201211273 六、發明說明： 【發明所屬之技術領域】 本發明係有關於一種熱散裝物品用冷卻設備。 【先前技術】 在冷卻諸熱散裝物品（例如燒結鐵礦）時盡可能有效 地利用與其同時所生成之廢熱的嘗試。 呈圓形井下熱交換器或圓形刮面熱交換器型式之又 流式熱交換器係屬先前技藝。然而，在圓形井下熱交換 器之情形中，隨著廢氣溫度持續下降，使得廢熱回收將 被限制在此熱交換器的前三分之一。在圓形刮面熱交換 器之情形中’將有熱與暖廢氣之混.合存在，但其溫度基 本上不可能達到如最高時之情形，以致使得廢熱回收之 效率也被降低。 【發明内容】 本發明之目的在於，藉由諸熱散裝物品於冷卻期間 所生成之廢熱可被更有效利用之手段，以創造許多可行 性0 此目地係經由-種具有如申請專利範圍帛i項中所 述特徵之熱散裝物品用冷卻設備而達成。本發明中所請 求之冷卻設備的其他有利發JS·目丨丨总* &由 』赞展則係申請專利範圍第2至 9項附屬項之目的。 一種熱散裝物品用 被發展成使得 -此冷卻設備包括一具 散裝物品在此冷卻塔 冷卻设備將如本發明中所請求般 有—垂直主軸之冷卻塔，而諸熱 中係藉由—氣流被冷卻， 201211273 -此冷卻設備具有一供應裝置’而諸熱散裝物品藉由此 供應褒置從上方灌注至冷卻塔内，使諸熱散裝物品可 堆置於該冷卻塔中， -此冷卻設備具有一移除裝置，而處於冷狀態下之諸散 裝物品藉由此移除裝置從冷卻塔之底部移除，以便使 餘留在該冷卻塔中之諸散裝物品可向下地滑出， 一此冷卻設備具有一送氣裝置，而氣流藉由此送氣裝置 被輸送通過冷卻塔， -此冷卻設備具有一帶離裝置，而氣流藉由此帶離裝置 被帶離冷卻塔， 一複數個氣流引導手段被配置在冷卻塔中，而諸氣流引 導手段從複數個被配置在該塔外壁中之入口處起徑 向地向内延伸至該主軸， 諸氣流引導手段被實施成細長型引導手段，其當朝各 自之延伸方向觀看時在其長度上具有複數個玎供氣 流用之出口，以致使此氣流可被引入位於冷卻塔中之 諸熱散裝物品内， —在朝該主軸之方向觀看時，諸氣流引導手段被配置在 "p ?之中央區域中，且該帶離裝置被配置在冷卻塔 之上部區域中，以致使此氣流從底部至頂部地橫貫位 於此冷卻塔中之諸熱散裝物品。 此發展在於達成：氣流並非以交又流而是以反向流 只貝諸熱散裝物品。因此不可能再有熱與暖廢氣之混合。 角声 的疋，諸氣流引導手段相對於水平形成一傾斜 又’以使此諸氣流引導手段可向上傾斜至該主軸。此 201211273 發展進一步優化廢埶 m壁# & 士 …、利用之效率。此在，如果此傾斜角 度被選疋成大約與接细i ” 裝物品角度尤1可起=相對於水平所形成之散 介於20。與45。之間作用。因此，此傾斜角度較佳地係 曰〕且大部分情形係介於25。盘35。之 間0 '、 車{的疋，諸出口被獨有地配置在諸氣流引導手段 此發展在於達成：使諸出口阻塞之風險被 降至最低，且甚至被完全避免。 。“將諸出口獨有地配置在諸氣流引導手段之下表面上 :藉由下述達成，例如：在各種情形下均具有兩個側面 區f及一個橋接此諸側面區域之頂部區域的諸氣流引導 手#又大致成垂直延伸之側面區域，以及具有成倒r v」 形狀之戴面的頂部區域。 諸氣流引導手段較佳的是延伸直至主軸處，或直至 一被配置在此主軸上之轂部處。於此達成：諸熱散裝物 品實際上在冷卻塔的整個橫截面上可被氣流橫貫並冷 卻。 帶離裝置較佳的是被配置在該塔外壁中。此發展在 於達成.可在無需考量此帶離裝置之發展下設計該供應 裝置。 在本發明之一較佳發展中，此供應裝置係呈一旋轉 導槽之形式。此發展達成使諸熱散裝物品在冷卻塔之截 面面積上有更好之分佈。 較佳的是，此冷卻設備被發展成使得： -冷卻塔被配置在一建築物中，而此建築物之諸側壁從 201211273 底部起延伸直至諸入口上方處， 移除裝置被配置在此建築物之内部，以便使自冷卻塔 處移除之諸散裝物品被安置在此建築物之内部， -此冷郃設備具有一連續式輸送裝置，則自冷卻塔中移 除之諸散裝物品可藉由此連續式輸送裝置被帶離該 建築物， 此連續式輸送裝置具有多個槽狀容器，其在相對於輸 送方向橫向觀看時具有-容器截®，而在朝此輸送方 向觀看時則具有一容器長度， 諸容器經由兩個被實施成隧道形式之通道區域而從 忒建築物露出並進入該建築物内，並且 -諸隨道之截面係順應該容器截面，當朝諸隨道輸送方 向觀看時’均具有大於該容器長度之隧道長度。 此發展在該送氣裝置被實施成風扇時尤其有利。此 風扇在於達成使該氣流之洩漏損失最小化。 其它優點與細節可兹+ θ , 、即了藉由下列不範性實施例之說明以 及配合參照所附圖式而被提出。 【實施方式】 如弟1圖所示 品1 (例如小 垂直主軸3 4而被冷卻 禋用於冷卻熱散I 顆粒^燒結鐵礦）之冷卻設備具有一配備 之冷郃塔2。此諸熱散裝物品1係藉由 於冷卻塔2中。 物品 此乃 1藉 意謂 此冷卻設備具有—供應裝置5。諸熱散 由供應裝置5而從上方被灌注至冷卻塔2内、 此諸熱散裝物品1會被堆積在冷卻塔2中。 201211273 對應於第1圖中所示，供應裝置5可被實施成—以 預定速度η而轉動之旋轉導槽。速度η通常係相當低的。 例如，倘若供應裝置5被發展成一旋轉導槽，則逮度η 可在0.25 rev/min(轉數/分鐘）至1 rev/min間之範圍内。 成為一旋轉導槽之設計意謂諸熱散裝物品1較佳的 係分布在冷卻塔2之（水平）橫截面上。然而，可由供應 裝置5藉以分布諸熱散裝物品1之有效半徑r，通常係顯 著小於冷卻塔2之半徑R。具體而言，此由供應裝置5 藉以分布諸熱散裝物品1之有效半徑r最大係冷卻塔2 之半徑R的30%。在大部分情形中，所達數值甚至僅在 10%與25%之間。因此，一頂錐被形成於塔外壁6(亦即 冷卻塔2之垂直或大致垂直壁）附近。此頂錐具有—典型 之散裝物品角度α。通常，此散裝物品角度α(取決^諸 散裝物品1)係介於大約3 0。與大約3 8。之間。 ^ 此外，此冷卻設備具有一移除裝置7。諸散裝物品^ 藉由此移除裝置7而被從冷卻塔2之底部移除。此乃音 謂餘留在冷卻塔2中之諸散裝物品1會向下I滑出^ ^ 移除裝置7可被實施成一能以圓形方式 此 叉砂動之推台。 此冷卻設備亦具有一送氣裝置8。氣流4經 氣裝置8被輸送通過冷卻塔2。送氣裝_置8 & 施成-風扇。然而，原則上亦可成為—抽佳地被Λ 久我置。 4藉由此帶 此冷卻設備亦具有一帶離裝置9。氣、、穿 離裝置9被帶離冷卻塔2。 當諸散裝物品1被供應至冷卻拔2拉 丨D Ζ砰，這此物品是 熱的。此時典型之溫度達到9〇〇〇C。备訣也 ~ 田请政裴物品1從 201211273 冷卻塔2被移除時，、二 之溫度係介於7〇。。至Μ物品是(相當)冷的。此時典型 卻大致係藉由流經Av:c之間。諸熱散裝物品1之冷 氣…以冷的Λ :2之氣流4而被執行。因此， 卻塔2中，且係以^、'皿度通常寺於周遭溫度）被引至冷 ’ ·、、、的狀態（溫度通常介於6〇〇。(：1 800oe 之間)自冷卻塔2處被帶離。 冷卻塔2通常被配置在一建築 1 〇具有多個側壁丨丨 、 中。此建築物 塔2之-中間高户U 11從底#起延伸至冷卻 個古卢Μ μ Λ又處。通常，相對於此冷卻塔2之整 個…’此中間高度h係介於 ：： Η的40。/。與6〇%之間。 。2之整個尚度 送氣裝置8(特別是如果装 置在建築㈣内部。