200920833 九、發明說明·· 【發明所屬之技術領域】 本發明係有關於一種子母同軸高溫旋轉反應爐，尤指 一種整合具有熱裂解、碳化、活化旋轉三種功能之高溫無 氧反應爐。 【先前技術】 習知處理粉狀/粒狀/柱狀/球狀之原料、活性碳或回收 廢棄物等原料之過程’主要包括熱裂解、碳化及活化三大 步驟，由於三者處理方式完全不同，且所需製程參數要求 差異甚Λ，因此一般係於獨立具有單一功能之熱裂解爐、 碳化爐戒活化爐中進行；大部份爐體設計僅以簡易的方 式，考量單一獨立的熱裂解製程、碳化製程或活化製程， 而熱裂解爐、碳化爐或活化反應爐之爐體外型，無論是臥 式爐、立式爐、單段式旋轉窯（爐）或双段式旋轉窯（爐）， 其爐體外型亦以配合乾燥、裂解、碳化或活化等單一功能 加以考量；此類傳統設置方式不僅無法連續作業，且機台 佔據極大空間。 【發明内容】 有鑑於習知技術之缺失’本發明之目的在於提出一種 子母同抽南溫旋轉反應爐，可將粉狀/粒狀/柱狀/球狀之原 料、活性礙或回收廢棄物等原料’在不間斷的進料、出料 與無氧的狀態下，藉由高溫加熱、攪拌與通入活化氣體， 使原料連續不斷的產生裂解反應、碳化反應與活化反應， 進而生產、改質與再生高孔洞性的高性能碳材之反應爐， 200920833 達到減少熱能 且生產過程中所產生之廢氣可回收再燃燒 消耗，資源再利用等目的。 為達到上述目的，本發明提出一種子母同軸高溫旋轉 反應爐，其包含：一儲料機構組，用以儲放原料；一入料 機組，與該儲料機構組連通，用以承接原料並可輸送原料； 一子式反應爐，可承接該入料機組所輸送之原料 掛 原料進行熱裂解或碳化反應；至少—母= 於該子式反應爐反應完成之原料，用以對原料進行碳化或 活化反應；一出料機構組，可承接於該母式反應爐反應完 成之原料’用以對原料進行冷卻及出料；一動力機構組， 用以驅動該母式反應爐；一旋轉支撐機構組，用以支撐該 母式反應爐疋位，一燃燒加熱室’用以回收廢棄再燃燒； 一咼壓燃燒機構組，用以負責該子母同軸高溫旋轉反應爐 之燃燒加熱。 為使貴審查委員對於本發明之結構目的和功效有更 進一步之了解與認同，茲配合圖示詳細說明如后。 【實施方式】 以下將參照隨附之圖式來描述本發明為達成目的所使 用的技術手段與功效，而以下圖式所列舉之實施例僅為輔 助說明，以利貴審查委員瞭解，但本案之技術手段並不限 於所列舉圖式。 請參閱第一圖至第三圖，本發明所提供之子母同軸高 溫旋轉反應爐，其主要包括有一儲料機構組1〇、入料機組 20、子式反應爐30、母式反應爐4〇、出料機構組5〇、動 力機構組60、旋轉支撐機構組7〇、氣密機構組8〇、氣體 供應機構組90、燃燒加熱室1〇〇、高壓燃燒機構組11〇、 200920833 基座120等機構組成。 該儲料機構組10係由第一儲料桶1〇1、入料第一問門 閥102、第二儲料桶103、入料第二閘門閥1〇4等機構組成， 該儲料機構組10係固定於入料機組2〇之原料入口法蘭 202，於該第一儲料桶1 〇 1下方設置該入料第一閘門閥1 並與該第二儲料桶103連接，於該第二儲料桶1〇3下方設 置該入料第二閘門閥104並與該入料機構組2〇連接。 原料可以人工方式將原料注入儲存於該第一儲料桶 101内’或可以自動抽取原料方式，以抽料機將原料抽離 包裝袋，注入儲存於第一儲料桶101内。當開啟該入料第 一閘門閥102 ’使原料進入該第二儲料桶1〇3時，先關閉 該入料第一閘門閥102，再開啟該入料第二閘門閥1〇4，使 原料可在高溫、無氧及氣氛狀態下，進入該入料機構組。 該入料機構組20係由原料輸送管固定法蘭201、原料 入口法蘭202、輸送馬達組203、原料輸送管204、原料輸 送螺旋葉片205等機構組成’該入料機構組20係由該原料 輸送管固定法蘭201固定於該母式反應爐40之前爐罩 402 ’通過該前爐罩402並插入該子式反應爐30。 當原料由該原料入口法蘭202進入原料輸送管204， 可藉由該輸送馬達組203及原料輸送螺旋葉片205之旋轉 作動’將原料推送進入該子式反應爐30。 該子式反應爐30係用以進行熱裂解及碳化反應，其係 由筒體301、筒體固定法蘭3〇2、出料口 303、導料螺旋線 或螺旋葉片304、導料螺旋線固定器30等機構組成，該子 式反應爐30之筒體301左側端口係插入該母式反應爐40 之前爐罩402内璧，由防止氣體洩漏之氣密機構組80固定 與支撐。筒體301之旋轉部份係由固定法蘭302連結於母 200920833 式反應爐40爐内支撐架上。而導料螺旋線或螺旋葉片304 係以導料螺旋線固定器305固定於筒體301上，可隨筒體 301旋轉’因而使原料得以持續向前推進，請參閱第四、 五圖所示。 當原料由該入料機組20推送進入該子式反應爐30 内，再經由爐體旋轉及爐内該導料螺旋線或螺旋葉片3〇4 的推進作用，原料得以緩慢前進，同時配合該子式反應爐 30加熱至攝氏約300〜700度，可使原料開始熱裂解而碳 化，而達熱裂解與碳化反應目的。當原料不斷前進，到達 反應爐尾端之出料口 303，掉落進入該母式反應爐4〇，即 完成第一階段的碳化反應製程，稱之為一次碳化。 該母式反應爐40係可進行碳化及活化反應，其係由筒 1前爐罩402、後爐罩403、原料輸送管入口 404、 ^氧體排放出口 、鏈輪齒輪組406、筒體支撐環 、後爐罩安全閥口 408、前爐罩活化料出料口 4〇9及長 二41 〇等機構組成，該母式反應爐40之筒體401呈約 祺沾^傾斜，該筒體401之傾斜度係可調整，可依不同原 化或活化溫度及時間需求’改變該筒體的 一具=，/〇者1^體4〇1内部圓周方向烊接等距且間斷的平 凸緣41G，當筒體4G1旋轉時，爐内活 Ιΐϊ獲得充分麟與活化。該筒體4G1左側及右侧 二」，入該前爐罩402與後爐罩，並由防 =機構組80加以固定與支樓。筒體4〇1外壁焊= 滑動407與該旋轉支撐機構組70之支撐輪組7〇1及pi =爐相：乍用，用咖 定&ί ί'ΐ避免筒體401因重量、高溫、_或 良，而4成該筒體401變形、錯位或位移。其次一， 200920833 該筒體401外壁之該鏈輪齒輪組406與該動力機構組60之 馬達601及變頻器602相互作用，透過馬達601、鏈輪603 的傳動及馬達變頻的作動，可使傾斜的筒體401得以依所 需速$緩慢旋轉。而該前爐罩402左前端所設置之該原料 輸送官，定法蘭201與入料機構組20相連接，該前爐罩 402上端之前爐罩氣體排放出口 405與廢氣排放管（圖中未 示出2目^接’使產生的廢氣得以進入該燃燒加熱室10 0再 燃燒，该前爐罩402下端所設置之前爐罩活化料出料口 409 與出料機構組50相連接。而該後爐罩403上端之後爐罩安 全閥口 408之作用在於，當爐體内爐溫不正常上升或爐壓 持續升高超出操作設定標準時，可透過該後爐罩安全閥口 408自動將氣體及時排放，以確保安全。再於前爐罩402 與後爐罩403的下方各設有一組氣體供應機構組90，負責 供應爐内各種不同氣氛及活化氣體；而該前爐罩402與該 後爐罩403之底部，係固定於該基座120上。 上述該第一階段碳化反應完成後的碳化料掉落進入該 母式反應爐40時’經由該傾斜筒體401及旋轉作用，可使 碳化料不斷前進’配合該母式反應爐40爐内持續升溫加熱 至攝氏約500~900度，可達最終碳化溫度；當碳化料持續 前進到達該母式反應爐40尾端出口，進入出料機構組50 後’即完成第二階段的碳化反應製程，稱之為二次碳化。 如在第二階段的碳化反應過程中，相對提高該母式反應爐 40爐内溫度至攝氏700〜1050度，並輸入不同的活化氣體， 即可使該母式反應爐40轉變成為具有活化功能之活化反 應爐，而達原料活化目的。當該傾斜之筒體401不斷旋轉 與筒體401内該長條狀凸緣410之擾拌作用，可使爐内活 化料得以缓慢前進，到達該母式反應爐40尾端出口，進入 11 200920833 出料機構組50冷卻後出料，即完成第一階段的活化反應製 程’稱之為一次活化。當第—階段之活化反應製程無法滿 足產品需求時，可採取下列二項步驟進行之： (1) 將第一階段活化反應尚未活化完全的活化料，直接 進入該出料機構組50冷卻後，再重複進行上述步驟。此 時’該子式反應爐30即成為補充碳化的碳化反應爐，該母 式^應爐40即成為補充活化的活化反應爐；當筒體401不 斷旋轉’爐内溫度到達所需溫度約攝氏8〇〇〜1〇5〇度時，輸 入不同之活化氣體後，爐内活化料到達母式反應爐4〇尾端 出口，進入該出料機構組5〇後，既完成第二階段的活化反 應製程，稱之為二次活化。 (2) 將第一階段活化反應尚未活化完全的活化料，在未 ，入该出料機構組5〇前，以連接管將未活化完全的活化 直接送入第二組母式反應爐（圖中未示出），此時，該 第一組母式反應爐即成為活化反應爐；當該第二組母式反 應爐爐内溫度到達所需溫度約攝氏8〇〇~1〇5〇度時，輸入不 同^活化氣體後，即完成第二階段的活化反應製程，稱之 為二次活化；據此可知，可視活化反應製程及產品需要， 規劃增加一組或二組該母式反應爐4〇。 、該出料機構組50係由冷卻筒501、成品輸送螺旋502、 ^送動力組503、區間閘門閥504、出料閘門閥505、成品 區間法蘭506、成品出料法蘭507等機構組成，該出料機 構組50係由成品區間法蘭506固定於該母式反應爐40， 於1成品區間法蘭506下方設置該區間閘門閥504，用以 負責控制活化料可在無氧之狀態下進入該冷卻筒5〇1，該 冷备卩筒501為雙層裝置，其内部具有冷確循環水，可用以 冷卻該冷卻筒501内部之活化料。另者，該冷卻筒501内 12 200920833 設有該成品輸送螺旋502，可負責活化料之輸送，其動力 來源係由冷卻筒501左侧之該輸送動力組503供應；該冷 卻筒501左側為活化料出料口，設置於該出料口之該出料 閘門閥505係由該成品區間法蘭506固定之。 當活化反應製程完成的活化料由該母式反應爐40尾 端出口進入該出料機構組50時，首先打開該區間閘門閥 504，使活化料得以進入該冷卻筒501，原本溫度約為攝氏 800〜1050度之高溫活化料經由該成品輸送螺旋502之輸 送，可於該冷卻筒501内緩慢冷卻，經冷卻至室溫之活化 料在確保無氧的狀態下，打開該出料閘門閥505，即可將 冷卻後之活化料成品排出口，再篩選、打包並裝袋。 該燃燒加熱室100係由加熱爐1001、熱能防漏裝置 1002、熱能輸入口 1003、廢氣排放口 1004、煙道1005等 機構組成，該燃燒加熱室100左右爐壁中心，由該母式反 應爐40之筒體401穿設而過，其穿設位置即設置該環狀熱 能防漏裝置102，用以防止燃燒加熱室100之熱能外漏。 於該燃燒加熱室100之上部前方設置有1〜4個該熱能輸入 口 1003，以及設置1〜4台之高壓燃燒機構組110。 請參閱第二圖所示，高壓燃燒機構組110由全自動雙 燃料比例式燃燒機1101、廢沼氣回收喷燃裝置1102及馬 達幫浦1103、燃料箱1104所構成，該高壓燃燒機構組110 係用以負責該子母同軸高溫旋轉反應爐之燃燒加熱，燃料 箱1104之燃料係由馬達幫浦1103輸送至全自動雙燃料比 例式燃燒機1101，該高壓燃燒機組110之全自動雙燃料比 例式燃燒機1101，可依不同溫度需求調整該馬達幫浦1103 大小及燃料、空氣比例。該廢沼氣回收喷燃裝置1102可依 原料熱裂解、碳化、活化不同時斷及所產生廢沼氣量的大 13 200920833 小；該回收喷燃裝置1102所回收之廢沼氣可全數回收再導 入該燃燒加熱室100完全燃燒，使CO、C〇2及黑煙之排放可 達環保標準’不致造成二次污染。至於該燃燒加熱室100 上部後方所設置之廢氣排放口 1004、煙道1005以及該燃 燒加熱室100底座’均固定於該基座120上。 綜上所述可知’本發明所提供之子母同轴高溫旋轉反 應爐，與習知熱裂解爐、碳化爐或活化爐之外型及功能上 均具有極大差異，具有以下優點： (―)就設備外型上，反應爐屬子母同軸型式，其最大優點： 1.可以有效縮短設備尺寸；2.可以有效的減少場地設 置空間；3.可以設置於車上隨需要移動設備；4.操 簡易。 (一*)就汉備功此上.1.在無氧及南溫的情形下，可連續不 間斷的進料，2.在無氧及咼溫的情形下，可連續不間 斷的出料，3.可單獨連續的進行乾燥處理；4.可單獨 連續的進行熱裂解反應處理；5.可單獨連續的進行碳 化反應處理；6·可單獨連續的進行活化反應處理；7 可同時進行乾燥與熱裂解反應製程；8•可同時進行埶 裂解與碳化反應製程；9.可同時進行碳化與活化反^ 製程；10.可同時進行熱裂解、碳化與活化反應製程。 因此本發明之最的大特色與目的，在於使用者可依不 =枓、種類及需求’進行不同的製程參數設定，而設計 壤，所須的製程，而習知熱裂解爐、碳化爐或活化 "無_在型式上與功能上，均無法達到此需求。 惟以上所述者，僅為本發明之最佳實施：已，當不 利蘇本發明所實施之範圍。即大凡依本發明申請專 爽圍所作之均等變化與修飾，皆應仍屬於本發明專利涵 14 200920833 蓋之範圍内，謹請貴審查委員明鑑，並祈惠准，是所至 禱。 【圖式簡單說明】 第一圖係本發明之實施例架構示意圖。 第二圖係本發明實施例之高壓燃燒機組及燃燒加熱室 結構不意圖。 第三圖係本發明實施例之動力機組、旋轉支撐機組結 構不意圖。 第四、五圖係本發明之局部結構示意圖。 【主要元件符號說明】 10-儲料機構組 101- 第一入料儲存桶 102- 入料第一閘門閥 103- 第二入料儲存桶 104- 入料第二閘門閥 20-入料機構組 201- 原料輸送管固定法蘭 202- 原料入口法蘭 203- 輸送馬達組 204- 原料輸送管 205- 原料輸送螺旋葉片 30-子式反應爐 301-筒體 15 200920833 302- 筒體固定法蘭 303- 出料口 304- 導料螺旋線或螺旋葉片 305- 導料螺旋線固定器 40-母式反應爐 401- 爐筒體 402- 前爐罩 403- 後爐罩 404- 原料輸送管固定入口 405- 前爐罩氣體排放出口 40 6-鏈輪齒輪組 407- 筒體支撐環 408- 後爐罩安全閥口 409- 前爐罩活化料出料口 410 -長條凸緣 50-出料機構組 501- 冷卻筒 502- 成品輸送螺旋 503輸送動力組 504- 區間閘門閥 505- 出料閘門閥 506- 成品區間法蘭 507- 成品出料法蘭 60-動力機構組 6 01 -馬達 16 200920833 602-變頻器 6 03-鍊條 70-旋轉支撐機構組 701- 支撐輪組組 702- 防滑動輪組 80-氣密機構組 90-氣體供應機構組 100-燃燒加熱室 1001- 加熱爐 1002- 熱能防漏裝置 100 3-熱能輸入口 1004_廢氣排放口 1005-煙道 110 -南壓燃燒機構組 1101- 全自動雙燃料比例式燃燒機 1102- 廢沼氣回收喷燃裝置 1103- 馬達幫浦 1104- 燃料箱 120-基座 17200920833 IX. INSTRUCTION DESCRIPTION OF THE INVENTION [Technical Field] The present invention relates to a sub-mica coaxial high-temperature rotary reactor, and more particularly to a high-temperature oxygen-free reaction furnace having three functions of thermal cracking, carbonization, and activation rotation. [Prior Art] Conventional processes for processing raw materials such as powder/granular/columnar/spherical materials, activated carbon or recycled waste mainly include three steps of thermal cracking, carbonization and activation. Different, and the required process parameters vary widely, so it is generally carried out in a separate thermal cracking furnace, carbonization furnace or activation furnace with a single function; most of the furnace design is only in a simple way, considering a single independent heat Cracking process, carbonization process or activation process, and furnace type of pyrolysis