201116332 六、發明說明： 【發明所屬之技術領域】 本發明尤指其提供—種可省時、U自 Ϊ的備操作安全性及降低設備能源“ 批次式進料之熱化學處理設備。 按，近幾年來，生質燃料乃為國内、外201116332 VI. Description of the invention: [Technical field to which the invention pertains] The present invention particularly provides a thermochemical processing device that can save time and U self-provisioning operation safety and reduce equipment energy. In recent years, biofuels are domestic and foreign.
^丈=生質技ί除了可以降低對石油能二依賴與減緩 放應外’以農業、畜牧業、1業廢棄物等（如枝葉、糞便、 原料來源時’還能達到廢棄物處理與環 生質燃料技術主要係將有機原料在高 ί學反應，於完成熱化學反應後，再以後 、’ P可獲致所需的生質燃料或前處理原料；目前敎 續ΐΪί ^，術的處理設備以進料方式來區分，係可分“ 式進料，以下就其設備及缺弊加以說明如下： 參閱第1圖’其係為美國第7,473, 285號專 ，^係於s路1〇的—端裝設—可供原料送人之入料口 ◦上另設有第—輸送裝置1 2，而可將原料以 壓力槽13及第二壓力槽14，接著管 0的第一輸送裝置15再將原料送入反應區i 6加敎 熱化學反應’完成熱化學反應後，再將反應後之混 ί1 =至t凝裝置17進行冷凝回收’最後再送至分離裝 離’以萃取出生質燃料，·該連續式進料的設備 雖I非常便於原料的裝填料作#，但其仍有如下之缺弊： .，:史個反應區1 6與冷凝裝置1 7及分離裝置1 8間並 ^置遮斷閥件，使得反應區16進行加熱反應時，熱氣 文專送至冷凝裝置^ 7，而必須同時啟動冷凝裝置丄了及 t離裝置1 8 ’峨動冷凝裝置1 7及分離裝置1 8的同 時’反應111 6糊觀狀S，導致反應區1 6不易達到 反應之臨界勤，而增加操作上的困難度。^丈=生生技术ί, in addition to reducing the dependence on oil energy and slowing down the release of 'in agriculture, animal husbandry, 1 industry waste, etc. (such as foliage, manure, raw materials source) can also achieve waste disposal and environmental The quality fuel technology mainly involves the organic raw materials in the high-reaction reaction. After the completion of the thermochemical reaction, the P can obtain the required raw fuel or pre-treatment raw materials. Currently, the processing equipment is According to the feeding method, the system can be divided into “feeding materials”. The following is the description of the equipment and the shortcomings: See Figure 1 for the US Department No. 7, 473, 285, and ^ for the s road 1—. The end device is provided with a first conveying device 12 for feeding the raw material, and the raw material is used for the pressure tank 13 and the second pressure tank 14, and then the first conveying device 15 of the tube 0 The raw material is sent to the reaction zone i 6 and the thermochemical reaction is completed. After the thermochemical reaction is completed, the reaction is further mixed to the t-condensing device 17 for condensation recovery and finally sent to the separation and removal to extract the raw material fuel. ·The continuous feeding equipment is very convenient for raw materials Filling with #, but it still has the following disadvantages: .,: between the reaction zone 16 and the condensing device 17 and the separating device 18, and the valve member is placed, so that the reaction zone 16 is heated. The hot gas is sent to the condensing unit ^7, and the condensing unit must be activated at the same time and the unit 1 8 'the condensing unit 17 and the separating unit 18 are simultaneously reacted. Zone 16 is not easy to reach the critical duty of the reaction, and increases the difficulty of operation.
