201030137 六、發明說明： 本發明係關於一種用於複數「熱回收」式煉焦爐室的 循環運作之方法，這些煉焦爐室（coke 〇ven chamber)形成一 部份的煉焦爐庫（coke oven bank)，該運作特別關於「填充 —煉焦一推進」的循環階段，且推進的程序係用以決定該 :環的配置方式，致使運用「熱回收」過程產生蒸汽與能 里而製造熱煉焦氣體能夠被均勻分佈於整個煉焦過程的時 間均數（temporal mean)上，因此能大幅增進蒸氣與能量的產 生，且特別增進位於煉焦過程下游的電氣能量之產生。 在煤炭的碳化過程（carb〇nizatj〇n)中，碳化過程中所散 發出來的煉焦氣體可藉由不同方式加以利用。在一些設計 類型中，捕捉並利用煉焦氣體，以回收並利用其中所含的 有用物質，例如：芳香族碳氫化合物、氫氣、氨、及甲烷。 在其他的設計類型中，煉焦氣體被用來燃燒，藉此產生熱 能，而此熱能被用於煤炭碳化過程中。藉由這些設計類型， 可以在燃燒及利用所產生的熱能之後將煉焦氣體排放到環 境中而沒有任何再次利用，這些設計類型被稱之為「非回 收J式煉焦爐；其他的設計類型中利用廢熱以回收其蒸氣， 此蒸氣例如可以被用來產生電氣能量，而此種設計類型則 被稱之為「熱回收」式煉焦爐。 基本上，煉焦爐的配置方式乃是將6個到34個之間的 煉焦爐聚集成一組，且彼此連結於—個主要單元内，此主 要單元亦被稱之為一煉焦爐庫。以此方式，可以使焦煤的 生產變得均勻化（h〇mogenized)。由於必須填充多個煉焦爐 201030137 至以持續生產過程，所以藉由形成幾組的煉焦爐室，就可 以顯著簡化填充步驟並達到自動化，其原因在於煤炭的碳 化過程是以「填充一煉焦—推進」的循環階段而實施；當 煉焦循環仍停留在一些煉焦爐室内時，可以填充或推進其 他的煉焦爐室。以此方式，也能夠使燃燒氣體產生固定的 輸出量。藉由裝填一焦煤淬火車，在煉焦爐室相反側上的 煉焦爐室外部完成焦煤推進。在爐組合的專有名稱中，上 ❺述所運用的方法中幾個「非回收」式《「熱回收」式的煉 <、’、爐之組〇被稱之為「爐庫（〇ven bank)」。相反地，多個習 知煉焦爐的組合則被稱之為「爐群（〇venbaUery)」。 WO 2006/128612 A1揭示一種藉由燃燒煉焦氣體而在 煉焦爐内碳化焦煤之方法，煉焦氣體起初流入焦煤塊（c〇ke cake)上方的一氣體空間内，而在該空間内藉由提供低於化 學备量體積的燃燒空氣而使煉焦氣體產生局部燃燒，此過 程被稱之為主要燃燒（primary e〇mbustj〇n)，它利用所謂的 ❿主要燃燒空氣進行燃燒。然:後，局部燃燒過的煉焦氣體則 透過所謂的下降管通道（d〇WnC〇mer channel)而被運送至一 第二加熱空間’在該空間内藉由提供其他量的燃燒空氣而 使煉焦氣體完全燃燒。此過程被稱之為二次燃燒(secondary combustion)，b利用所謂的第二燃燒空氣進行燃燒。藉此， 焦煤塊的下邛區段亦被加熱，因而增進焦煤品質。本發明 主張一種裝置及方法，用以使主要燃燒空氣能夠均勾地供 應至焦煤塊上方的氣體空間内，致使焦煤塊的上部區段中 的熱分佈能夠均勻化，因而獲得較佳的焦煤製品。本發明 5 201030137 可同樣運用於「非回收」式或「熱回收」式的煉焦爐。 US 5968320 A揭示一種「熱回收」式煉焦爐，其中從 煉焦爐排出原生的煉焦氣體，而且此煉焦氣體在一鍋爐系 統中燃燒以產生熱能與電力。原生的煉焦氣體經喷灑之 後，以藉由一沖洗溶劑進行清洗，且在一燃燒爐内進行燃 燒，藉此產生蒸汽與機械能量，接著利用上述能量而產生 電能。為了促進燃燒且避免壓縮機與測量裝置等昂貴的設 備，藉由在燃燒室下游安裝一吸風機，而在燃燒室内產生 股負壓。藉由此裝置，在上述煉焦爐的運作中由煤炭碳 化過程產生廢氣的不均勻結果也能夠被均勻化。但是就整 個煤炭碳化的過程看來’均勻化仍不完全。 上述的多種系統利用來自煤炭碳化及後續的燃燒過程 所產生的熱能，以回收蒸氣與能量，但是他們的缺點在於： 時間均數的熱燃燒亂體的輸出量必須幾乎完全一致，以碟 保均勻地供應燃燒氣體到鍋爐上，而在鍋爐内可以從煤炭 碳化所排出的熱能中產生蒸氣。必須供應份量最均勻的燃 燒氣體到這些鍋爐内，以確保渦輪肩及其下游的從動裝置 能獲得最佳運作。 就整個煉焦循環來看，從單一煉焦爐室排出的燃燒氣 體之輸出量並非固定一致。已知在起初百分之二十的煉焦 過程期間’釋放出最大量的粗煤a，此份量在煤炭碳化的 過程中將強烈減少。在煉焦爐室的一個煉焦循環期間所測 量到的熱燃燒氣體之典型份量係顯示於圖丨内以作為範 J假如一個煉焦爐庫内的所有煉焦爐室在很短的時間内 201030137 連續運作的話（㈣：被推進且被填充），則位於其下游處的 對應鋼爐在過度供應熱煙氣的時候將會超載，因而鋼爐將 無法在其最佳的工作範圍内繼綠^ 间α繼續運作。因此，亟需建構出 一種用於煉焦爐的控制方案， 系致使在整個運作期間，每次 一個鍋爐僅配合一個煉焦爐運作。201030137 VI. INSTRUCTIONS: The present invention relates to a method for recycling a plurality of "heat recovery" type coke oven chambers, which form a part of a coke oven bank (coke oven bank) The operation is particularly related to the cycle of "filling-coking-advancing", and the process of advancing is used to determine the arrangement of the rings, so that the use of the "heat recovery" process to generate steam and energy can produce hot coking gas. It is evenly distributed over the temporal mean of the entire coking process, thus greatly