furnace, carbonization furnace or activation reactor, whether it is horizontal furnace, vertical furnace, single-stage rotary kiln (furnace) or two-stage rotary kiln ( Furnace), the furnace type is also considered to be a single function of drying, cracking, carbonization or activation; such traditional setting methods can not only continue to operate, but the machine takes up a lot of space. SUMMARY OF THE INVENTION In view of the lack of the prior art, the object of the present invention is to provide a sub-mother and a south-temperature rotary reaction furnace, which can be used for powder/granular/columnar/spherical materials, active or recycled. The raw materials such as materials are continuously produced by the high temperature heating, stirring and introduction of the activating gas under the conditions of uninterrupted feeding, discharging and anaerobic, so that the raw materials continuously generate cracking reaction, carbonization reaction and activation reaction, and then produce, Reactor for upgrading and regenerating high-porosity high-performance carbon materials, 200920833 To achieve the purpose of reducing heat energy and recovering waste gas from re-burning and recycling of resources generated during production. In order to achieve the above object, the present invention provides a sub-coaxial coaxial high-temperature rotary reaction furnace, which comprises: a storage mechanism group for storing raw materials; and a feeding unit connected with the storage mechanism group for receiving raw materials and The raw material can be transported; a sub-reactor can be used to carry out thermal cracking or carbonization reaction of the raw material of the raw material conveyed by the feeding unit; at least - the raw material in the reaction of the sub-reactor is used for carbonizing the raw material. Or activation reaction; a discharge mechanism group, which can be subjected to the raw material of the reaction of the mother reactor to cool and discharge the raw material; a power mechanism group for driving the mother reaction furnace; The mechanism group is used for supporting the mother reactor, the combustion heating chamber is used for recycling waste and reburning; and the rolling combustion mechanism group is responsible for the combustion heating of the mother-child coaxial high-temperature rotary reactor. In order to enable the reviewing committee to have a better understanding and approval of the structural purpose and efficacy of the present invention, the detailed description is as follows. [Embodiment] Hereinafter, the technical means and effects of the present invention for achieving the object will be described with reference to the accompanying drawings, and the embodiments listed in the following drawings are only for the purpose of explanation, so that the reviewer understands, but the case Technical means are not limited to the illustrated figures. Referring to the first to third figures, the present invention provides a coaxial high-temperature rotary reaction furnace, which mainly comprises a storage mechanism group 1〇, a feeding unit 20, a sub-reaction furnace 30, and a mother-type reaction furnace. , discharge mechanism group 5〇, power mechanism group 60, rotary support mechanism group 7〇, airtight mechanism group 8〇, gas supply mechanism group 90, combustion heating chamber 1〇〇, high-pressure combustion mechanism group 11〇, 200920833 120 and other institutions. The stocking mechanism group 10 is composed of a first storage tank 1〇1, a first feed gate valve 102, a second storage tank 103, a second gate valve 1〇4, and