ί SI 3 201116332 Β·Γ=反應^完成反應後之混合物含有固體、液體 及虱體成伤，混合物由反應區丄6輸 ，因固體流動能力較差，在長期操作下，容易: 2 輸达%*路或輸送裝置，而無法長期穩定的使用。 ΐίϊΠϋΐ第2、3圖’其係為台灣第13_〇4號 ‘2 1二⑵力槽體2 1及封蓋2 2，槽體 以對槽體21内部加熱，封 =;;;==驅動之細2 5，蝴 行攪拌，而二i :封12 2传體Y内之原料進 4+ U係乂展列之螺栓2 6鎖固密 =槽體21内進行有機原料的熱化學反應，於完 ΐίΐ'ί ’可_體2 1與封蓋2 2分離，再將槽體2 1 ί 之反應物取出，於重新裝填有機原料後，即可以批次 ism學反應;該批次式進料的設備其雖可避免如i 、，式進枓之輸送管路阻塞的問題，但其 Α· 體2 1與封蓋2 2係以環列之螺固密 ==栓26，議 應槽20的產業放大運用與自動化。 、 Β.由於加熱器2 3裝設於槽體2 1外部，使得卿？ η與封蓋接 導致後封環墊的毁損’而降低其使用壽命。 谷易 c. j設^欠缺冷凝裝置，使得反應完成後，反 高壓的狀態’然為了提高生質燃料:“2 間自然冷卻降溫，使反應槽2工内=質料時 D ίίϊΪ蓋2 2取出生成物，導致製程時間過長4才可 D.於反應槽2㈣取tB反應物並重聽填原 批次的熱化學反應時，由於反應槽2 〇已經自然冷 201116332 重新加熱到反應溫度，且因反應槽2 〇為耐高溫、高壓之 反應槽2 0需為厚奴夠的金屬結構才能達到強度 應f2 0之4量相當重’相對的導致反應槽 2 0反覆重新加熱所需熱能與成本相對提高。 經驗有關行業的研發與製作 研創出—種不僅可省時、省力、自動化的快速進行批 二有！’且可縮短製程時間、降低設備能源耗損，達 ^ ί ί 賴招枝全性之熱化學處财備，並藉 ^大幅改善習式之缺弊’此即為本發明之設計宗旨。 【發明内容】 直户ίϊΓί，—係提供—種批次式進料之熱化學處理設備， si 以—封蓋蓋合，並於封蓋與處理槽間設有密封 ίϊ ’ ίΐΞΐ理槽之槽口，再以—封蓋緊閉裝置鎖合處理槽及 ίί二：Ϊ的將處理槽與封蓋密封固定，即可對處理槽内之 化學反應’完成熱化學反應後，啟動封蓋緊閉裝 ϋΐ槽與封蓋分離’以進行下-批次的入、出料作業，進而 _ 本發明之目的二係提供一種批次式進料埶 係延伸峰陶附連結冷卻裝置放又J上 理槽進行熱化學反應時，可闕閉啟關，而於 二則開啟啟閉闕，使高虔高溫反應生成之高溫 Γ ίϊίίΓ裝置，赠處賴觀並精生錄的冷凝回 長時間自然冷卻降溫及釋壓，以縮短製程時間， 達到有效如升設備產能及設備操作安全性之目的。 的二係提供一種批次式進料之熱化學處理設備， =理槽^⑧溫反應生紅高溫赫槪 得處理槽翻超行生齡凝时卩使 即可啟動封蓋緊閉裝置，以進行下一批次的“學 201116332 ίί，=理槽並未自然冷卻降到低溫，而係仍處於較高溫的 =，因此如下-批次的熱化學反應時，不需由低溫重新開始 加…到反應溫度，進而達到有效降低設備能源耗損之目的。 本發明之目的四係提供一種批次式進料之熱化學處理 其處理槽内係設有加熱裴置，該加熱裝置包含一環座，^ ，周側設加熱H，使得承裝鑛之容II架置於環座後，可由二 器直接對該容器加熱，以進行熱化學反應，由; 環座周側’而不會將大量的熱能傳導至處理槽之槽壁 封環墊的使用壽命，且可提高對容器的熱 傳效果’進而有效降低設備能源耗損之目的。 【實施方式】 為使貝審查委員對本發明作更進一步之瞭解，兹舉 實施例並配合圖式，詳述如后： f 請參閱第4、5圖，本發明之熱化學處理設備，盆 ^糸於槽π處向外延伸設有凸緣3 Q丄，於槽_設有加I 置，該加熱裝置包含一上方具有較大開口之圓錐狀環座 ^ ’ 並於該圓錐狀環座3 0 3周側裝設有加熱器3 0 4，該圓錐狀環 f3 0 3係設置於處理槽3 Q内部之腳座3◦2，於本實施^ 工座3^ 2係設於處理槽3 〇底部，在其他應用上，該腳 於3 〇 3 ’並透過腳座3 ◦ 2的區隔，可使^加熱器3 0 4、 加熱於處理槽3 ◦之槽壁上，以避免大量的熱能傳導至 J理槽3 0 ’而降低設備能源的耗損，較佳地座3 = 類係r、糞便、有機污泥、 乂 係可吊达裝置（如天車〕吊送並架置於處理槽3 〇之 3内，並使容器3 i緊密貼合树座3 ^内== ’進而加熱& 3 〇 4可對容11 3 1内之原料加執。於本 實施例中，該環座3 Q 3無容器3丨均呈圓缝，但^發^ [S] 6 201116332 應用並不以此為限，該環座 或其他能相互對應之形狀。〇 U ^與該容器31亦可為圓筒狀， 清參閱第6、7、8圖太杳 一輸送裝置上，該輸送裝置^實_施例之處理槽3 0係可架置於 動，而於滑軌3 2上平移〜之載可由平移驅動機構3 3 1驅 動機構3 3 2驅動而作升降你二，且該載台3 3可由升降驅 後’即可由輸送襄置帶動移入至作架置於載台3 3上 定架設於機架3 4上之封甚q =蒹區或移出至交換料區；一固 並於下方設有可套合於處理槽π^環側延伸設有卡緣3 51， 柱3 5 2之外環面套設有‘ ^ $套柱3 5 2，其中該套 3 3以升降驅動機構3 3 2 3，而於輸送裝置之载台 時，密封環塾3 5 3可==，〇與封蓋35蓋合 架設一可由動力機構3 7_之封蓋3 5上 封蓋3 5穿伸至處理槽3 0内，而拌棒3 6係於 的擾掉，以促進容器3 1内原料1内f原料作均勻 4上之封蓋緊職置，其係包含’―架設於機架3 等夾套係為弧形之夾套3 8 =巧夾套，於本實施例中，該 設有内凹環槽3 8 1、3 9 1，以對應^ 9於内側分別 及封蓋3 5之卡緣3 5 1，另夾套3 之凸緣3 0 1 機構4 0、4 !