TW485056B - Venting and stirring methods in feeding solid material to horizontal tank and its structure - Google Patents
Venting and stirring methods in feeding solid material to horizontal tank and its structure Download PDFInfo
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- TW485056B TW485056B TW89121412A TW89121412A TW485056B TW 485056 B TW485056 B TW 485056B TW 89121412 A TW89121412 A TW 89121412A TW 89121412 A TW89121412 A TW 89121412A TW 485056 B TW485056 B TW 485056B
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哪056 —---— 五、發明說明(1) 一種固體 自進料口投入 板不僅可攪拌 移動,複數個 夠作生化反應 、 習用之有 送帶來作傳送 拌混合狀況, 來;在習用之 顆粒堆層中, 氣體,效率很 習用之設備, 效用少之現況 且必須常讓 理上會消耗較 因此,如 之解決方法, 成本,長久以 決之困難點所 關研究、開發 窮其個人之專 作樣品及改良 攪拌法及其構 本發明之 通氣攪拌 内,具有 推進該物 充分氧氣 體之混合 設備其物 輸送方式 法得到充 由物料層 因攪拌所 料能夠作 、大體積 處理上會 舊換新, 用所發生 處理生垃 者殷切盼 人基於多 務經驗, 方設計、 出一種固 述之問題 於提供一 法及其構造,將物料 一斜面角度之授拌紫 應槽内作水平 中,使物料能 物料臥 該臥式 該物料 通氣管 ’或固 機廢棄 之動作 常使得 設備中 僅有表 低,無 大都是 下,生 該機械 高的成 何針對 不僅可 來一直 在,而 、及銷 業知識 後,終 造,以 主要目 槽進程 反應槽 ,且可 可提供 體語氣 物處理 ,但該 物料無 ,通常 面亦即 法使物 高價格 垃圾的 設備汰 本0 上述習 有效的 是使用 本發明 售之實 ,經多 於研究 解決上 的,在 料在反 至物料 反應。 料輸送 並無法 分的攪 上方通 揚起之 充分的 、低功 有更多 如此對 方式大 配合物 拌即被 氣,很 物料上 生化反 能、多 的困難 於生垃 多以輸 料之攪 輸送出 難深入 部接觸 應,且 問題及 及麻煩 圾的處 的問題提出一種新穎 圾,且可使用較低的 望及本發明人欲行解 年從事相關產品的相 乃思及改良之意念, 探討,並經無數次試 體物料臥槽進程通氣 。爰是 種固體物料臥槽進程Which 056 ——————— V. Description of the invention (1) A solid self-feeding port input plate can not only stir and move, but also a number of biochemical reactions. In the particle stack, gas, very efficient equipment, the current situation of less utility and must be more reasonably consumed, such as the solution, cost, and long-term difficulties related to research and development The special sample and improved stirring method and the structure of the aeration stirring device of the present invention are provided with a mixing device for advancing the substance with sufficient oxygen gas. The material conveying method method is obtained by filling the material layer due to the stirring. The old ones are replaced with new ones, and the people who use them to deal with the waste earnestly hope that based on multi-service experience, they will design and formulate a fixed problem. Provide a method and its structure, and mix the material with a bevel angle. In the process of enabling the material to lie horizontally or horizontally, or to abandon the solid machine, the action often makes the equipment only have a low surface, and most of them are lower. The aim of the mechanical high is not only to be able to come all the time, but also after the sales knowledge, and finally to build the reaction tank with the main mesh process, and cocoa to provide body tone treatment, but the material is not, usually noodles The equipment of high-price garbage is simple. The above-mentioned practice is effective using the present invention, which is more than research and solution. The material transportation cannot be divided, and the upper channel is fully raised, and the low power has more. This way, the large complex is mixed with the gas, which is very biochemically reactive, and it is difficult to produce more materials. Conveying difficult and deep contact problems, and problems and troublesome problems, propose a new type of waste, and can use a lower hope and the inventor ’s desire to solve the acacia and improvement ideas of related products, Discussed, and ventilated through the process of lying on the body of countless times.爰 is a solid material process