the like, and the storage mechanism group 10 is fixed to the material inlet flange 202 of the feeding unit 2, and the first gate valve 1 is disposed below the first storage tank 1 〇1 and connected to the second storage barrel 103. The incoming second gate valve 104 is disposed below the second storage tank 1〇3 and is connected to the feeding mechanism group 2〇. The raw material can be manually injected into the first storage tank 101 or the raw material can be automatically extracted, and the raw material can be pumped out of the packaging bag by the suction machine and injected into the first storage tank 101. When the first gate valve 102' is opened to allow the raw material to enter the second storage tank 1〇3, the first gate valve 102 is closed first, and then the second gate valve 1〇4 is opened. The raw materials can enter the feeding mechanism group under high temperature, oxygen-free and atmospheric conditions. The feeding mechanism group 20 is composed of a raw material conveying pipe fixing flange 201, a raw material inlet flange 202, a conveying motor group 203, a raw material conveying pipe 204, a raw material conveying spiral blade 205, and the like. Before the raw material delivery pipe fixing flange 201 is fixed to the mother reaction furnace 40, the furnace cover 402' passes through the front furnace cover 402 and is inserted into the sub-reaction furnace 30. When the raw material enters the raw material delivery pipe 204 from the raw material inlet flange 202, the raw material can be pushed into the sub-reaction furnace 30 by the rotation of the conveying motor group 203 and the raw material conveying spiral blade 205. The sub-reaction furnace 30 is used for performing thermal cracking and carbonization reaction, which is composed of a cylinder 301, a cylinder fixing flange 3〇2, a discharge port 303, a guide spiral or a spiral blade 304, and a guide spiral. The fixing device 30 and the like are composed of a mechanism, and the left port of the cylindrical body 301 of the sub-type reaction furnace 30 is inserted into the furnace cover 402 before the mother-type reaction furnace 40, and is fixed and supported by the airtight mechanism group 80 for preventing gas leakage. The rotating portion of the cylinder 301 is coupled to the support frame of the mother furnace of the 200920833 type reaction furnace 40 by a fixing flange 302. The guide spiral or spiral blade 304 is fixed to the cylinder 301 by the guide screw holder 305, and can rotate along with the cylinder 301, so that the raw material can be continuously advanced. Please refer to the fourth and fifth figures. . When the raw material is pushed into the sub-reaction furnace 30 by the feeding unit 20, and then through the rotation of the furnace body and the advancement of the guide spiral or the spiral blade 3〇4, the raw material can slowly advance and cooperate with the sub-feeder. The reaction furnace 30 is heated to about 300 to 700 degrees Celsius, and the raw material can be thermally cracked and carbonized to achieve the purpose of thermal cracking and carbonization reaction. As the raw material continues to advance, it reaches the discharge port 303 at the end of the reactor and falls into the mother reactor 4, completing the first stage of the carbonization process, which is called primary carbonization. The mother reactor 40 is capable of carbonization and activation reaction, which is composed of a front furnace cover 402, a rear furnace cover 403, a raw material delivery pipe inlet 404, an oxygen discharge outlet, a sprocket gear set 406, and a