驅動由外側向⑵8而上==J驅動 30與封蓋35蓋合後，再以夾套38 置頂升處理槽 3 9 〇3^Ti8i3 封蓋35鎖合密封 反應，由於加熱器3 0 4：係對環i 3 ^熱進订熱化學 3 0 2的區隔，可避免=的iiH3 f妾加熱，並透過腳座 理槽3 ◦接觸之密二得= 蓋r之套柱3 5 處= 签1卩高壓使得處理槽3 0*封 盍3 5間產生極微小的滑移，密封環塾3 5 3仍可使處理槽3、圭〇 7 S] 201116332 與封蓋3 5間保持在封閉的狀態，而不會因該極微小的滑移產生 外j的情形；為使處理槽3 0内快速達到高壓狀態，封蓋3 5上 裝β又有由處理槽3〇延伸於外部之導入管42，而可由該導入管 41輸入如硫酸、氫氣、一氧化碳、氮氣之流體，並提供作為熱 化學反，之添加劑使用；另封蓋3 5上裝設有連通至處理槽3〇、 =放管4 3 ’該排放管4 3上設有啟關4 3 1 ’並連結至冷 24 :於處理槽3 〇進行熱化學反應時，可自動關閉啟閉 11，以保持處理槽3 0内高壓高溫的狀態，於完成熱化學 μ二時、’，開啟啟閉閥4 3 1，使高壓高溫反應生成之高溫流體 排，至冷卻駭4 4 ’不僅可使處理槽3⑽壓，且可對生成物 凝回而不需耗費長時間自然冷卻降溫及釋壓，以縮短 日、間，元成生成物的冷凝回收後，由於處理槽3 〇已經釋壓， 封蓋緊閉裝置’使聽38、39脫離壓爽處理槽3〇 盍3 5，再由輸送裝置將處理槽3 〇移出至交換料區，以進 ^人谷态3 1的交換料’進而不需費力、費時的拆裝螺栓， 由於處力的ί速進行交換料作業；完成交換料後， 鲅，^=3 〇並未自然冷卻降到低溫，而仍處於較高溫的狀 的熱化學反應時，不需由低溫重新開始加 ”、、心，恤度，進而達到有效降低設備能源耗損之目的。 架置iQ圖’本發明另—實施例之處_5 〇係可 1驅動，該輸送裝置包含—可由平移驅動機構5 3 二R 3 μa ^月軌5 2上平移之載台5 3，處理槽5 0架置於載 i ; -樞送裝置帶動移入至作#區或移出至交換料 5，德機5 4上之擺臂541，其前端部係連結封蓋5 作動時;mg，，，構5 4 2，於頂升驅動機構5 4 2 部之封蓋1在機架上5 4上樞轉，進而帶動前端 環側係延伸處理槽5 ◦之槽° ’其中’封蓋5 5之 5 2，而5 1，並於下方設有密封環塾5 a. - ^ 』闲蛟埋槽bϋ之槽口，另封盍緊閉震置， 201116332 中，該環Ϊ J口，環套5 6，於本實施例 套5 6之内環面上方設有複槽5 Q槽口外側，環 5 7、5J之凸耳5 C ?面兩側分別設有連結旋轉驅動機構 8作動時可帶動環套5 6轉:6】使機構5 7、5 封蓋之外凸齒5 5 !錯位或J疊，凸齒5 6 1與 1係位於封蓋之外凸齒5 5由於絲5 6之内凸齒5 6 凸齒5 6 i與封蓋卜2=位置，因此在環套5 6之内 之内凸齒5 6 齒1利用環套5 6 密封 後，由於處理槽5 0已_„)，虽兀成生成物的冷凝回收 驅動機構5 7、ΐίΐΐ，蓋緊閉裝置，由旋轉 ，套5 6之内凸齒5 61即脫離壓夾 Hi輸送裝置將處理槽5 ◦移出至交換料區，以進行 料’ _的不需f力、f時的職螺栓，達到省 時嚙力且自動化的快速進行交換料作業。 轉本僅可省時、省力自動化的快速進行批次化的 可提高設備操作安全性及降低設備能源的耗損， 妙去目w间稍使料’實為—深具實祕及進步性之設計， ΐ依法ί=ί產品及刊物公開，從而允符發明專利中請要件， 【圖式簡單說明】 第1圖.係為美國第7, 473, 285號專利案之示意圖。 第2圖，係為台灣第I 30_4號專利案之外觀示意圖。 第3圖：係為台灣第I 3GG8G4號專利案之剖面示意圖。 第4圖：本發明處理槽之剖面示意圖。 第5圖：本發明處理槽架置容器之剖面示意圖。 201116332 第6圖：本發明之架構示意圖。 第8圖 第9圖 第7圖：本發明處理槽與封蓋蓋合之外觀示意圖。 本發明處理槽與封蓋蓋合之剖面示意圖。 本發明另一實施例之架構示意圖。 。:本發明另—實施例之處理槽與封蓋蓋合之剖面示意圖 【主要兀件符號說明】 習式部份：SI SI 3 201116332 Β·Γ=Reaction^ After the completion of the reaction, the mixture contains solids, liquids and carcasses. The mixture is transported from the reaction zone ,6. Due to the poor solid flow ability, it is easy to operate under long-term operation: 2 % of transmission * Road or conveyor, not long-term stable use. ΐίϊΠϋΐ第2, 3'' is the 13th_〇4 '2 1 2 (2) force trough body 2 1 and the cover 2 2 in Taiwan, and the trough body heats the inside of the trough body 21, sealing =;;;== Drive the fine 2 5, the butterfly is stirred, and the second i: seal 12 2 the material in the body Y into the 4 + U system to expand the bolts 2 6 lock solid density = the thermochemical reaction of the organic material in the tank 21 , after finishing ΐ ΐ ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί Although the feeding equipment can avoid the problem of blockage of the conveying pipeline such as i, and the type of the inlet, the body 2 1 and the cover 2 2 are fixed by the ring of the screw == bolt 26, The industry of scale 20 is used for automation and automation. Β. Since the heater 2 3 is installed outside the tank 2 1 , so that? The connection of η to the cover results in damage to the back seal ring and reduces its useful life. Gu Yi c. j set ^ lack of condensing device, so that after the reaction is completed, the state of anti-high pressure 'in order to improve the biomass fuel: "2 