缺而，、;”貫"成一風扇)可被配 築物10外H M k孔裝置8通常被配置在建 外4。▼離裝置9被配 中，且因此在涂罝在冷郃塔2之上部區域 U此在建桌物1 0之外部。 π離裴置9可被配置在冷 離裝置9較佳的是 。2之上表面12上。帶 置在塔外壁6中，亦即在側面。 複數個氣流引導手段丨3 ,、 在側面 上，氣流弓|導手段j 3之最己置在冷钟％ 2中。原則 本實施例中至少有〜’、之量係兩個。然而’實際上 引導手段u之最大數量俜 x原則上’氣、 會超過4〇個。+ 糸…、限制的。然而，通常數量不 數量係介於8與16之間。 中軋抓引導手段丨3之 諸氧流引導手段1 3祐眘於』、 形引導手ρ。此 、&成如第1圖中所示之細長 又此堵手段具有被酉己置在塔外壁6之入口 -10- 201211273 14。從此諸入口 14處，氣流引導手段1 3徑向地朝内延 伸至冷卻塔2之主軸3。此諸氣流引導手段1 3之發展例 如可為輪輻狀（如圖所示）、新月形等。其他之發展亦係 可能的。唯一之重要因素在於：其與冷卻塔2之主軸3 相隔的距離必須沿著氣流引導手段之縱向延長而減小。 諸氣流引導手段1 3(當由其各自之延伸方向觀看時 在其長度上）具有可供氣流4用之出口 1 5。氣流4(在仍 冷之時刻）藉由諸入口 1 4被引入諸氣流引導手段1 3内， 並藉由諸出口 15而自該處被引導至位於冷卻塔2中之諸 熱散裝物品内。 諸氣流引導手段1 3之截面在從其長度上觀看時可 為恆定的。然而，諸氣流引導手段1 3之截面較佳地係朝 冷卻塔2之主轴3而減小，對應第1圖所示。 當由冷卻塔2之主軸3方向觀看時，諸氣流引導手 段1 3被配置在冷卻塔2之中央區域1 6。此中央區域1 6 從冷卻塔2之整個高度Η的大約30%處起延伸至冷卻塔 2之整個高度Η的大約70%處。然而，與諸氣流引導手 段1 3之精確配置無關的是，此諸氣流引導手段1 3被配 置在帶離裝置9之下方。當冷卻塔2被配置在建築物10 中時，諸入口 1 4被附加地配置在建築物1 0之頂部1 7下 方。因此，建築物1 0之諸側壁1 1延伸直至超過諸氣流 引導手段1 3之諸入口 1 4處。由於諸氣流引導手段1 3位 於帶離裝置9下方之配置，使得氣流4由底部至頂部地 橫貫位於冷卻塔2中之諸熱散裝物品1 (反向流原理）。 原則上，諸氣流引導手段1 3能以水平方式延伸。然 -11 - 201211273 而，相對應於第i圖中所示者，諸氣流引導手段i3較佳 的是與水平面形成一傾斜角度P，以便使諸氣流？丨導手 段13朝冷卻塔2之主# 3向上傾斜。此傾斜角度"依 需要被決定。此傾斜角度β較佳的是可被選擇成使其大 致與散裝物品角度α相對應。具體而t，傾斜角度ρ應 介於20。與4 5。間。介於28。與40。間之值尤其較佳。 原則上，可在諸氣流引導手段丨3中之多個任意點處 设置出口 1 5。然而，較佳的是，對應於第2圖所示者， 此諸出口 1 5被專屬地配置在諸氣流引導手段L 3之底部 表面上。具體而言，如第2圖所示者，此諸氣流引導手 段1 3在其整個底部表面上可為敞開的。在此情形中，諸 氣流引導手段1 3較佳的是具有兩個側面區域1 8及〜頂 部區域1 9。諸側面區域} 8大致呈垂直地延伸。頂部區 域1 9則橋接諸側面區域1 8。頂部區域1 9較佳的是具有 一倒“V”形之戴面。 諸氣流引導手段1 3可終止於冷卻塔2之主軸3的前 方。然而’此諸氣流引導手段i 3較佳的是延伸直至主軸 3處（或直至一配置在冷卻塔2之主軸3區域中的r轂部」 2 0 處）。 當冷卻塔2被配置在建築物1〇内部時’移除裝置7 通常也被配置在建築物1 〇之内部。因此’被從冷卻塔2 處所移除之諸散裝物品1 (仍然）如最初地被置於建築物 1 〇之内部。因此，在此情形中，此冷卻設備具有一裝置， 而被從冷卻塔2處所移除之諸散裝物品1則藉此裝置被 ▼離建築物1 0。此裝置較佳地被實施成一如第3圖中所 -12- 201211273 示之連續式輸送裝置21。 尤其是在送氣裝置8成一風扇型式之情 流4因此在一開始時被吹至建築物10内，炎 14而僅從該處被引導至諸氣流引導手段13 式輸送裝置21可從建築物10露出，並立存 物10 ’而在連續式輸送裝置21中之諸通道1 對被岔封。為達成此目的，如第3圖中所承 輪送裝置21可具有多個槽狀容器23。當相 向X橫向觀看時，此諸容器23具有一如第4 器戴面。當朝輸送方向X觀看時，此諸容器 3圖所示之長度1 ^例如，連續式輸送裝置 貫施成一種所謂之輸送機，其包括多個具有 波狀側壁。 讓多個連續輸送機裝置21(更精確而言 23)得以藉由從建築物處露出並進入建築 區域22，其較佳的是被實施成隧道。此諸 道）22具有一可順應該容器截面之截面，如】 在適當處’多個密封唇或類似者可被配置名 側面。當朝輪送方向X觀看時，諸隧道2 2名 亦具有一隊道長度L，其係大於容器長度厂 較佳的是’甚至其長度至少係容器長度I纪 大約2·5至3·5倍長。 本發明具有許多優點。尤其是，可較高 位於冷卻塔2中之諸熱散裝物品丨。此外， 中所請求之冷卻設備僅具有很少之機械組件 形中，當氣 藉由諸入口 内時，連續 度進入建築 1域22應相 ，此連續式 對於輸送方 圖所示之容 具有一如第 2 1因此可被 交又通道之 :多個容器 物1 0内通道 通道區域（隧 胃4圖所示。 :邊隨道壁之 :各種情形下 ’隧道長度L 1兩倍，例如 效率地冷卻 由於本發明 。因此，在 -13- 201211273 其生產成本及維護兩方面皆優於習知之系統。除此之 外，本發明所需之冷卻空氣量小於先前技藝。因此，送 氣裝置8之尺寸相較於習知冷卻設備之尺寸要小。任何 隨後被連接至帶離裝置9上的清潔與除塵裝置在尺寸上 亦可被設計成較小於先前技藝者。以上為專門用以說明 本發明之敘述。對照本發明之保護範圍，將獨有地藉由 所附申請專利範圍而決定。 【圖式簡單說明】 第1圖顯示一可供熱散裝物品用之冷卻設備， 第2圖顯示一氣流引導手段之剖面圖， 第3圖顯示一連續式輸送裝置之側視圖，及 第4圖顯示一具有槽形容器之通道區域的剖面圖。 【主要元件符號說明】 1 熱散裝物品 2 冷卻塔 3 主軸 4 氣流 5 供應裝置 6 塔外壁 7 移除裝置 8 送氣裝置 9 帶離裝置 10 建築物 11 側壁 12 上表面 -14- 201211273 13 氣 流 引 導 手 段 14 入 口 15 出 σ 16 中 央 區 域 17 頂 部 18 側 面 區 域 19 頂 部 域 20 轂 部 21 連 續 式 *»/ 达 裝置 22 通 道 區 域 23 容 器 α 散 裝 物 品 角 度 β 傾 斜 角 度 h/H 向 度 1/L 長 度 η 速 度 r/R 半 徑 X ¥m 送 方 向 -15-201211273 VI. Description of the Invention: [Technical Field to Which the Invention Is Alonged] The present invention relates to a cooling device for a heat-dissipating article. [Prior Art] Attempts to utilize waste heat generated at the same