915A TW 538019 B TW538019 B TW 538019B
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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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
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538019538019
傳統的廚餘處理機程序參照第一圖所示,廚餘 =絞碎機10的處理,使其體積縮小;再來經過 ^ ^ 處理,將殘渣中的油水擠",減少殘渣的重量,:2。的 兩道處理後所得之殘渣量為其處理前之1/3〜1/6量, 有兩種方式處理殘渣’—為將其發酵6G成肥料再做利用: 為將之視為垃圾丢棄7 〇。而經由擠油機所擠出的油 合物部分,則需奴M ^ 、 刀 〜而、、二過一油水分離設備3 0,將其分解為水和 由刀別儲放於水收集桶及油收集桶。所分離出來的油可 538019 五、發明說明(2) --- =次用來作為清,劑原料80,水則排放至下水道9 士殘渣造成水官的堵塞’或是產生有毒物會 污染而增加污水處理之費用。 、^衣*兄造成 傳統的錢處理機確實已㈣ 重罝,回收已絞碎之廚餘殘渣廢物#作堆肥心之二積及 源回收的目的。但是在發酵或堆肥,兩 、山達到資 費工或耗電,甚至會產生發臭及怎友而、",,s的費時、 易侵蝕機器内部構造。咸短機器;。:氣等有毒物質’ 時間及次^降低機器的整體工作效:::二=的 險因子增高。若沒有經過發酵的叙从 作¥纟兄的危 渣當作垃圾一般處理,雖铁I#積而直接將擠完油殘 ,但是在其埋入土壤做分解量都已有明顯的減少 "所丨F用之時,你合甚4 物有害現象及有毒物質,對環境造成二次“。:::作 餘的殘渣物應做成液肥,即不合A & '、 U此將廚 才能達到高度的資源回收率,唯罐吐Γ作物及% 1兄污染, 人千、、隹4生活環境的品質。 傳統處理廚餘的發酵程序皆在發酵機内進 速度的緩慢及耗電,也一直是為A1 且务酵 進行中,一般需要經過心二處到以作用 的程度1但此;ίΠ未能腐熟,而產生作物傷::ΐί ,一般堆肥之腐热要達到完全成熟的程戶 ',問碭 時間。堆肥所需要的發酵時間太長,= 6個月的 甚為低落。 k成處理廚餘的速度The traditional food waste processor program is shown in the first figure, and the food waste is processed by the crusher 10 to reduce its volume. Then, ^ ^ treatment is performed to squeeze the oil and water in the residue to reduce the weight of the residue. :2. The amount of residue obtained after the two treatments is 1/3 to 1/6 of the amount before the treatment. There are two ways to treat the residue'—for fermenting 6G into fertilizer for reuse: Discard it as garbage 7 〇. The oil compound extruded through the extruder requires M ^, knives, and two-to-one oil-water separation equipment 30 to decompose it into water and store it in a water collection bucket and a knife. Oil collection barrel. The separated oil can be 538019. 5. Description of the invention (2) --- = used for cleansing, raw material 80, and water is discharged to the sewer. 9 Residues cause blockage of water officials' or the production of toxic substances will pollute and Increase the cost of sewage treatment. The traditional money processing machine is indeed heavy, and the grated kitchen waste residues # are recycled for composting purposes and source recovery purposes. However, during fermentation or composting, the cost of labor or power consumption in the two or mountain areas may even produce odors, odors, " s, which are time-consuming and easy to erode the internal structure of the machine. Salty short machine ;. : Qi and other toxic substances' time and time ^ reduce the overall working efficiency of the machine ::: two = the risk factor increases. If the fermented slag used as ¥ 发酵 brother's dangerous slag is generally treated as garbage, although iron I # accumulates and directly squeezes out the oil residue, the amount of decomposition in its buried soil has been significantly reduced " Therefore, when you use F, you will combine 4 harmful phenomena and toxic substances, which will cause a secondary environment. "::: The remaining residue should be made into liquid fertilizer, which is not suitable for A & Achieved a high rate of resource recovery, only pots of Γ crops and% 1 contaminated, the quality of the living environment of thousands of people, 隹 4. The traditional fermentation process of processing food waste is slow in the speed and power consumption of the fermentation machine, has also been It is for A1 and the fermentation is in progress. Generally, it needs to go through two places to the degree of function1 but this; ίΠ fails to rot, and crop injury is caused: ΐ ,, the decomposing heat of general compost must reach full maturity. Ask the time. The fermentation time required for composting is too long, which is very low for 6 months. The speed of processing kitchen waste