natural cooling and cooling, so that the reaction tank 2 inside = material when D ίίϊΪ cover 2 2 The product is produced, and the process time is too long to be 4. D. When the tB reactant is taken in the reaction tank 2 (4) and the thermochemical reaction of the original batch is re-listen, the reaction tank 2 〇 has been naturally cooled to 201116332 and reheated to the reaction temperature, and The reaction tank 2 is a high-temperature resistant and high-pressure reaction tank. The metal structure required for thick slaves can reach the strength. The amount of f2 0 is quite heavy. The relative heat energy required to reheat the reaction tank 20 is opposite to the cost. Improve the experience of the industry's R & D and production research and development - not only save time, effort, automation and rapid implementation of the second! 'And can shorten the process time, reduce equipment energy consumption, up to ^ ί ί 招 全 全 全The hot chemistry department prepares and uses the ^ to greatly improve the shortcomings of the formula'. This is the design tenet of the invention. [Summary of the invention] 直ϊΓ ,, 提供 provides a batch of hot chemical processing equipment for feeding,Si is covered by a cover, and a seal is provided between the cover and the treatment tank, and the groove of the sealing groove is closed, and the sealing device is closed with the sealing device and the processing groove is The seal is sealed and fixed, and the chemical reaction in the treatment tank can be completed. After the thermochemical reaction is completed, the closure is closed and the sealing tank is separated from the cover to perform the lower-batch inflow and discharge operations, and further _ this The second object of the invention is to provide a batch type feeding system, a truss extension peak, a ceramic attachment cooling device, and a J-top tank for a thermochemical reaction, which can be closed and closed, and the second opening and closing 阙, high Γ High temperature reaction generated by high temperature reaction ϊ ϊ Γ Γ 并 并 并 并 并 并 并 并 并 并 并 并 并 并 并 并 并 并 并 并 精 精 精 精 精 精 精 精 精 精 精 精 精 精 精 精 精 精 精 精 精 精 精 精 精 精 精 精 精The second series provides a batch-type feed thermal chemical treatment equipment, = the control tank ^ 8 temperature reaction, the red high temperature, the high-temperature treatment, the treatment tank, the super-life, the condensate, the lid closure device can be activated to carry out the closure device The next batch of "learning 201116332 ίί, = The tank is not naturally cooled down to a low temperature, and the system is still at a higher temperature =, so the following - batch thermochemical reaction, no need to restart from the low temperature ... to the reaction temperature, thereby achieving the purpose of effectively reducing