第5頁 485056 五、發明說明(2) 通氣攪拌法及其構造,其可使攪拌作用與輸料速度之間, 不致相互牵制,而可以獨立設定,如此可依生質微生物分 解之生化反應過程,規劃成合理之連續流程。 本發明之次要目地,在於提供一種固體物料臥槽進程 通氣攪拌法及其構造,其可進行物料層内之通氣,削減物 料上方無效通氣,使通氣運用效率大為提升。 本發明之又一目的,在於提供一種固體物料臥槽進程 通氣攪拌法及其構造,其可充分有效處理生垃圾或固體物 ,且該設備機構較為簡單、較不佔體積、及多功能,如此 可節省使用者在使用上所耗費的成本。 茲為使 貴審查委員對本發明之結構特徵及所達成之 功效有共進一步之瞭解與認識,謹佐以較佳之實施例圖及 配合詳細之說明,說明如後: 請參閱第1圖,為本發明一較佳實施例之側視圖;如 圖所示,該臥式反應槽1下方一端有一低位支撐座1 1 , 另一端有一高位支撐座1 3 ,可造成該臥式反應槽1具有 一坡度;進料口 1 2在該槽低位端之上方處、排料口 1 4 在其高位端之下方處、及溢料口 1 6在其高位端之上方處 ;溢料口 1 6處設有一排氣裝置1 5 ,在該排氣裝置1 5 中有匣式貯料槽1 7,且在該溢料口 1 6處設有一篩網; 排水管1 8在該槽之低位端之下方處,且距離該槽底部有 一高度;轉軸兼中空供氣管2設於該槽之中央處,其兩端 設有一鼓風機2 2及攪拌驅動器2 4 ;複數個攪拌槳板2 6以一斜面角度設置於轉軸兼中空供氣管2上,複數個通Page 5 485056 5. Description of the invention (2) The aeration and stirring method and its structure can make the stirring effect and the conveying speed not restrain each other, but can be set independently, so it can be based on the biochemical reaction process of the microbial decomposition , Planning into a reasonable continuous process. A secondary objective of the present invention is to provide a method for aerating a solid material in a horizontal tank and its aeration method, which can perform aeration in the material layer, reduce ineffective aeration above the material, and greatly improve the efficiency of aeration operation. Another object of the present invention is to provide a process for aerating and stirring a solid material in a horizontal tank and its structure, which can fully and effectively treat raw garbage or solid objects, and the equipment mechanism is relatively simple, does not occupy volume, and is multifunctional. It can save users the cost in use. In order to make your reviewing members have a better understanding and understanding of the structural features and achieved effects of the present invention, I would like to refer to the preferred embodiment diagrams and detailed descriptions, as described below: Please refer to FIG. 1 for this A side view of a preferred embodiment of the invention; as shown in the figure, there is a low-level support base 1 1 at one end below the horizontal reaction tank 1 and a high-level support base 1 3 at the other end, which can cause the horizontal reaction tank 1 to have a slope ; The feed port 1 2 is above the low end of the tank, the discharge port 1 4 is below its high end, and the overflow port 16 is above its high end; the overflow port 16 is provided with a The exhaust device 15 has a box-type storage tank 17 in the exhaust device 15 and a screen is arranged at the overflow port 16; the drain pipe 18 is below the lower end of the tank And a height from the bottom of the tank; the rotating shaft and the hollow air supply pipe 2 are arranged at the center of the tank, and a blower 2 2 and a stirring driver 2 4 are arranged at both ends; a plurality of stirring paddle plates 26 are arranged at an inclined plane angle at The shaft and the hollow air supply pipe 2