第5頁 538019 五、發明說明(3) 5 - 3發明目的及概述: 本發明的提出是結合油水處理系統、殘渣處理系統以 及滅菌生成液化肥處理系統的更進一步發展。 本發明的第一個目的是將廚餘利用本系統變成有用的 液化肥,沒有廢水,合乎環保觀念,完全利用廚餘之成分 ,達到資源回收的目的,減少垃圾的產量及環境的污染。 本發明的第二個目的是利用油水處理系統、殘渣處理 系統以及滅菌處理系統的良好結合,以達到迅速且大量處 理含水量高及含油廚餘之目的。 本發明的第三個目的是利用自行設計之高溫高壓滅菌 生成液化肥系統,消滅漿狀廚餘殘渣中之可能有害細菌, 並添加新型對土壤有益的微生物菌種,以抑制當此種液體 肥料在後續埋入土壤後所生成之有害毒素,避免發生二次 污染的現象。 本發明的第四個目的是利用生產液態肥料在土壤中才 發酵而不產生對作物傷害的特性,並結合高溫高壓的殺菌 模式及新型微生物菌種的加入,使得在·生產過程中,不會Page 5 538019 V. Description of the invention (3) 5-3 Purpose and summary of the invention: The present invention is a further development of the oil and water treatment system, the residue treatment system, and the sterilized liquefied fertilizer treatment system. The first object of the present invention is to turn kitchen waste into a useful liquefied fertilizer using the system, without waste water, in accordance with environmental protection concepts, and fully using the ingredients of kitchen waste to achieve the purpose of resource recovery, reduce waste production and environmental pollution. The second object of the present invention is to use a good combination of an oil-water treatment system, a residue treatment system, and a sterilization treatment system, so as to achieve the purpose of quickly and massively processing high water content and oily food waste. The third object of the present invention is to use a self-designed high-temperature and high-pressure sterilization to generate a liquefied fertilizer system, eliminate potentially harmful bacteria in the slurry-like kitchen waste residue, and add new microbial strains that are beneficial to the soil to prevent such liquid fertilizers. Harmful toxins generated after subsequent burial in the soil to avoid secondary pollution. The fourth object of the present invention is to utilize the characteristics of producing liquid fertilizers to ferment in the soil without causing damage to the crops, combined with the high-temperature and high-pressure sterilization mode and the addition of new microbial strains, so that during the production process, no
第6頁Page 6
的詳細說明及附說:…點在發明Detailed description and attached: ... points in the invention
的詳細說明 第 - ' 〜廚餘i ΐ為廚餘液化肥處理系統之簡易流程圖至少包含 理系统50 0。糸統1〇0、一電磁閥4 0 0及一滅菌生成液化肥處 在第- 1 〇 0谁圖的實施例中’廚餘直接進入廚餘處理系統 此嘮办, 處理後所得之產物為油及一漿狀物質,將 狀物暂{一 埋系统 貝、、生由電磁閥 4 0 0之控制送入滅菌生成液化肥處 )¾ ^ 〇 〇中進行處理,即可得到所要生產之液化肥。而 回收作Α、兔, F為清潔劑之原料。Detailed description Section-'~ Kitchen waste i ΐ is a simple flowchart of a kitchen waste liquefied fertilizer processing system including at least the physical system 501. The system 100, a solenoid valve 400, and a sterilized liquefied fertilizer are in the embodiment of the figure-100. 'Food waste directly enters the food waste processing system. The product obtained after processing is The oil and a slurry-like substance are temporarily processed (the control system is sent to the sterilized liquefied fertilizer by the control of the solenoid valve 400), and the liquid to be produced can be obtained. fertilizer. Recovered as A, rabbit, F is the raw material of detergent.
五、發明說明(5) 因為蜮菌生成液化肥處理系 環境下運作,若在非密閉式介^ ’ 而要在咼溫高壓的 條件’因此滅菌生成液化肥系‘:二怕無法達到其所需之 須藉由一電磁閥4 0 0分開運作,〃At对餘處理系統1 0 0必 處理系統1 〇 〇運作時,滅菌生 =同時運作。當廚餘 閥400因此不通過電流而閘門開夜啟化肥系統5〇〇關閉,電磁 形成之漿狀物質通過閘門而至滅菌生=餘經過處理後所 ,當此系統開啟電源開始運成作囷時生= 而問門關閉,€此系統有-封閉式^門則到電;^ 4〇。因通電 態下進行運作。 ”才’式工間到達高溫高壓的狀 =三圖為廚餘處理系統100的詳細系統方塊圖,其至 =前處理系統110、一油水處理系統2〇〇及一 理糸統3 0 0。 在第三圖的實施例中,廚餘直接傾倒於前處理系統 Π 〇中進行處理,而分離成油水及乾殘渣。油水進入油水 處理系統中進行處理,將水、油及内含之細渣分開;而乾 殘 >查則進入殘渣處理系統中進行處理,得到的產物為一漿 狀物質。油水處理系統2 〇 〇及殘渣處理系統3 0 0皆為獨立之 系統’因此可同時運作而不會互相影響,增加處理的速度V. Description of the invention (5) Because it is operated under the environment of the liquefied fertilizer treatment system of the fungus generation, if it is in a non-closed medium ^ ', it must be under the conditions of high temperature and high pressure'. Therefore, the liquefied fertilizer system is sterilized. Need to be separated by a solenoid valve 400, 〃At the remaining processing system 100 must be processed system 1000 operation, sterilization = simultaneous operation. Therefore, when the food waste valve 400 does not pass the current, the gate is opened and the fertilizer system is closed at 500. The electromagnetically formed slurry is passed through the gate to sterilize the waste = after the treatment, the system starts to operate when the power is turned on.