time as efficiently when cooling hot bulk items (e.g., sintered iron ore). A reflow heat exchanger of the type of a circular downhole heat exchanger or a circular scraped surface heat exchanger is a prior art. However, in the case of a circular downhole heat exchanger, as the exhaust gas temperature continues to decrease, waste heat recovery will be limited to the first third of the heat exchanger. In the case of a circular scraped surface heat exchanger, there is a mixture of heat and warm exhaust gas, but the temperature is substantially impossible to reach the highest temperature, so that the efficiency of waste heat recovery is also lowered. SUMMARY OF THE INVENTION The object of the present invention is to create a lot of feasibility by utilizing the heat generated during the cooling of the heat-dissipating articles to create a lot of feasibility. The purpose of this invention is as follows: The hot bulk items of the features described in the item are achieved with a cooling device. Other advantageous developments of the cooling equipment requested in the present invention are the purpose of applying for the scope of the subsidiary items 2 to 9 of the patent application. A heat bulk item is developed such that the cooling apparatus includes a bulk item in which the cooling tower cooling apparatus will have a vertical spindle cooling tower as claimed in the present invention, and the heat is Cooling, 201211273 - the cooling device has a supply device' and the hot bulk items are poured into the cooling tower from above by means of the supply device, so that the heat bulk items can be stacked in the cooling tower - the cooling device has a device is removed, and the bulk items in the cold state are removed from the bottom of the cooling tower by the removing device, so that the bulk items remaining in the cooling tower can slide downward, thereby cooling The device has a gas supply device, and the gas flow is transported through the cooling tower by the gas supply device. The cooling device has a belt-off device, and the air flow is carried away from the cooling tower by the belt-off device, and a plurality of air flow guiding means are configured. In the cooling tower, the airflow guiding means extend radially inward from the plurality of inlets disposed in the outer wall of the tower to the main shaft, and the airflow guiding means are Providing an elongated guide means having a plurality of outlets for the supply of air in its length as viewed in the respective extension directions, so that the air flow can be introduced into the heat-dissipating articles located in the cooling tower, When viewed in the direction of the main shaft, the airflow guiding means are disposed in the central region of the "p?, and the belt-off device is disposed in the upper region of the cooling tower such that the airflow traverses from bottom to top Hot bulk items in this cooling tower. The development lies in the fact that the airflow does not flow in the opposite direction but in the reverse flow. Therefore, it is