五、發明說明(3)V. Invention Description (3)
氣管 中空 反應 動, 鼓風 通氣 流力 料槽 少堵 餘水 置, 速生 3各設置 供氣管2 槽1内, 使該複數 機2 2供 ,可提供 及槳板提 1 7,且 阻;可利 至排水管 可保留少 化反應。 於各攪 之中空 攪拌驅 個攪拌 氣至轉 物料足 料可使 以攪拌 用該具 1 8流 許餘水 處相通; 動器2 4 紫板2 6 軸兼中空 夠的氧氣 細微顆粒 所帶動之 有坡度之 出至外部 ,作為過 物料自 驅動轉 可對物 供氣管 可行生 自溢料 物料顆 臥式反 ’且略 度乾燥 且其内 進料口 軸兼中 料攪拌 2内, 化反應 口 1 6 粒,刷 應槽1 高於該 生質潤 部與該 1 2投 空供氣 及平移 使各通 ;可利 排出至 洗篩網 設置匯 槽底部 濕之用 轉軸兼 入臥式 管2轉 推進, 氣管3 用排氣 匣式貯 ,以減 集過量 之本設 ’以加The air pipe reacts in a hollow state, and the blower airflow force tank reduces the remaining water. The fast-growing 3 sets the air supply pipe 2 in the tank 1 so that the multiple machines 2 2 can supply and the paddle board 1 17 can be blocked. Facilitate the drainage pipe to retain and minimize the reaction. Drive the stirring gas in each of the stirring hollows until the material is fully transferred, so that the 18-flow and remaining water can be used for stirring; the actuator 2 4 purple plate 2 6 axis and hollow enough oxygen fine particles are driven by the gradient It can be used as a self-driven rotation of the material, and the material supply pipe can be produced from the overflow material. The material particles are horizontally reversed, and are slightly dry. Granules, brushing tank 1 higher than the biomass moisturizing part and the 12 air supply and translation to make each pass; can be drained to the washing screen to set the wet bottom of the sink tank and the horizontal tube 2 turns to advance The air pipe 3 is stored in an exhaust box type to reduce the excessive setting of the setting.
立體圖 置於種 攪拌槳 進程之 如此 攪拌槳時,可 請 如圖所 氣管3 該排渣 參閱第 ;如圖 轴兼中 板之正 速度, 可充分 板2 6 使所有 參閱第 不’該 之通氣 口 3 6 2圖, 所示, 空供氣 、逆轉 且該複 作水平 之間以 物料充 3圖, 通氣管 控制閥 口徑小 為本發明 複數個授; 管2上, 次數,進 數個攪拌 方向之物 一定距離 分受到樓 為本發明 3内有一 ;通氣管 於該活動 貫施例於攪動槳板 拌槳板2 可利用該 行推料、 槳板2 6 料交流均 重疊設置 拌。 之實施例 活動球體 3末端有 球體3 2 6以一斜面 具有一斜面 退料運作, 以錯位之方 勻混合;而 ,如此在攪 之通氣管剖 3 2 ’其作 一排湩口 3 之直徑,當 裝置之 角度裝 角度之 以操作 式排列 兩相鄰 拌物料 面圖; 為該通 6,且 活動球When the three-dimensional view is placed on such a stirring blade process, please refer to the air pipe 3 for the slag discharge as shown in the figure; as shown in the shaft and the positive speed of the middle plate, you can fully plate 2 6 to make all the reference The figure of port 3 6 2 shows that the air supply and reversal are reversed and the material is filled between the three levels. The small diameter of the snorkel control valve is a multiple of the invention; The objects in the direction are separated by a certain distance from the building, which is included in the present invention 3; the ventilation tube is used in this embodiment to stir the paddle board and the paddle board 2 can use the row of pushing material, the paddle board 2 6 materials exchange are overlapped and mixed. Example: There is a sphere 3 2 6 at the end of the movable sphere 3. It operates with an oblique mask and an oblique surface, and mixes it in a dislocated way; When the device is installed at the angle of the device, two adjacent materials are arranged in an operational manner.