cylinder support. The ring, the rear furnace cover safety valve port 408, the front furnace cover activation material discharge port 4〇9, and the long two 41 〇 mechanism, the cylinder 401 of the mother reaction furnace 40 is inclined, the cylinder body The inclination of the 401 can be adjusted, and the one of the cylinders can be changed according to different originalization or activation temperature and time requirements, and the inner circumferential direction of the 1^body 4〇1 is connected to the equidistant and intermittent planoconvex. At the edge 41G, when the cylinder 4G1 rotates, the live raft in the furnace is fully activated and activated. The left side and the right side of the cylinder 4G1 are inserted into the front furnace cover 402 and the rear furnace cover, and are fixed to the branch by the anti-mechanism group 80. The outer wall welding of the cylinder 4〇1=sliding 407 and the supporting wheel set 7〇1 and pi=the furnace phase of the rotating support mechanism group 70 are used for the purpose of avoiding the weight and high temperature of the cylinder 401 by the coffee and the 咖 ί , _ or good, and 40% of the cylinder 401 is deformed, misaligned or displaced. Next, 200920833, the sprocket gear set 406 of the outer wall of the cylinder 401 interacts with the motor 601 and the frequency converter 602 of the power mechanism group 60, and can be tilted by the transmission of the motor 601, the sprocket 603, and the motor frequency conversion. The barrel 401 is able to rotate slowly at the desired speed of $. The raw material conveying officially disposed at the front end of the front furnace cover 402 is connected to the feeding mechanism group 20, and the upper end of the front furnace cover 402 is preceded by the furnace gas discharge outlet 405 and the exhaust gas discharge pipe (not shown) The generated exhaust gas can enter the combustion heating chamber 10 and re-burn, and the lower furnace cover activated material discharge port 409 is connected to the discharge mechanism group 50 at the lower end of the front furnace cover 402. After the upper end of the furnace cover 403, the function of the furnace safety valve port 408 is to automatically discharge the gas through the rear furnace safety valve port 408 when the furnace temperature in the furnace body rises abnormally or the furnace pressure continues to rise beyond the operating setting standard. In order to ensure safety, a set of gas supply mechanism groups 90 are respectively disposed under the front furnace cover 402 and the rear furnace cover 403, and are responsible for supplying various atmospheres and activation gases in the furnace; and the front furnace cover 402 and the rear furnace cover The bottom of the 403 is fixed on the susceptor 120. When the carbonized material after the completion of the first-stage carbonization reaction falls into the mother-type reaction furnace 40, the carbonized material can be made through the inclined cylinder 401 and the rotating action. Keep moving forward The mother furnace 40 is continuously heated to a temperature of about 500-900 degrees Celsius to reach the final carbonization temperature; when the carbonized material continues to advance to the outlet end of the mother reactor 40, after entering the discharge mechanism group 50' That is, the second stage carbonization process is completed, which is called secondary carbonization. For example, in the second stage of the carbonization reaction, the temperature of the mother reactor 40 is relatively increased to 700 to 1050 degrees Celsius, and different inputs are