equipment energy consumption . The purpose of the present invention is to provide a thermochemical treatment of batch feed, wherein the treatment tank is provided with a heating device, the heating device comprises a ring seat, and the circumference side is provided with heating H, so that the capacity of the ore is II. After the rack is placed on the ring seat, the container can be directly heated by the two devices to perform a thermochemical reaction, and the life of the groove wall gasket of the groove of the treatment tank is not transmitted to the circumference of the ring seat. Moreover, the heat transfer effect on the container can be improved, thereby effectively reducing the energy consumption of the device. [Embodiment] In order to make the present invention further understand the present invention, the embodiments and the drawings are described in detail as follows: f Please refer to Figures 4 and 5 for the thermochemical treatment equipment of the present invention. The flange 3 is disposed outwardly from the slot π, and the slot is provided with an I. The heating device includes a conical ring seat having a larger opening above and a conical ring seat 3 0 3 weeks side is equipped with a heater 306, which is provided in the inside of the processing tank 3Q, 3'2, and is disposed in the processing tank 3 in the present embodiment. At the bottom of the crucible, in other applications, the foot is separated by 3 〇 3 ' and through the foot 3 ◦ 2, so that the heater 3 0 4 can be heated on the groove wall of the treatment tank 3 to avoid a large amount of The heat energy is transmitted to the J tank 30' to reduce the energy consumption of the equipment. Preferably, the seat 3 = the type r, the feces, the organic sludge, the slingable lifting device (such as the crane) is hoisted and placed in the treatment. The inside of the tank 3 is 3, and the container 3 i is closely attached to the tree seat 3 ^ == ' and then the heating & 3 〇 4 can be added to the raw material in the capacity 11 31. In this embodiment The ring seat 3 Q 3 has no container 3 丨 all rounded, but ^ ^ ^ [S] 6 201116332 application is not limited to this, the ring seat or other shapes that can correspond to each other. 〇U ^ and the container 31 can also be cylindrical, as shown in Figures 6, 7, and 8 of the Tweezing-Conveying Device, the processing device can be placed in motion, and the sliding rail 3 2 The upper translational load can be driven by the translation drive mechanism 3 3 1 drive mechanism 3 3 2 to lift and lower the second, and the stage 3 3 can be moved by the transport device to be placed on the stage 3 3 is fixed on the frame 3 4, the seal is even q = 蒹 area or removed to the exchange material area; a solid is placed under the sleeve π ^ ring