485056 五、發明說明(4)485056 V. Description of the invention (4)
體3 2向末端位移時,可推擠管内之細微顆粒自排渣口 3 6排出;該通氣管3與轉軸兼中空供氣管2處有一進氣口 3 8 ,且該進氣口 3 8 口徑亦小於該活動球體3 2之直徑 ,轉軸兼中空供氣管2可自此進氣口 3 8供氣至通氣管3 内;又在該通氣管3内距離末端大於該活動球體3 2直徑 距離處之兩端各設一出氣口 3 4,其可在物料底層通氣用 ;通氣管3之斷面積隨其徑向長度增加而增加,其可使活 動球體3 2在移動至末端時,通氣量亦可增加,如此可使 該通氣量與物料深度走向相近;又該通氣管3之内側兩端 為錐形縮口 ,如此可導引該活動球體3 2在位移初期沿管 壁轉向,消弭自由落體之.噪音問題。When the body 32 is displaced toward the end, the fine particles in the pipe can be pushed out of the slag discharge port 36; the air pipe 3 and the rotating shaft and the hollow air supply pipe 2 have an air inlet 3 8, and the air inlet 3 8 caliber Also smaller than the diameter of the movable sphere 32, the rotating shaft and hollow air supply pipe 2 can supply air from the air inlet 3 8 into the ventilation pipe 3; and the distance from the end of the ventilation pipe 3 is greater than the diameter of the movable sphere 32 An air outlet 34 is provided at each of the two ends, which can be used for ventilation at the bottom of the material; the cross-sectional area of the ventilation pipe 3 increases as its radial length increases, which allows the movable sphere 3 2 to move to the end, and the ventilation volume is also increased. It can be increased so that the ventilation volume is close to the depth of the material; and the two ends of the inner side of the ventilation tube 3 are tapered and constricted, so that the movable sphere 32 can be guided to turn along the tube wall at the beginning of the displacement to eliminate free fall. Noise problem.
請參閱第4圖,為本發明之實施例之通氣管通氣控制 示意圖;如圖所示,該活動球體3 2為該通氣管3之通氣 控制閥;當通氣管3在A處時,通氣管3直立於上方,活 動球體3 2因重力下落停在進氣口 3 8處以封住進氣口 3 8 ,此時氣體無法進入通氣管3内,使出氣口 3 4排氣量 為零;當通氣管3在於B處時,活動球體3 2因i皮度(角 度)改變,使其重力分力減少,使該球體在進氣口 3 8處 有鬆化之現象;當通氣管3在於C處時,通氣管3位於水 平位置,活動球體3 2便僅受氣體推力作用,故有部分空 間可通氣;當通氣管3在於D處時,活動球體3 2因重力 作用增加及氣體推力加速向下方滾動,使出氣口 3 4通氣 量略有增加;當通氣管3在於E處時,活動球體3 2快速 通過該通氣管3之出氣口 3 4處而停留於底部,此時進氣Please refer to FIG. 4, which is a schematic diagram of ventilation control of an embodiment of the present invention; as shown in the figure, the movable sphere 32 is a ventilation control valve of the ventilation pipe 3; when the ventilation pipe 3 is at A, the ventilation pipe 3 stands upright, and the movable sphere 3 2 stops at the air inlet 38 due to gravity drop to seal the air inlet 38. At this time, the gas cannot enter the vent pipe 3, so that the exhaust volume of the air outlet 3 4 is zero; when When the snorkel 3 is located at B, the movable sphere 32 is changed by the i-degree (angle), so that the gravity component force is reduced, so that the sphere is loosened at the air inlet 38; when the snorkel 3 is at C When the ventilation tube 3 is in a horizontal position, the movable sphere 32 is only affected by the gas thrust, so there is some space for ventilation; when the ventilation tube 3 is at D, the movable sphere 32 is increased due to the effect of gravity and the gas thrust accelerates. Scroll down to slightly increase the ventilation of outlet 3; When the vent 3 is at E, the moving sphere 32 quickly passes through the outlet 3 of the vent 3 and stays at the bottom.