impossible to mix hot and warm exhaust gases. The cornering of the horns, the airflow guiding means form a tilt relative to the horizontal so that the airflow guiding means can be tilted upward to the main axis. This 201211273 development further optimizes the efficiency of the waste m wall # & Therefore, if the inclination angle is selected to be approximately the same as the fineness of the article, the angle of the article is particularly high; the dispersion formed with respect to the level is between 20 and 45. Therefore, the angle of inclination is preferably The ground system 且] and most of the cases are between 25. Pan 35. Between 0 ', car {疋, the exits are uniquely arranged in the airflow guiding means. This development is achieved: the risk of blocking the outlets is Minimized and even completely avoided. "Distribute the outlets exclusively on the surface below the airflow guiding means: by achieving, for example, in each case with two side zones f and one The airflow guiding hand #bridged to the top region of the side regions is again substantially a vertically extending side region, and a top region having a worn-out shape. Preferably, the airflow guiding means extends up to the main shaft or up to a hub disposed on the main shaft. This is achieved by the fact that the hot bulk items are actually traversed and cooled by the air flow over the entire cross section of the cooling tower. Preferably, the strapping device is disposed in the outer wall of the tower. This development is being achieved. The supply can be designed without the need to consider the development of the strip device. In a preferred development of the invention, the supply means is in the form of a rotating guide channel. This development has resulted in a better distribution of hot bulk items across the cross-sectional area of the cooling tower. Preferably, the cooling device is developed such that: - the cooling tower is arranged in a building, and the side walls of the building extend from the bottom of 201211273 up to above the inlets, the removal device being arranged in the building The inside of the object, so that the bulk items removed from the cooling tower are placed inside the building. - The cold heading device has a continuous conveying device, and the bulk items removed from the cooling tower can be borrowed The continuous conveying device is thus carried away from the building, the continuous conveying device having a plurality of trough-like containers having a container cross-section when viewed transversely with respect to the conveying direction and having a viewing direction when viewed in this conveying direction A container length, the containers are exposed from the raft building and into the building via two passage areas that are implemented in the form of tunnels, and the cross-sections of the channels conform to the cross-section of the container, as they are directed toward the lanes. When viewed, each has a tunnel length greater than the length of the container. This development is particularly advantageous