时 生 = While the door is closed, this system has-closed ^ door to electricity; ^ 4〇. The operation is performed because the power is on. The state of the “cai” -type workshop reaching high temperature and high pressure = The three pictures are detailed system block diagrams of the food waste treatment system 100, which are = pretreatment system 110, an oil and water treatment system 2000, and a system 300. In the embodiment of the third figure, the food waste is directly dumped into the pre-treatment system Π 〇 for treatment, and separated into oil water and dry residue. The oil and water enter the oil and water treatment system for processing, and the water, oil and fine residue contained therein are processed. Separate; and dry residues> check into the residue treatment system for processing, the product obtained is a slurry. The oil and water treatment system 2000 and the residue treatment system 300 are independent systems, so they can operate simultaneously. Does not affect each other, increasing processing speed
第8頁 538019 五、發明說明(6) 第四圖為一前處理李蜞1 1 ^ ^ ^ ^ ^ ^ 1 1 〇 ^ U 0的砰細方塊圖,其至少包 含一疋里輸送4置1 1 2、一、、山日匕、、士、土壯 /由月曰冲洗裝置1 1 5及一加熱器117° 將廚餘 第四圖的實施例中,两於 以宗旦66古4、、,廚餘直接傾倒於定量輸送裝置’ 以疋里的方式送入機哭由考 間内進入機器中,i:處以防止過多的廚餘 在短時間内進入機器中,;軍以防止過多的廚餘 之目的。將定量送入的廚利用螺距來達到定量輸送 油水及乾殘渣兩大部分了 ‘二過7過濾裝置11 9後,分為 ’不易藉由濾網從厨餘殘逢中:ΐ水i:!:”易凝固器117。績遺,所提到之油水分離設備2;〇=:加熱 分離出來之水’經由玆‘也w 4〜I,照弟五圖 )所分離出來之水,、經由該加熱器117加 ^ 了弟五圖 t後,灌於過繼U 9上之殘逢中進行油、,〜55 分解已凝固的油脂,使其與殘渣分離。 r况11 5,可 第五圖為一油水處理系統 至少包含一油水分離設備2 1 〇、 一抽水幫浦2 4 0。 2 0 0的詳細系統方塊圖 —油槽22 0、—水槽 ,其 2 3 0及 第五 餘中分離出參照第。圖)後隨即進入一從禮 行油與水的分離。將分離出來的油導刀隹:伟 而將分離出來的水導入水槽2 3 0中暫存。在Λ 日1卞 在油水分, 210,進 中Page 8 538019 V. Description of the invention (6) The fourth picture is a thin block diagram of a pre-processed Li 蜞 1 1 ^ ^ ^ ^ ^ ^ 1 1 〇 ^ U 0, which contains at least one mile to convey 4 set 1 1 2. First, the mountain sun dagger, Shishi, Tu Zhuang / Yueyue washing device 1 1 5 and a heater 117 ° will be used in the fourth embodiment of the kitchen waste, two in the Zongdan 66 ancient 4 ,,, The food waste is dumped directly into the quantitative conveying device. It is fed into the machine in a cricket manner and enters the machine from the test room, i: to prevent excessive food waste from entering the machine in a short time; the military to prevent excessive food waste Purpose. The fixed-feed kitchen uses a pitch to achieve the quantitative delivery of oil and water and dry residue. After passing through the 7 filter device 11 9, it is divided into 'It is not easy to pass from the kitchen waste through the filter screen: ΐ 水 i :! : "Easy coagulator 117. Ji Yi, the mentioned oil-water separation equipment 2; 〇 =: the water separated by heating 'through here' also w 4 ~ I (according to the figure of the brother 5)), After the heater 117 is added to the fifth figure t, it is filled with oil on the relay U 9 to carry out oil, ~ 55 to decompose the solidified oil and separate it from the residue. R Condition 11 5, can be the fifth figure It is a detailed system block diagram of an oil-water treatment system including at least one oil-water separation device 2 1 0 and a pumping pump 2 4 0. 2 0 0-an oil tank 22 0 and a water tank, 2 3 0 and a fifth of which are separated. (Refer to the figure.) Then immediately enter a separation from the saluting oil and water. The separated oil guide knife 隹: Wei and the separated water is introduced into the water tank 2 30 for temporary storage. On the Λ day 1 in the oil Moisture, 210
538019 五、發明說明(7) 的過程中還可得到一細渣 9 0 0,此殘渣為細微顆粒之廚餘 ,因為顆粒過於微小而無法被過濾裝置所過濾,導致在油 水分離的過程中被分離出來。分離出來的細渣 9 0 0回收至 殘渣處理系統 3 0 0進行處理。分離出來的油可回收作清潔 劑原料 7 0 0,減少對環境的污染。而分離出來的水則利用 一抽水幫浦 2 4 0回收至兩處,一處為回收至殘潰處理系統 3 0 0中(參照第三圖)進行再利用2 6 0,另一處為回收至加 熱器中進行加熱以作油脂沖洗2 7 0。538019 V. Description of the invention (7) A fine slag 9 0 0 can also be obtained during the process of the invention. The residue is fine-grained food waste, because the particles are too small to be filtered by the filtering device, resulting in the oil-water separation process. separate from. The separated fine slag 9 0 0 is recycled to the residue processing system 3 0 0 for processing. The separated oil can be recycled as a detergent raw material 700, reducing environmental pollution. The separated water is recycled to two places by a pumping pump 240, one is recycled to the residual treatment system 300 (refer to the third figure) for reuse and the other is recycled. Heat in a heater for grease washing 2 70.