input. By activating the gas, the mother reactor 40 can be transformed into an activation reactor having an activation function for the purpose of material activation. When the inclined cylinder 401 is continuously rotated and the elongated flange 410 in the cylinder 401 The disturbing action can make the activated material in the furnace advance slowly, reach the outlet end of the mother reactor 40, enter the 11 200920833 discharge mechanism group 50 after cooling and discharge, that is, complete the first stage of the activation reaction process For the first activation, when the activation process of the first stage cannot meet the product requirements, the following two steps can be taken: (1) The first stage activation reaction has not yet activated the complete activation material, directly After the cooling of the discharge mechanism group 50 is completed, the above steps are repeated. At this time, the sub-reaction furnace 30 becomes a carbonization reaction furnace which is supplemented with carbonization, and the mother-type furnace 40 becomes a supplementary activated activation reaction furnace; When the cylinder 401 is continuously rotated, when the temperature in the furnace reaches the required temperature of about 8 〇〇 1 〇 5 摄 5 degrees, after inputting different activation gases, the activation material in the furnace reaches the exit end of the mother reactor 4, and enters. After the discharge mechanism group 5, the second stage activation reaction process is completed, which is called secondary activation. (2) The first stage activation reaction has not activated the complete activation material, and the injection mechanism is not introduced into the discharge mechanism. Before the group 5〇, the unactivated complete activation is directly sent to the second group of the mother reactor (not shown) by the connecting pipe. At this time, the first group of the mother reactor becomes the activation reactor; When the temperature in the second set of the mother reactor reaches the required temperature of about 8 〇〇 to 1 〇 5 摄, the activation reaction process of the second stage is completed after inputting different activation gases, which is called secondary Activation; according to this, the visible activation reaction process and Product needs, planning a group or two groups to increase the female-type reactor 4〇. The discharging mechanism group 50 is composed of a cooling cylinder 501, a finished conveying screw 502, a sending power group 503, a section gate valve 504, a discharging gate valve 505, a finished section flange 506, a finished discharging flange 507, and the like. The discharge mechanism group 50 is fixed to the mother reaction furnace 40 by the finished section flange 506, and the interval gate valve 504 is disposed under the 1 finished section flange 506 for controlling the activation material to be in an oxygen-free state. Down into the cooling cylinder 5〇1, the cold preparation cylinder 501 is a double-layered device having cold circulating water inside, which can be used to cool the activated material inside the cooling cylinder 501. In addition, the cooling cylinder 501 12 200920833 is provided with the finished conveying screw 502, which can be responsible for the transportation of the activated material, and the power source thereof is supplied by the conveying power group 503 on the left side of the cooling cylinder 501; the left side of the cooling cylinder 501 is activated The material discharge port, the discharge gate valve 505 disposed at the discharge port is fixed by the finished section