increasing the generation of steam and energy, and in particular increasing the generation of electrical energy downstream of the coking process. In the carbonization process of coal (carb〇nizatj〇n), the coking gas emitted during the carbonization process can be utilized in different ways. In some design types, coking gas is captured and utilized to recover and utilize useful materials contained therein, such as aromatic hydrocarbons, hydrogen, ammonia, and methane. In other design types, coking gas is used to burn, thereby generating thermal energy that is used in the carbonization process of coal. With these design types, the coking gas can be discharged into the environment after combustion and utilization of the generated heat without any reuse. These design types are called “non-recycled J-type coke ovens; other design types are utilized. Waste heat is used to recover its vapor, which can be used, for example, to generate electrical energy, and this type of design is referred to as a "heat recovery" type coke oven. Basically, the coke oven is configured by agglomerating between 6 and 34 coke ovens and connected to each other in a main unit, also referred to as a coke oven bank. In this way, the production of coking coal can be homogenized. Since it is necessary to fill multiple coke ovens 201030137 to continue the production process, by forming several sets of coke oven chambers, the filling step can be significantly simplified and automated, because the carbonization process of coal is "filling a coking-propulsion" It is implemented in the cycle phase; when the coking cycle is still in some coke oven chambers, other coke oven chambers can be filled or propelled. In this way, it is also possible to produce a fixed output of the combustion gases. Coking coal propulsion is completed outside the coke oven on the opposite side of the coke oven chamber by loading a coke quench train. In the exclusive name of the furnace combination, several "non-recycling" types of "heat recovery" type "refining", "furnace group" are referred to as "furnace library". Ven bank)". Conversely, the combination of a plurality of conventional coke ovens is referred to as "〇 venbaUery". WO 2006/128612 A1 discloses a method for carbonizing coking coal in a coke oven by burning coking gas, which initially flows into a gas space above a coke cake, and provides low in the space Partial combustion of the coking gas is produced by chemically preparing a volume of combustion air. This process is called primary combustion, which uses the so-called primary combustion air to burn. After that, the locally burned coke gas is transported