第六圖為一殘渣處理系統 3 0 0的詳細系統方塊圖,其 至少包含一絞碎機3 1 0及一研磨機3 3 0,其中絞碎機至少包 含一組刀片3 1 5 (參照第七圖);而研磨機至少包含一研磨 刀刃3 3 5及一研磨壁3 4 0 (參照第八圖)。The sixth figure is a detailed system block diagram of a residue treatment system 300, which includes at least a grinder 3 1 0 and a grinder 3 3 0, wherein the grinder includes at least a set of blades 3 1 5 (refer to Figure 7); and the grinder includes at least a grinding blade 3 3 5 and a grinding wall 3 4 0 (refer to Figure 8).
第六圖的實施例中,當乾殘渣經由前處理系統1 1 0 (參 照第四圖)從廚餘中分離出來後,隨即進入絞碎機3 1 0進行 絞碎的動作。使用的絞碎機是由馬達來帶動一組刀片 315 (參照第七圖),對所進入的物體進行絞碎的動作,其轉 速約為1 7 2 0 r p m,進入的乾殘渣經絞碎後其顆粒之粒徑大 小約大於0 . 5公分。 在絞碎殘渣的過程中通常需要加入水做為潤滑劑或冷 卻劑,以防止刀片在做絞碎動作時因為摩擦產生高熱而影 響刀片的壽命;或是因為絞碎後的殘渣黏附在刀片上造成In the embodiment of the sixth figure, when the dry residue is separated from the food waste through the pre-processing system 1 10 (refer to the fourth figure), it then enters the mincing machine 3 1 0 to perform the mincing action. The mincing machine used is a motor to drive a group of blades 315 (refer to the seventh figure) to perform a mincing action on the entered object, and the rotation speed is about 1720 rpm. Its particle size is greater than about 0.5 cm. Water is usually added as a lubricant or coolant in the process of crushing the residue to prevent the blade from affecting the life of the blade due to the high heat generated by friction during the crushing action; or because the residue after the crushing adheres to the blade Cause
第10頁 538019 五、發明說明(8) 力:入的水可利用經過油水分離設備 外…水回收做為水源,而毋須另 有-引導的功 二 3 3 0中繼續處理。而妳+1俊勺歹欠/查引钕敎研磨機 所分離出來的细、、杳90二0 ΐί分離設備210(參照第五圖) 。 丨的、^查也是導入絞碎機31〇中進行再處理 將已絞碎的殘渣送入研磨機33〇中進行研磨 碎後的殘渣顆粒其粒徑大小約大於。因因 设计為一漏斗开“參照第八圖)以利運轉。研磨::此 345處九研,刀刃335與研磨壁—之間的距離約為口 ===4後之殘·座進人進行研磨;在研磨機出料口 $ ^刀=研磨刀刀3 35與研磨壁34〇之間的距離頸縮為。^ 刀^因此奴碎後之殘渣經研磨後其粒徑約大於〇. 〇 △ 所使用之研磨機330轉速約為345〇rpm。 刀。 在研磨的過程中需加入水作引導及冷卻之 Π刃335在做研磨動作時因為摩擦產生高熱影塑= 的哥命;或是因為絞碎後的殘潰黏附在刀片上 ,的降…引導正進行研磨中的殘渣往研 :里效 350移動使其顆粒越磨越細並和水混合成一渡狀物質+,、、& 入滅菌生成液化肥處理系統5〇〇中。所使用的的水源w 碎機所使用後引導殘渣進Λ研磨機33〇之水’毋須另Page 10 538019 V. Description of the invention (8) Force: The incoming water can be used outside the oil-water separation equipment ... water recovery as a water source, without the need for additional-guided work. And you +1 歹 歹 歹 查 / check the Nd 敎 grinding machine to separate the fine, 杳 90 0 20 ΐ separation equipment 210 (refer to the fifth figure). The inspection is also introduced into the grinder 31 for reprocessing. The ground residue is sent to the grinder 33 for grinding and the size of the residue particles after crushing is about larger than that. Because it is designed as a funnel to open (refer to the eighth figure) to facilitate the operation. Grinding :: The distance between the blade 335 and the grinding wall at this 345 Nine Research Institute is about the residue after the mouth === 4 Grinding; the distance between the grinder outlet $ ^ knife = grinding knife knife 3 35 and the grinding wall 34 0 necked to. ^ Knife ^ so the residue after crushing after grinding the particle size is greater than about 0. 〇 △ The speed of the grinder 330 used is about 3450 rpm. Knife. During the grinding process, water needs to be added for guidance and cooling. The razor blade 335 has a high thermal image due to friction during the grinding action. It is because the crushed residue adheres to the blade, and it guides the residue that is being ground to the ground: the Li 350 moves to make the particles finer and finer and mixes with water to form a substance + ,,, & amp Into the sterilization generated liquefied fertilizer treatment system 500. The used water source w crusher is used to guide the residue into the water of the Λ grinder 33〇 'without additional