flange 506. When the activation material completed by the activation reaction process enters the discharge mechanism group 50 from the outlet end of the mother reaction furnace 40, the interval gate valve 504 is first opened to allow the activated material to enter the cooling cylinder 501, and the original temperature is about Celsius. The high temperature activated material of 800~1050 degrees is transported through the finished conveying screw 502, and can be slowly cooled in the cooling cylinder 501. The cooling material cooled to room temperature opens the discharging gate valve 505 under the state of ensuring no oxygen. The cooled activated product product can be discharged, filtered, packaged and bagged. The combustion heating chamber 100 is composed of a heating furnace 1001, a thermal energy leakage preventing device 1002, a thermal energy input port 1003, an exhaust gas discharge port 1004, a flue 1005, and the like. The combustion heating chamber 100 is located at the center of the furnace wall, and the mother reaction furnace is The cylinder 401 of 40 is passed through, and the annular thermal energy leakage preventing device 102 is disposed at a position to prevent leakage of heat energy from the combustion heating chamber 100. One to four such heat energy input ports 1003 and one to four high pressure combustion mechanism groups 110 are disposed in front of the upper portion of the combustion heating chamber 100. Referring to the second figure, the high-pressure combustion mechanism group 110 is composed of a fully automatic dual-fuel proportional combustion machine 1101, a waste biogas recovery combustion device 1102, a motor pump 1103, and a fuel tank 1104. Responsible for the combustion heating of the mother-child coaxial high-temperature rotary reactor, the fuel of the fuel tank 1104 is sent from the motor pump 1103 to the fully automatic dual-fuel proportional burner 1101, and the automatic dual-fuel ratio of the high-pressure combustion unit 110 The burner 1101 can adjust the size of the motor pump 1103 and the ratio of fuel to air according to different temperature requirements. The waste biogas recovery and combustion device 1102 can be small according to the thermal cracking, carbonization, activation, and the amount of waste biogas generated by the raw material; the waste biogas recovered by the recovery and combustion device 1102 can be fully recovered and then introduced into the combustion. The heating chamber 100 is completely burned, so that the emission of CO, C〇2 and black smoke can reach the environmental protection standard' without causing secondary pollution. The exhaust gas discharge port 1004, the flue 1005, and the base of the combustion heating chamber 100, which are disposed at the rear of the combustion heating chamber 100, are fixed to the base 120. In summary, it can be seen that the sub-coaxial high-temperature rotary reaction furnace provided by the present invention has great differences in appearance and function from the conventional thermal cracking furnace, carbonization furnace or activation furnace, and has the following advantages: (―) On the appearance of the equipment, the reaction furnace is a coaxial type of the mother and child, and its biggest advantages: 1. It can effectively shorten the size of the equipment; 2. It can effectively reduce the space for setting the venue; 3. It can be set on the vehicle and move the equipment as needed; 4. simple. (一*) On the Han dynasty work. 1. In the case of anaerobic and south temperature, continuous uninterrupted feeding, 2. In the case