第8頁 485056 五、發明說明(5) 口 3 8與出 氣管3在於 故活動球體 當通氣管3 ,活動球體 管3在於Η 斷面減少, 故本發 能力劇增; 反應最適宜 大幅減少設 能,無須增 ,無效通氣 程’滿足長 小型化;該 隨時投入, 水,不致對 ,反應槽中 ,高效率, 可製作,無 綜上所 ^攪拌法及 ,具有一斜 $物料在反 氣口 3 4之 F處時,重 3 2仍處於 在於G處時 3 2重力消 處時,活動 最後該球體 明可依生化 流程中各區 之環境條件 備裝置;又 設機械及操 損失減少, 時間生化反 連續流程, 不必待機產 後續流程造 物料不致過 占用空間少 須特殊專業 述,本發明 其構造’將 面角度之攪 應槽内作水 間無阻礙物 力作用漸減 端座,亦即 ,通氣管3 失,通氣量 球體3 2由 便會又回至 反應階段構 段,可以獨 ;且在單槽 可以攪拌回 作;直接顆 節省通氣動 應需要,而 不受批次反 生腐敗發臭 成妨害或厭 量影響反應 ,且構造簡 〇 係有關於一 物料自進料 拌槳板不僅 平移動,複 ,通氣量為 ,但重力與 氣體仍以最 在2 7 0度 尚接近最大 末端向中心 進氣口 3 8 成流程微生 立控制操作 内構成流程 轉運作供給 粒層中通氣 力;且可使 使流程長度 應投料限制 ;又以自然 氧化;且溢 ;而本設備 單一般習知 種固體物料 口投入該臥 可攪拌該物 數個通氣管 最大;當通 氣力同向, 大量供氣; 之水平位置 值;當通氣 下滾,通氣 停止。 物增殖分解 ’提供生化 區段作用, 大量附加功 ’效果提升 微量物料進 縮短,設備 ’廢棄物可 重力排除餘 料自動排出 集約小型化 工程技術即 认槽進程通 式反應槽内 料且可推進 可提供充分Page 8 485056 V. Description of the invention (5) Mouth 3 8 and air outlet tube 3 are the movable spheres used as the ventilation tube 3, and the movable sphere tube 3 is located in the Η section, so the capacity of the hair increases sharply; Yes, no need to increase, ineffective aeration path to meet long miniaturization; the time to invest, water, no misalignment, in the reaction tank, high efficiency, can be made, no summary ^ stirring method, and has a diagonal $ material in the anti-air port At 3 of F, the weight of 3 2 is still at G, and at the time of 3 2 gravity elimination, at the end of the activity, the sphere can be prepared according to the environmental conditions of each area in the biochemical process; mechanical and operating losses are reduced, and time is reduced. The biochemical anti-continuous process does not need to wait for the production of subsequent processes to create materials that do not take up too much space. It requires special expertise. The structure of the invention is to use the surface angle mixing tank as the end seat without obstructing the physical force between the water. The trachea 3 is lost, and the ventilation sphere 3 2 will return to the reaction stage. It can stand alone; and it can be stirred in a single tank. The direct pellet saves the ventilation and needs, without being affected by the batch. Stinking and stinking become nuisance or annoying to affect the response, and the structure is simple. It is related to a material self-feeding. The paddle board not only moves flat, complex, and has a ventilation volume, but gravity and gas are still at a maximum of 270 degrees. Close to the maximum end to the central air inlet 3 8 into the flow micro-control control operation constitutes the flow conversion operation to supply ventilation in the granular layer; and can make the length of the process should be limited to the feed; natural oxidation; and overflow; and this equipment A single conventionally known type of solid material can be placed into the bed to agitate the material. Several ventilation pipes are the largest; when the ventilation force is in the same direction, a large amount of air is supplied; the horizontal position value; when the ventilation is rolled down, the ventilation stops. Bio-propagation and decomposition 'provides the role of biochemical section, a large amount of additional work' effect improves the trace material input and shortens, and the equipment 'waste can be gravity-excluded and the remaining material is automatically discharged. Can provide