538019 五、發明說明(9) 設水源,以增加資源的回收率並減低成本。 第九圖為滅菌生成液化肥處理系統 5 0 0至少包含一滅 菌桶5 0 5、循環冷卻裝置5 1 0、循環馬達 5 1 5、循環加熱裝 置5 2 0、循環幫浦5 2 5、液化肥出口 5 4 0、消泡電極5 4 5、進 料口 5 5 0、排氣口 5 5 5及加壓蓋560。其中滅菌桶内50 5至少 包含有一撲:拌葉片530,滅菌桶50 5内部或外部至少包含有 一組磐附在桶壁的高壓鋼管5 3 5。 第九圖的實例中,經由廚餘處理系統 1 0 0處理過後的 漿狀物質隨即經由電磁閥 4 0 0的控制進入滅菌生成液化肥 處理系統5 0 0中做處理(參照第二圖)。當漿狀物質從進料 口進料時’滅囷生成液化肥糸統之電源關閉’電磁闊 400 的閥門因未通電而形成一開啟狀態,使漿狀物質能順利進 入滅菌桶中,當加入的漿狀物質到達滅菌桶的一定容量時 即打開滅菌生成液化肥處理系統 5 0 0之電源,此時電磁閥 4 0 0因通過電流而使閥門關閉並蓋上加壓蓋停止進料的動 作。因為此系統需要在高溫高壓下進行滅菌的工作,所以 滅菌桶 5 0 5中不能完全充滿待殺菌之漿狀物質,必須留下 一點空間以防止氣爆的發生。 經過廚餘處理系統 1 0 0所產生的漿狀物質内涵許多有 害微生物菌,在其後發酵的過程中會產生有毒的物質造成 二次公害,因此必須利用高溫高壓的環境來做殺菌的動作538019 V. Description of the invention (9) Set up water source to increase resource recovery rate and reduce cost. The ninth picture is a sterilization generated liquefied fertilizer treatment system 5 0 0 including at least a sterilization barrel 5 5, a circulating cooling device 5 1 0, a circulating motor 5 1 5, a circulating heating device 5 2 0, a circulating pump 5 2 5, a liquid The fertilizer outlet 5 4 0, the defoaming electrode 5 4 5, the feed inlet 5 5 0, the exhaust outlet 5 5 5 and the pressure cover 560. The sterilization bucket 50 5 contains at least one flap: the mixing blade 530, and the sterilization bucket 50 5 contains at least a set of high-pressure steel pipes 5 3 5 attached to the barrel wall. In the example of the ninth figure, the slurry-like substance processed by the food waste treatment system 100 is then controlled by the solenoid valve 400 to enter the sterilization and liquefied fertilizer treatment system 500 (see the second figure). When the slurry-like substance is fed from the feed port, the power of the "elimination of liquefied fertilizer system is closed" electromagnetic 400 valve is opened because it is not energized, so that the slurry-like substance can enter the sterilization barrel smoothly. When the slurry-like substance reaches a certain capacity in the sterilization barrel, it turns on the power supply of the sterilization fertilizer processing system 500, and at this time, the solenoid valve 400 closes the valve due to the current flow and closes the pressure cap to stop the feeding operation. . Because this system needs to be sterilized under high temperature and pressure, the sterilization barrel 5 05 cannot be completely filled with the pulpy substance to be sterilized, and a little space must be left to prevent the occurrence of gas explosion. The slurry-like substance produced by the food waste treatment system 100 contains many harmful microorganisms. During the subsequent fermentation process, toxic substances will be generated to cause secondary pollution. Therefore, high temperature and high pressure environment must be used for sterilization.