to a second heating space through a so-called downcomer channel (in the space to make coking by providing other amounts of combustion air) The gas is completely burned. This process is called secondary combustion, and b uses the so-called second combustion air for combustion. Thereby, the crotch section of the coking coal block is also heated, thereby improving the quality of coking coal. The present invention claims an apparatus and method for enabling the main combustion air to be uniformly supplied to the gas space above the coking coal block, so that the heat distribution in the upper section of the coking coal block can be homogenized, thereby obtaining a better coking coal product. . The present invention 5 201030137 can be equally applied to a "non-recycling" type or "heat recovery" type coke oven. No. 5,968,320 A discloses a "heat recovery" type coke oven in which a raw coke gas is discharged from a coke oven and this coke gas is combusted in a boiler system to generate heat and electricity. The primary coke gas is sprayed, washed with a flushing solvent, and burned in a furnace to generate steam and mechanical energy, which is then used to generate electrical energy. In order to promote combustion and avoid expensive equipment such as a compressor and a measuring device, a negative pressure is generated in the combustion chamber by installing a suction fan downstream of the combustion chamber. By this means, the unevenness of the exhaust gas generated by the coal carbonization process in the operation of the above coke oven can be uniformized. However, as far as the whole process of carbonization of coal is concerned, the homogenization is still incomplete. The various systems described above utilize thermal energy from coal carbonization and subsequent combustion processes to recover steam and energy, but their disadvantages are: The time-averaged heat-burning volume must be almost identical in output to ensure uniform disk The combustion gas is supplied to the boiler, and in the boiler, steam can be generated from the heat energy discharged from the carbonization of the coal. The most uniform amount of combustion gas must be supplied to these boilers to ensure optimum operation of the turbine shoulder and its downstream followers. As far as the entire coking cycle is concerned, the output of the combustion gas discharged from the single coke oven chamber is not fixed. It is known that during the initial 20% coking process, the maximum amount of crude coal a is released, which will be strongly reduced during the carbonization of coal. The typical portion of the hot combustion gases