side extension with a card edge 3 51, column 3 5 2 The outer toroidal sleeve is provided with a ' ^ $ sleeve 3 5 2 , wherein the sleeve 3 3 is a lifting drive mechanism 3 3 2 3 , and when the carrier of the conveying device is mounted, the sealing ring 塾 3 5 3 can be = =, the 〇 and the cover 35 are erected and erected, and the cover 3 5 of the power mechanism 3 7_ can be inserted into the processing tank 30, and the mixing rod 36 is disturbed to promote the container. 3 1 raw material 1 inside f raw material for uniform 4 The cover is tightly closed, and the system includes a sleeve that is mounted on the frame 3 and has a curved sleeve. The sleeve is a sleeve. In this embodiment, the recessed groove 3 8 1 is provided. , 3 9 1, corresponding to ^ 9 on the inside and the cover 3 5 of the card edge 3 5 1, the other sleeve 3 of the flange 3 0 1 mechanism 4 0, 4 ! drive from the outside to (2) 8 up == J After the drive 30 and the cover 35 are closed, the cover 38 is placed in the top of the processing tank 3 9 〇 3 ^ Ti8i 3 cover 35 locks the sealing reaction, because the heater 3 0 4: is hot to the ring i 3 ^ The interval of chemical 3 0 2 can avoid the heating of iiH3 f妾, and it can be contacted through the foot socket 3 ◦ contact the second set = the cover of the cover r 3 5 = 1 high pressure makes the treatment tank 3 0* The sealing ring 3-5 has a very slight slip, and the sealing ring 塾3 5 3 can still keep the processing tank 3, the 〇7 7] 201116332 and the cover 3-5 in a closed state, without being extremely small. The sliding occurs to generate the outer j; in order to quickly reach the high pressure state in the processing tank 30, the cover 35 has a beta tube and an introduction tube 42 extending from the processing tank 3〇 to the outside, and can be input by the introduction tube 41. Such as sulfuric acid, hydrogen, carbon monoxide, nitrogen The fluid is supplied as an additive for the thermochemical reaction; the other cover 35 is provided with a communication to the treatment tank 3〇, = the discharge tube 4 3 'the discharge tube 4 3 is provided with the opening and closing 4 3 1 'and Linked to cold 24: When the thermochemical reaction is carried out in the treatment tank 3, the opening and closing 11 can be automatically closed to maintain the state of high pressure and high temperature in the treatment tank 30, and when the thermochemical μ is completed, ', the opening and closing valve is opened 4 3 1, the high-temperature fluid generated by the high-pressure high-temperature reaction, until the cooling 骇 4 4 ' can not only press the treatment tank 3 (10), and can condense the product without taking a long time to naturally cool down and release pressure, to shorten the day After the condensate recovery of the product, the sealing