第9頁 485056 五、發明說明(6) 氧氣至物料中,使物料能行生化反應。故本發明實為一富 有新穎性、進步性、及可供產業利用性者,應符合專利申 請要件無疑,爰依法提出發明專利申請,祈鈞局早曰賜准 專利,至為感禱。 惟以上所述者,僅為本發明之一較佳實例而已,並非 用來限定本發明實施之範圍。故即凡依本發明申請專利範 圍所述之形狀、構造、特徵及精神所謂之均等變化與修飾 ,均應包括於本發明之申請專利範圍之内。 圖號簡單說明: 1臥式反應槽 1 1低位支撐座 1 2進料口 1 3高位支撐座 1 4排料口 1 5排氣裝置 1 6溢料口 1 7 E式貯料槽 1 8排水管 2轉轴兼中空供氣管 2 2鼓風機 2 4攪拌驅動器 2 6攪拌槳板 3通氣管 3 2活動球體Page 9 485056 V. Description of the invention (6) Oxygen is added to the material so that the material can perform biochemical reactions. Therefore, the present invention is truly novel, progressive, and available for industrial use. It should meet the patent application requirements. It is no doubt that the invention patent application is submitted in accordance with the law. However, the above is only a preferred example of the present invention and is not intended to limit the scope of implementation of the present invention. Therefore, all the so-called equal changes and modifications in the shape, structure, characteristics, and spirit described in the scope of patent application of the present invention shall be included in the scope of patent application of the present invention. Brief description of drawing numbers: 1 horizontal reaction tank 1 1 low support 1 2 feed inlet 1 3 high support 1 1 discharge port 1 5 exhaust device 1 6 overflow port 1 7 E-type storage tank 1 8 drainage Tube 2 shaft and hollow air supply tube 2 2 Blower 2 4 Stirring driver 2 6 Stirring paddle 3 Ventilation tube 3 2 Moving sphere
485056 五、發明說明(7) 3 4出氣口 3 6排渣口 3 8進氣口485056 V. Description of the invention (7) 3 4 air outlet 3 6 slag outlet 3 8 air inlet
(ill 第11頁 485056 圖式簡單說明 第1圖:為本發明一較佳實施例之侧視圖; 第2圖:為本發明之實施例於攪動槳板裝置之立體圖; 第3圖:為本發明之實施例之通氣管剖面圖;及 第4圖:為本發明之實施例之通氣管通氣控制示意圖。(ill Page 11 485056 Brief description of the drawings Figure 1: This is a side view of a preferred embodiment of the present invention; Figure 2: This is a perspective view of an agitating paddle device according to an embodiment of the present invention; Figure 3: This is a A cross-sectional view of a ventilation tube according to an embodiment of the invention; and FIG. 4 is a schematic diagram of ventilation control of a ventilation tube according to an embodiment of the invention.
第12頁Page 12
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TW89121412A TW485056B (en) | 2000-10-13 | 2000-10-13 | Venting and stirring methods in feeding solid material to horizontal tank and its structure |
TW89121412A01 TW568796B (en) | 2000-10-13 | 2001-02-09 | Inlet ventilation mixing device for solid material storage tank |
JP2001104033A JP2002205038A (en) | 2000-10-13 | 2001-04-03 | Horizontal stirring and preparation tank for treating organic waste and method for stirring and preparing organic waste utilizing horizontal stirring and preparation tank |
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TW89121412A TW485056B (en) | 2000-10-13 | 2000-10-13 | Venting and stirring methods in feeding solid material to horizontal tank and its structure |
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TW89121412A TW485056B (en) | 2000-10-13 | 2000-10-13 | Venting and stirring methods in feeding solid material to horizontal tank and its structure |
TW89121412A01 TW568796B (en) | 2000-10-13 | 2001-02-09 | Inlet ventilation mixing device for solid material storage tank |
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TW89121412A01 TW568796B (en) | 2000-10-13 | 2001-02-09 | Inlet ventilation mixing device for solid material storage tank |
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