of anaerobic and enthalpy, continuous uninterrupted discharge 3. The drying treatment can be carried out continuously continuously; 4. The thermal cracking reaction can be carried out continuously continuously; 5. The carbonization reaction can be carried out continuously; 6) The activation reaction can be carried out continuously; 7 can be dried simultaneously And thermal cracking reaction process; 8 • Simultaneous cesium cracking and carbonization process; 9. Simultaneous carbonization and activation reaction process; 10. Simultaneous thermal cracking, carbonization and activation reaction processes. Therefore, the most important feature and purpose of the present invention is that the user can design different processes parameters according to different types, process requirements, and design processes, and the conventional thermal cracking furnace, carbonization furnace or Activation "no _ in terms of type and function, can not meet this demand. However, the above is only the best practice of the present invention: it has been limited to the scope of the invention. That is to say, the equal changes and modifications made by the applicants in accordance with the application of the present invention should still fall within the scope of the patent of the invention 14 14 200920833, and I would like to ask your review committee to give a clear explanation and pray for the best. BRIEF DESCRIPTION OF THE DRAWINGS The first figure is a schematic diagram of an embodiment of the present invention. The second drawing is not intended to be a high-pressure combustion unit and a combustion heating chamber structure according to an embodiment of the present invention. The third figure is not intended to be a power unit or a rotary support unit according to an embodiment of the present invention. The fourth and fifth figures are schematic views of the partial structure of the present invention. [Main component symbol description] 10-Storage mechanism group 101- First feed storage tank 102- Feed first gate valve 103- Second feed storage tank 104- Feed second gate valve 20-Feed mechanism group 201- Raw material conveying pipe fixing flange 202- Raw material inlet flange 203- Conveying motor group 204- Raw material conveying pipe 205- Raw material conveying spiral blade 30-Sub-reaction furnace 301-Cylinder 15 200920833 302- Cylinder fixing flange 303 - Outlet 304 - Guide spiral or spiral blade 305 - Guide spiral holder 40 - Female reactor 401 - Furnace body 402 - Front furnace cover 403 - Rear furnace cover 404 - Raw material delivery pipe fixed inlet 405 - Front hood gas discharge outlet 40 6- sprocket gear set 407 - Cylinder support ring 408 - Rear hood safety valve port 409 - Front hood activation material discharge port 410 - Long flange 50 - Discharge mechanism group 501- Cooling cylinder 502- Finished product conveying screw 503 conveying power group 504- Interval gate valve 505- Discharge gate valve 506- Finished section flange 507- Finished material discharge flange 60-Power mechanism group 6 01 -Motor 16 200920833 602- Inverter 6 03-Chain 70-Rotary Support Mechanism Group 701- Support Wheel Set 702- Non-slip Wheel set 80 - airtight mechanism group 90 - gas supply mechanism group 100 - combustion heating chamber 1001 - heating furnace 1002 - thermal energy leakage preventing device 100 3-thermal energy input port 1004_exhaust gas discharge port 1005 - flue 110 - south pressure combustion mechanism Group 1101 - Fully automatic dual fuel proportional burner 1102 - Waste biogas recovery burner 1103 - Motor pump 1104 - Fuel tank 120 - Base 17