when the air supply device is implemented as a fan. This fan is designed to minimize leakage losses from the gas stream. Other advantages and details can be derived from the description of the following non-limiting embodiments and the accompanying drawings. [Embodiment] The cooling device of the product 1 (e.g., the small vertical main shaft 34 is cooled and used to cool the heat dispersive I particles/sintered iron ore) as shown in Fig. 1 has a cold tower 2 equipped. The heat-dissipating articles 1 are in the cooling tower 2. Item This is 1 means that the cooling device has a supply device 5. The heat shares are poured into the cooling tower 2 from above by the supply means 5, and the heat-dissipating articles 1 are deposited in the cooling tower 2. 201211273 Corresponding to that shown in Fig. 1, the supply device 5 can be implemented as a rotary guide that rotates at a predetermined speed η. The speed η is usually quite low. For example, if the supply device 5 is developed into a rotary guide, the catch η can be in the range of 0.25 rev/min (rev/min) to 1 rev/min. The design of a rotating guide means that the heat-dissipating articles 1 are preferably distributed over the (horizontal) cross section of the cooling tower 2. However, the effective radius r of the heat-dissipating articles 1 which may be distributed by the supply means 5 is generally significantly smaller than the radius R of the cooling tower 2. Specifically, the effective radius r of the heat-dissipating articles 1 distributed by the supply device 5 is at most 30% of the radius R of the cooling tower 2. In most cases, the value is even between 10% and 25%. Therefore, a cone is formed near the outer wall 6 of the tower (i.e., the vertical or substantially vertical wall of the cooling tower 2). This tip has a typical bulk item angle a. Typically, this bulk item angle α (depending on the bulk item 1) is between about 30. With about 3 of 8. between. ^ In addition, this cooling device has a removal device 7. The bulk items ^ are removed from the bottom of the cooling tower 2 by means of the removal device 7. This means that the bulk items 1 remaining in the cooling tower 2 will slide downwards. ^ The removal device 7 can be implemented as a push table that can be moved in a circular manner. This cooling device also has a gas supply device 8. The gas stream 4 is conveyed through the cooling tower 2 via the gas unit 8. Air supply _ 8 & implement - fan. However, in principle, it can also become a good one. 4 By means of this, the cooling device also has a belt-off device 9. The gas and permeation device 9 is carried away from the cooling tower 2. When the bulk items 1 are supplied to the cooling tray 2, the article is hot. At this time, the typical temperature reaches 9 〇〇〇C.