538019 五、發明說明(ίο) ’通常依醫學殺菌標準而言是採用1 2 TC維持三十分鐘來 殺菌。而以本滅菌生成液化肥處理系統5 0 〇而言是採用溫 度為1 2 1C〜1 30°C,壓力為2〜3 lb/cm2,維持3〇分鐘的環 境來做為滅菌的處理。 滅菌桶5〇5所採用的加熱方式可為一間 力二的進方: Π,, /2Vc° ;^ ^ ?r, Μ ^ ^ 刀口熱到125C〜135C並持續加熱錐拄i π麻 如 循環幫浦5 2 5導入環繞在滅菌桶外皿又,再藉由加熱 "環-圈後二外 環的熱能帶往高壓鋼管5 35内,間接#亩^;,此一流動循 。因為溫度不斷上升而滅菌桶頂;u對滅菌桶加溫 容積,導致滅菌桶内之壓力不斷 〇 ^5 6 0密封整個 成為一高溫高壓之環境。 间使滅囷桶内之環境 营Ϊ 1 : ί Ϊ囷生成液化肥處理系、统5 0 0運作之、H 。百先由廚餘處理系統1GG處理 2 U王圖 閥40 0的控制進人滅菌桶中進曼々二二物貝經由電磁 菌生成液化肥處理系統5 0 0啟動時务^在肥系統。當滅 環境820利於滅菌,隨後攪拌葉片開妒 一〃高溫高壓之 務使滅菌桶内之漿狀物質的每一^ 仃攪拌8 3 0, 高壓環境下進行消毒殺菌的動: 的暴露在高溫 I思者^度之上昇壓力也538019 V. Description of invention (ίο) ′ Generally speaking, according to medical sterilization standards, 1 2 TC is maintained for 30 minutes to sterilize. In the case of the sterilization liquefied fertilizer treatment system 500, the sterilization treatment is performed by using a temperature of 12 1C to 1 30 ° C, a pressure of 2 to 3 lb / cm2, and maintaining the environment for 30 minutes. The heating method used by the sterilization bucket 505 can be a force of two: Π ,, / 2Vc °; ^ ^? R, Μ ^ ^ The knife edge is heated to 125C ~ 135C and the cone 拄 i π 麻 如 is continuously heated The circulation pump 5 2 5 is introduced around the outer plate of the sterilization barrel, and then the heat energy of the second outer ring is brought into the high pressure steel pipe 5 35 by heating "ring-ring", and this flow is indirect. The top of the sterilization barrel is heated because the temperature is constantly rising; u Heating the volume of the sterilization barrel causes the pressure in the sterilization barrel to be continuously sealed. The entire environment becomes a high temperature and high pressure environment. The environment inside the bucket to destroy the battalion 1: ί Ϊ 囷 generates liquefied fertilizer treatment system, system 500 operation, H. Baixian is processed by the kitchen waste treatment system 1GG 2 U King chart The control of the valve 40 0 is put into the sterilization tank and the manganese 22 is processed by the electromagnetic bacteria to generate a liquefied fertilizer treatment system 5 0 0 Start the task ^ in the fertilizer system. When the environment 820 is conducive to sterilization, then the stirring blades are envious of high temperature and high pressure to stir each of the paste-like substances in the sterilization bucket 8 8 0. The disinfection and sterilization under high pressure environment: exposure to high temperature I The pressure of thinkers
538019 五、發明說明(11) 隨之增加,當超過所需之壓力繼續往上攀升時,有可能會 造成系統的氣爆現象,因此必須要有一安全排氣閥進行通 氣 8 4 0的動作,確保系統運作之安全性。當漿狀物質在高 溫高壓的環境下進行攪拌時會產生出氣泡,這些氣泡均有 可能隱藏些許未經消毒的微生物菌,會為之後的發酵作用 帶來毒素,因此在滅菌桶内裝設電極,在系統運作時通電 打散泡泡簡稱消泡 8 5 0作用。當系統處理三十分鐘後,代 表殺菌過程完成,即將對系統進行降溫的動作8 6 0。 本系統利用冷卻循環幫浦 5 1 5將水導入滅菌桶外部的 冷卻壁 5 3 7中進行降溫的動作。循環冷卻裝置的體積通常 設計為所需水量的2〜3倍,藉以冷卻循環水之溫度並加快 降溫速率。在本系統設計中,加熱時採用高壓鋼管,而在 冷卻時則將液體充滿機器外壁和滅菌桶壁間的冷卻壁 53 7 | 中以達儘速降溫。 當系統降溫至4 0°C以下時,即可添加微生物菌種至漿 狀物質中,即為菌種混合 8 7 0的過程。在此過程中,可添 加兩種菌種,一種為新型對土壤有益之菌種,或另一種為 發酵之菌種。 而本實施例所添加之新型微生物菌種為對土壤有益之 菌種。因此本實施例是採機外發酵,即為等到液態肥加入 土壤中使用時,才開始進行發酵的作用,而所加入的微生538019 V. Description of the invention (11) Increases accordingly. When the pressure exceeds the required pressure and continues to climb upwards, it may cause gas explosion in the system. Therefore, a safety exhaust valve must be used to ventilate 8 4 0. Ensure the security of system operation. When the slurry-like substance is stirred under high temperature and high pressure environment, bubbles will be generated. These bubbles may hide some unsterilized microorganisms and bring toxins for subsequent fermentation. Therefore, electrodes are installed in the sterilization barrel. When the system is in operation, the bubbles will be de-energized for short. When the system is processed for 30 minutes, it means that the sterilization process is completed, and the system will be cooled down 8 6 0. This system uses the cooling circulation pump 5 1 5 to introduce water into the cooling wall 5 3 7 outside the sterilization bucket to lower the temperature. The volume of the circulating cooling device is usually designed to be 2 to 3 times the amount of water required to cool the temperature of the circulating water and accelerate the cooling rate. In the design of this system, high-pressure steel pipes are used during heating, and liquid is filled into the cooling wall 53 7 | between the outer wall of the machine and the wall of the sterilization tank during cooling to achieve rapid cooling. When the temperature of the system drops below 40 ° C, microbial strains can be added to the slurry, which is the process of mixing 870 strains. In this process, two kinds of bacteria can be added, one is a new strain that is good for soil, or the other is a fermentation strain. The new microbial strain added in this embodiment is a strain beneficial to the soil. Therefore, this embodiment is the fermentation outside the harvester, that is, when the liquid fertilizer is added to the soil for use, the fermentation is started.