tank 3 〇 has been released, and the cap closing device 'disconnects the 38, 39 from the pressurization treatment tank 3〇盍3 5, and then the treatment tank will process the tank 3 〇 Move out to the exchange material area to enter the exchange material of the person's valley state 3 1 and then eliminate the need for laborious and time-consuming disassembly and assembly of bolts, and exchange work due to the force of the force; after completing the exchange of materials, 鲅, ^ =3 〇 Thermochemical reaction that does not naturally cool down to a low temperature, but is still at a higher temperature When, by the cold restart without adding ",, heart, shirts degree, and then to reduce the energy consumption of the destination device. Mounting the iQ diagram 'In the other part of the invention' - the _5 〇 can be driven by 1 , the conveying device comprises - the stage 5 3 can be processed by the translational drive mechanism 5 3 2 R 3 μa ^ month rail 5 2 The slot 50 is placed on the carrier i; the pivoting device is driven to move into the # zone or to the exchange material 5, the swing arm 541 on the German machine 5 4, and the front end portion is connected to the cover 5 to operate; mg, , the cover 5 of the jacking drive mechanism 5 4 2 pivots on the frame 5 4 , thereby driving the front end ring side extension processing groove 5 ◦ groove ° 'where 'the cover 5 5 5 2, and 5 1, and a sealing ring 塾5 a. - ^ 』 蛟 蛟 蛟 蛟 蛟 蛟 蛟 a a a a a a 蛟 蛟 蛟 蛟 蛟 蛟 2011 2011 2011 2011 2011 2011 2011 2011 2011 2011 2011 2011 2011 2011 2011 2011 2011 2011 2011 2011 2011 2011 2011 5, in the embodiment of the sleeve 56, the outer ring surface is provided with a double groove on the outer side of the ring, and the outer side of the ring 5 C? face of the ring 5 7 and 5J is respectively provided with a connecting rotary drive mechanism 8 to be actuated. Drive the ring sleeve 5 6 turns: 6] make the mechanism 5 7, 5 cover the convex teeth 5 5 ! dislocation or J stack, the convex teeth 5 6 1 and 1 are located outside the cover convex teeth 5 5 due to the wire 5 6 The inner teeth 5 6 convex teeth 5 6 i and the cover cover 2 = position, so in the ring Within 5 6 the inner teeth 5 6 teeth 1 are sealed by the ring sleeve 56, and since the treatment tank 50 has been _„), the condensing recovery drive mechanism 5 7 , ΐίΐΐ, the lid closing device, By rotating, the inner teeth 5 61 of the sleeve 5 6 are removed from the press clamp Hi conveying device, and the processing tank 5 ◦ is removed to the exchange material area, so as to carry out the material bolts of the material ' _ without f force and f, saving time Fast and automated exchange of materials. The transfer can only save time and effort, and the rapid batching can improve the operation safety of the equipment and reduce