备诀 also ~ Tianzheng political article 1 from 201211273 When the cooling tower 2 was removed, the temperature of the second system was 7〇. . As for the item, it is (quite) cold. At this point, it is typical to flow through between Av:c. The cold air of the hot bulk items 1 is executed with a cold air flow of 2:2. Therefore, in Tower 2, and in the state of ^, 'the degree of the temple is usually around the surrounding temperature, it is led to the state of cold ',,, (the temperature is usually between 6 〇〇. (: 1 800 oe) self-cooling The tower 2 is taken away. The cooling tower 2 is usually arranged in a building 1 〇 with a plurality of side walls 中, in the middle of the building tower 2 - the middle high U 11 extends from the bottom # to the cooling of a Gulu μ Λ Λ. Usually, relative to the entire cooling tower 2 ... 'this intermediate height h is between: Η 40. /. and 〇 。 。 整个 整个 整个 整个 整个If the device is inside the building (four), the lack of, "through" a fan can be used to be the outer 10 of the HM k-hole device 8 is usually configured outside the building 4. The device 9 is matched, and therefore It is applied to the upper portion U of the cold tower 2 and is outside the table 10. The π separation device 9 can be disposed on the upper surface 12 of the cold separation device 9. In the outer wall 6 of the tower, that is, on the side, a plurality of airflow guiding means 丨3, on the side, the airflow bowing guide j3 is most placed in the cold clock %2. Principle This embodiment There are at least ~', the quantity is two. However, the actual number of guiding means u is 原则x in principle, 'gas will exceed 4 。. + 糸..., limited. However, usually the quantity is not in the quantity Between 8 and 16. The medium-rolling and guiding means 丨3 of the oxygen flow guiding means 1 3 be careful to "," the shape guiding hand ρ. This, & as shown in Figure 1 is slender and this blocking means has The inlet is placed at the inlet of the outer wall 6 of the tower-10-201211273 14. From here the inlets 14, the airflow guiding means 13 extend radially inwardly to the main shaft 3 of the cooling tower 2. The development of the airflow guiding means 13 For example, it may be spoke-shaped (as shown), crescent, etc. Other developments are also possible. The only important factor is that the distance from the main shaft 3 of the cooling tower 2 must be along the longitudinal direction of the airflow guiding means. Extending and decreasing. The air guiding means 13 (on their length when viewed from their respective extension directions) have an outlet 15 for the air flow 4. The air flow 4 (at the still cold moment) by the entrances 1 4 is introduced into the airflow guiding means 13 and by the outlets 15 The portion is directed into the heat-dissipating articles located in the cooling tower 2. The cross-section of the airflow guiding means 13 can be constant when viewed from its length. However, the cross-section of the airflow guiding means 13 is preferably preferably It is reduced toward the main shaft 3 of the cooling tower 2, corresponding to Fig. 1. When viewed from the direction of the main shaft 3 of the cooling tower 2, the air flow guiding means 13 are disposed in the central region 16 of the cooling tower 2. The central region 16 extends from approximately 30% of the entire height Η of the