538019 五、發明說明(12) 物菌種,其功能為抑制毒素之產生,使得此液化物質在土 壤中進行發酵作用時,不會產生有毒物質造成二次污染。 當所加入的菌種為另一發酵菌種時,則在菌種混合 8 7 0的步驟完成並生成液化肥產物後,必須再放入發酵桶 中進行大約1 2〜7 2小時之發酵,此液化肥才為真正可利用 之產物。移至發酵桶中進行發酵的過程,一方面可使機器 不會因為發酵的作用停止運作,另一方面可維護機器壽命 ,使其不受發酵中有毒物質之影響。 當漿狀物質與對微生物菌種充分混合之後,系統即可 經由出料口進行出料 8 8 0,即為本系統所欲產生的成品液 化肥。 第十一圖為本系統處理廚餘使其生成液化肥之各階段 j 綜合流程圖。放入之廚餘首先經過前處理系統分離為油水 及乾殘渣兩大部分。油水部分經由油水分離設備分離成油 及水,分離出的油可當清潔劑之原料,分離出之水可回收 再做利用(參照第二、三、四圖)。乾殘渣部分則進入絞 碎機及研磨機中進行處理,產物為一漿狀物質。再將此種 漿狀物質送入滅菌桶中進行滅菌生成液化肥處理,即可得 到一新產品液化肥(參照第五、六、七、八、九圖)。 以上關於本發明的描述僅為最佳範例而已,足可使一538019 V. Description of the invention (12) The species strain has the function of inhibiting the production of toxins, so that when the liquefied substance is fermented in the soil, it will not produce toxic substances and cause secondary pollution. When the added strain is another fermented strain, after the steps of mixing the strains 870 and generating the liquefied fertilizer product, it must be put into the fermentation tank for about 12 to 72 hours of fermentation. This liquefied fertilizer is a truly usable product. The process of moving to the fermentation tank for fermentation will not only stop the machine from stopping due to the fermentation, but also maintain the life of the machine and prevent it from being affected by the toxic substances in the fermentation. After the slurry-like substance is sufficiently mixed with the microbial species, the system can discharge 8 8 0 through the discharge port, which is the finished liquid chemical fertilizer that the system wants to produce. The eleventh figure is a comprehensive flow chart of each stage of the system's processing of food waste to produce liquefied fertilizer. The putted food waste is first separated into oil and water and dry residue by the pretreatment system. The oil and water are separated into oil and water by oil-water separation equipment. The separated oil can be used as the raw material of the cleaning agent, and the separated water can be recovered and reused (refer to the second, third, and fourth figures). The dry residue is then processed in a crusher and a grinder, and the product is a slurry. Then the slurry-like substance is sent to a sterilization barrel for sterilization to produce liquefied fertilizer, and a new product liquefied fertilizer can be obtained (refer to Figures 5, 6, 7, 8, and 9). The above description of the present invention is only the best example, which is enough to make one
538019 五、發明說明(13) 具有一般技術者製作並使用,具一般技術者可暸 實施例的各種變化組合及等效者。本發明不限於 ,更包含符合後述之專利申請範圍精神的所有實 解本較佳 本實施例 施例。 538019 圖式簡單說明 第一圖為傳統廚餘處理機之運作流程圖; 第二圖為本發明之系統處理廚餘使其轉換為液態肥之 簡易流程圖; 第三圖為本發明系統中所使用之廚餘處理系統處理廚 餘時之流程圖; 第四圖為本發明系統中所使用之前處理系統分離乾殘 渣與油水之流程圖; 第五圖為本發明系統中所使用之油水處理系統處理油 水時之流程圖; 第六圖為本發明系統中所使用之殘逢處理系統處理殘 渣時之流程圖; 第七圖為本發明系統中所使用之粗碎機之俯視圖; 第八圖為本發明系統中所使用之研磨機之剖面圖; 第九圖為本發明系統中所使用之滅菌生成液化肥處理 系統之結構示意圖;538019 V. Description of the invention (13) Those skilled in the art can make and use, and those skilled in the art can understand various combinations and equivalents of the embodiments. The present invention is not limited to, but also includes all practical solutions that are consistent with the spirit of the scope of patent applications described later. 538019 The diagram is briefly explained. The first diagram is the operation flowchart of a traditional food waste processor. The second diagram is a simple flowchart of the system for processing food waste and converting it into liquid fertilizer. The third diagram is the system in the invention. Flow chart of the food waste processing system used for processing food waste; Figure 4 is a flow chart for separating dry residues from oil and water in the pre-treatment system used in the system of the present invention; Figure 5 is a oil and water treatment system used in the system of the present invention Flow chart when processing oil and water; Figure 6 is a flowchart of the residue processing system used in the system of the present invention when processing residues; Figure 7 is a plan view of a coarse crusher used in the system of the present invention; A cross-sectional view of a grinder used in the system of the present invention; the ninth figure is a schematic structural diagram of a sterilized liquefied fertilizer treatment system used in the system of the present invention;