the energy consumption of the equipment. For the design of the secret and progressive, 公开 ί=ί products and publications, so as to allow the invention patents, [simplified description] Figure 1 is the United States 7, 473, 285 A schematic diagram of the patent case. Fig. 2 is a schematic view of the appearance of the patent No. I 30_4 of Taiwan. Fig. 3 is a schematic cross-sectional view of the patent No. I 3GG8G4 of Taiwan. Fig. 4: section of the treatment tank of the present invention Fig. 5 is a schematic cross-sectional view of a processing tank mounting container of the present invention. 201116332 Fig. 6 is a schematic view of the structure of the present invention. Fig. 8 is a view showing the appearance of the processing tank and the cover. The cross section of the treatment tank and the cover is closed. Schematic diagram of an embodiment of the present invention: a cross-sectional view of a processing tank and a cover cover according to another embodiment of the present invention [main element symbol description]
10 13 16 20 2 3 2 6 管路 第一壓力槽 反應區 反應槽 加熱器 螺松 11:入料口 14:第二壓力槽 17:冷凝裝置 2 1 :槽體 2 4 :動力機構 12:第一輸送裝置 15:第二輸送裝置 18:分離裝置 2 2 :封蓋 2 5 :攪動桿 本發明部份： 3 0 :處理槽 3 0 3 :環座 3 1 :容器 3 2 :滑執 3 3 :載台 3 01 :凸緣 3 0 4 :加熱器 3 0 2 :腳座 3 31 :平移驅動機構 3 4 :機架10 13 16 20 2 3 2 6 Pipeline first pressure tank reaction zone reaction tank heater screw loose 11: inlet port 14: second pressure tank 17: condensing unit 2 1 : tank body 2 4: power mechanism 12: A conveying device 15: a second conveying device 18: a separating device 2 2: a cover 2 5: agitating rods Part of the invention: 3 0: treatment tank 3 0 3 : ring seat 3 1 : container 3 2 : slippery 3 3 : Stage 3 01 : Flange 3 0 4 : Heater 3 0 2 : Foot 3 31 : Translation drive mechanism 3 4 : Rack
3 5 :封蓋 3 5 3 .密封環塾 3 6 攪拌棒 3 8 夾套 3 9 夾套 40 推移驅動機構 42 導入管 44 冷卻裝置 5 0 處理槽 3 5 2 :套柱 3 3 2 :升降驅動機構 3 51 :卡緣 3 7 :動力機構 3 81 :内凹環槽 3 91 :内凹環槽 41:推移驅動機構 4 3 :排放管 4 31 :啟閉閥 [S 1 10 201116332 5 2 :滑軌 5 3 :載台 5 3 1 5 4 :機架 5 4 1 :擺臂 5 4 2 5 5 :封蓋 5 5 1 :外凸齒 5 5 2 5 6 :環套 5 6 1 :内凸齒 5 6 2 5 7 :旋轉驅動機構 5 :平移驅動機構 :頂升驅動機構 :密封環墊 :凸耳 5 6 3 :凸耳 3:旋轉驅動機構3 5 : Cover 3 5 3 . Sealing ring 塾 3 6 Stirring rod 3 8 Jacket 3 9 Jacket 40 Pushing drive mechanism 42 Inlet pipe 44 Cooling device 5 0 Treatment tank 3 5 2 : Set post 3 3 2 : Lift drive Mechanism 3 51 : Card edge 3 7 : Power mechanism 3 81 : Inner ring groove 3 91 : Inner ring groove 41: Shift drive mechanism 4 3 : Discharge pipe 4 31 : Opening and closing valve [S 1 10 201116332 5 2 : Slip Rail 5 3 : Stage 5 3 1 5 4 : Rack 5 4 1 : Swing arm 5 4 2 5 5 : Cover 5 5 1 : Outer tooth 5 5 2 5 6 : Ring sleeve 5 6 1 : Inner tooth 5 6 2 5 7 : Rotary drive mechanism 5 : Translation drive mechanism: jack-up drive mechanism: seal ring pad: lug 5 6 3 : lug 3: rotary drive mechanism