cooling tower 2 to approximately 70% of the entire height Η of the cooling tower 2. However, irrespective of the precise configuration of the airflow guiding means 13, this is The airflow guiding means 13 are disposed below the belt separating device 9. When the cooling tower 2 is disposed in the building 10, the inlets 14 are additionally disposed below the top 17 of the building 10. Therefore, the side walls 11 of the building 10 extend beyond the inlets 14 of the air guiding means 1 3 . Due to the arrangement of the air flow guiding means 13 under the stripping means 9, the air stream 4 traverses the heat-dissipating articles 1 (reverse flow principle) located in the cooling tower 2 from the bottom to the top. In principle, the airflow guiding means 13 can extend in a horizontal manner. However, -11 - 201211273, corresponding to those shown in Fig. i, the airflow guiding means i3 preferably form an oblique angle P with the horizontal plane so as to make the airflows? The guide 13 is tilted upward toward the main #3 of the cooling tower 2. This tilt angle is determined as needed. Preferably, the angle of inclination β can be selected such that it generally corresponds to the angle α of the bulk item. Specifically, t, the tilt angle ρ should be between 20. With 4 5 . between. Between 28. With 40. The value between them is especially preferred. In principle, the outlet 15 can be arranged at any of a number of points in the air flow guiding means 丨3. Preferably, however, the outlets 15 are exclusively disposed on the bottom surface of the airflow guiding means L3, as shown in Fig. 2. Specifically, as shown in Fig. 2, the airflow guiding means 13 may be open on the entire bottom surface thereof. In this case, the air flow guiding means 13 preferably has two side areas 18 and a top area 19. The side regions 8 extend substantially vertically. The top area 1 9 bridges the side areas 18 . The top region 119 preferably has an inverted "V" shaped face. The air flow guiding means 13 may terminate in front of the main shaft 3 of the cooling tower 2. However, the air flow guiding means i 3 preferably extends up to the main shaft 3 (or up to a r hub portion disposed in the main shaft 3 region of the cooling tower 2) 20). When the cooling tower 2 is disposed inside the building 1', the removal device 7 is also usually disposed inside the building 1 . Therefore, the bulk items 1 (still) removed from the cooling tower 2 are initially placed inside the building 1 . Therefore, in this case, the cooling device has a device, and the bulk items 1 removed from the cooling tower 2 are thereby ▼ are taken away from the building 10. This device is preferably implemented as a continuous conveyor 21 as shown in Figure 3, -12-201211273. In particular, the airflow device 8 is formed into a fan-type flow 4 so as to be blown into the building 10 at the beginning, the fire 14 is only guided from there to the airflow guiding means 13 and the transporting device 21 can be taken from the building 10 The channels 1 are exposed and stacked 