第17頁 538019 圖式簡單說明 第十圖為本發明系統中所使用之滅菌生成液化肥處理 系統運作之流程圖; 第十一圖為本發明之系統處理廚餘使其轉換為液態肥 之詳細流程圖。 主要部份的代表符號: 10 絞 碎 機 20 擠 油 機 30 油 水 分 離 -i-fL 5又 備 40 水 收 集 筒 50 油 收 集 筒 60 發 酵 70 丟 棄 100 廚 餘 處 理 系 統 110 前 處 理 系 統 112 定 量 m 达 裝 置 117 加 埶 i ''X 器 119 過 渡 裝 置 200 油 水 處 理 系 統 2 10 油 水 分 離 設 備 220 油 槽 230 水 槽 240 水 幫 浦538019 on page 17 Brief description of the diagram The tenth diagram is a flowchart of the operation of the sterilized liquefied fertilizer treatment system used in the system of the present invention; the eleventh diagram is the detailed process of the system of the present invention to process food waste and convert it to liquid fertilizer flow chart. Representative symbols of main parts: 10 mincing machine 20 oil squeezer 30 oil-water separation-i-fL 5 and 40 water collecting cylinder 50 oil collecting cylinder 60 fermentation 70 discard 100 food waste treatment system 110 pre-treatment system 112 quantitative m up to Device 117 plus '' X device 119 transition device 200 oil-water treatment system 2 10 oil-water separation equipment 220 oil tank 230 water tank 240 water pump
第18頁Page 18
538019 圖式簡單說明 300 殘 渣 處 理 系 統 310 絞 石卒 機 315 絞 碎 機 所 使 用 之刀 片 330 研 磨 機 335 研 磨 刀 刃 340 研 磨 壁 345 研 磨 機 進 料 V 350 研 磨 機 出 料 Π 40 0 電 磁 閥 500 滅 菌 生 成 液 化 肥處 理系統 505 滅 菌 桶 51 0 循 環 冷 卻 裝 置 51 5 冷 卻 循 環 幫 浦 520 循 環 加 熱 裝 置 525 加 孰 循 環 幫 浦 530 攪 拌 葉 片 535 南 壓 鋼 管 537 冷 卻 壁 539 機 器 外 壁 540 液 化 肥 出 料 口 545 消 泡 電 極 550 進 料 π 555 排 氣 U 560 加 壓 蓋538019 Brief description of the diagram 300 Residue treatment system 310 Rock grinder 315 Blade used by the grinder 330 Grinder 335 Grinding blade 340 Grinding wall 345 Grinder feed V 350 Grinder discharge Π 40 0 Solenoid valve 500 sterilization generation Liquefied fertilizer processing system 505 Sterilization bucket 51 0 Circulating cooling device 51 5 Cooling circulating pump 520 Circulating heating device 525 Heating pump Circulating pump 530 Stirring blade 535 South pressure steel pipe 537 Cooling wall 539 Machine outer wall 540 Liquid fertilizer outlet 545 Defoaming Electrode 550 feed π 555 exhaust U 560 pressure cap
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Claims (1)
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TW89116915A TW538019B (en) | 2000-08-21 | 2000-08-21 | Kitchen leftover fermentation and fermentation-free liquefying fertilizer treatment system |
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TW89116915A TW538019B (en) | 2000-08-21 | 2000-08-21 | Kitchen leftover fermentation and fermentation-free liquefying fertilizer treatment system |
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TW538019B true TW538019B (en) | 2003-06-21 |
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TW89116915A TW538019B (en) | 2000-08-21 | 2000-08-21 | Kitchen leftover fermentation and fermentation-free liquefying fertilizer treatment system |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1557403A1 (en) | 2004-01-26 | 2005-07-27 | Yes-Sun Holdings Limited | System and method for composting-free disposal of organic wastes |
CN106747705A (en) * | 2017-03-21 | 2017-05-31 | 中合生态农业科技有限公司 | Kitchen garbage aerobic treatment system and method |
-
2000
- 2000-08-21 TW TW89116915A patent/TW538019B/en not_active IP Right Cessation
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1557403A1 (en) | 2004-01-26 | 2005-07-27 | Yes-Sun Holdings Limited | System and method for composting-free disposal of organic wastes |
CN106747705A (en) * | 2017-03-21 | 2017-05-31 | 中合生态农业科技有限公司 | Kitchen garbage aerobic treatment system and method |
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