10' and the channels 1 in the continuous conveyor 21 are sealed. To achieve this, the transfer device 21 as in Fig. 3 can have a plurality of trough-like containers 23. The containers 23 have a fourth wearing surface as viewed in the lateral direction of the X. The length of the containers 3 as viewed in the conveying direction X is, for example, a continuous conveying device which is applied as a so-called conveyor comprising a plurality of corrugated side walls. A plurality of continuous conveyor devices 21 (more precisely 23) are allowed to be tunneled by being exposed from the building and into the building area 22. The passages 22 have a cross section that conforms to the cross section of the container, such as where appropriate, a plurality of sealing lips or the like may be assigned to the side of the name. When viewed in the direction of the transport X, the tunnels 22 also have a team length L, which is greater than the length of the container. The preferred one is even 'even its length is at least the length of the container I. about 2. 5 to 3. 5 Double. The invention has many advantages. In particular, the hot bulk items located in the cooling tower 2 can be higher. In addition, the cooling device requested therein has only a few mechanical component shapes. When the gas is passed through the inlets, the continuity enters the building 1 domain 22, and the continuous mode has one for the capacity shown in the conveying diagram. As in the 21st, it can be handed over to the channel: a plurality of containers in the channel channel area (shown in Figure 4 of the tunnel): edge-to-wall: in each case, the tunnel length L 1 is twice, such as efficiency Ground cooling is due to the present invention. Therefore, both the production cost and the maintenance are superior to the conventional system in the period of -13 to 201211273. In addition, the amount of cooling air required by the present invention is smaller than that of the prior art. Therefore, the air supply device 8 The size is smaller than that of the conventional cooling device. Any cleaning and dust removal device that is subsequently attached to the tape removal device 9 can also be designed to be smaller in size than the prior art. The scope of the invention will be determined solely by the scope of the appended claims. [Fig. 1 shows a cooling device for hot bulk items, Fig. 2 shows A cross-sectional view showing a flow guiding means, Fig. 3 shows a side view of a continuous conveying device, and Fig. 4 shows a sectional view of a passage area having a grooved container. [Main component symbol description] 1 Hot bulk item 2 Cooling tower 3 Spindle 4 Airflow 5 Supply device 6 Tower outer wall 7 Removal device 8 Air supply device 9 With device 10 Building 11 Side wall 12 Upper surface-14- 201211273 13 Airflow guidance 14 Entrance 15 Out σ 16 Central area 17 Top 18 Side area 19 Top field 20 Hub 21 Continuous *»/ Up to 22 Channel area 23 Container α Bulk item angle β Tilt angle h/H Dimension 1/L Length η Speed r/R Radius X ¥m Send direction -15 -