measured during a coking cycle in the coke oven chamber is shown in Figure 假 as a standard J. If all the coke oven chambers in a coke oven are operated continuously in 201030137 in a short period of time. ((4): being pushed and filled), the corresponding steel furnace located downstream of it will be overloaded when excessively supplying hot flue gas, so the steel furnace will not be able to continue in the best working range. Operation. Therefore, there is an urgent need to construct a control scheme for a coke oven that allows one boiler to operate with only one coke oven each time during the entire operation.
可透過改變循環次數而以簡單方式實行燃燒氣體的份 篁控制；基於成本考量，最好不要在中間設置多個用於敎 燃燒氣體的儲存槽或累積裝置。接著，僅能夠藉由精確控 制接近煉錢室的時間順序而改變循環次數。根據習知的 水平式煉焦至技術’這樣的控制方案之順序被稱之為「推 進排程（pushing schedlUe)」，其亦藉由焦煤充填程序的時間 及練焦爐機器的最大行進速“決定。精料畫過的推進 排程能夠錢燃燒氣體的流動達到簡單均句化。 因此，本發明之目的是要提出一種簡單的製程與方 法藉& &變循環次數或推進排冑而控制燃《氣體的份 量。可以理解的是，燃燒氣體係用以涵蓋完全燃燒且從煉 焦爐室流出的氣體。但是，假如在後續的輔助設備或鍋爐 内破燃燒的話’這些氣體也可以是局部燃燒的煉焦氣體。 為凡成上述任務，本發明提出一種結合特定數量的「熱 回收」式煉焦爐室而形成煉焦爐庫之裝置，且提出一種方 〇 此夠以精破決定的順序控制並接近這些煉焦爐室以 進行焦煤推進。由於所謂的「填充—煉焦—推進」循環終 於推進循環，所以在此推進循環的盡頭控制個別煉焦爐 的整個循環。也能夠暫時接近個別的煉焦爐室，致使在沒 201030137 有產生燃燒氣體的情形下所執行的填充與推進程序之時間 内分佈於所有的煉焦爐庫及所有的煉焦爐室。然後，在煉 焦循環持續地產生熱燃燒氣體。由於精確控制所有 煉焦爐庫及煉焦爐室㈣間分冑，使歸氣的產生變得均 勻化，因而不再需要例如氣體儲存器、管路轉換器、或中 間儲存槽等控制設備。 為了實施本發明的裝置，多個煉焦爐室亦被建構成一 個穩固連結的空間整體結構而形成煉焦爐庫，可以利用偶 ^或奇數個煉焦爐室而完成此空間整體結構’連桿被認為 是煉焦爐室的結構性包圍物’但其可以具有任何隨意的结 構，其周圍可以具有磚塊結構或保護罩，但是也可以具有 「中間壁體。「推進循環」__詞被認為是指煉焦循環中的 推進與填充」兩個部份。較佳地煤炭不要預先加熱且 直接填充到先前的煉焦猶環所預熱的煉焦爐内。 近所^:的[可以藉由一填充機及一推進機而控制接 有的煉焦爐室，致使能夠n纟一 推逸以η |關㈣。機15而實施填充與 上，填充機總是與一淬火車組合在一 ^卒火車可控制地接近欲填充的開口以便進行推進 ^二地，此推進程序的實施方式是從正面前端側的煉隹爐 =始執行填充程序，同時從正面後端側的煉焦爐室開1 :推進程序。以此方式，可以使個別循環達到 有時間有關但並未遲鈍的表現。 鍋爐。例如，假如煉焦爐包含十個煉焦爐 201030137 2的Ί整個單元包含五個錦爐，這些鑛爐被用來產生 Ά與月b量’而且’來自煉焦爐庫的熱煉焦氣體被供應至 這些鍋爐内。這一點可 應至 ’、 透過B路而達成，此管路透過一 收集裝置而連結至個別的煉焦爐室。 -種用於填充個別煉焦爐室的控制方式乃是如下 初僅接近個別煉焦爐庫内的一個煉焦爐室而已，例如，這 疋煉焦爐庫的第-個煉焦爐室。為了使填充過程在整個時 間過程上分佈得越均勾趟招： ❹ Γ 接近第—個隸爐庫的第 -個煉焦爐室之後’則接近下二個（第三個）煉焦爐庫中的一 個煉焦爐室。這樣具有以下優點，因為另-個鍋爐(第二號 鋼爐）係連結至第三個煉焦爐庫，藉此避免額外的最大體積 流，此額外的體積流可能會使燃燒氣體不均句地供應至銷 爐内。此動作應用於每下二個煉焦爐庫的第一個煉焦爐室 之所有煉焦爐室，直到已經填充並推進倒數第二個練焦爐 庫的第一個煉焦爐室為止，這些程序代表第一推進循環。 G 帛著進行其他的推進循環，以填充並推進其他的煉焦 爐室。然後’這些煉焦爐室將作為下一個練焦爐庫的下一 個煉焦爐室。以此方式，可利用控制方式接近第二個及每 下一個煉焦爐室的第二個煉焦爐室，直到已經接近最後一 個煉焦爐庫的第二個煉焦爐室為止。在下一個推進循環 中，推進並填充此一連串煉焦爐庫中的後續煉焦爐庫。例 如，這些是第一個及每下二個煉焦爐庫的第三個煉焦爐室。 接近個別煉焦爐室的控制方案亦與煉焦爐庫内的溫度 梯度有關。由於煤炭填充程序起初會使煉焦爐内產生溫度 9 201030137 下降，因此對於個別煉焦爐y的1]定熱量預算來說，相鄰 的煉焦爐y+1肖W並未立刻進行運作，而是與煉焦爐y 相隔幾個小時之後才開始進行運作，如此一來，能使整個 練焦爐庫的區段產生溫度下降；可以選擇填充循環，致使 相鄰的煉焦爐y+Ι與y-l僅能在至少24個小時之後進行運 作。 假如除了最後幾個之外，所有的煉焦爐室均已經推進 並填充好了的話，第-個及每下二個煉焦爐庫的最後一個 煉焦爐室的推進與填充則是在最後的循環中完成。以此方 式，在所有煉焦循環的時間均値上，可以產生非常均句的 廢熱，並將此廢熱傳遞至鍋爐設備内，致使可以非常均勾 地供應廢熱至鋼爐内。 特別地，本發明提出-種用於—連串偶數個或奇數個 「熱回收」式煉焦爐庫的循環運作之方法，而且此煉焦爐 庫具有偶數個或奇數個煉焦爐室’其中煉焦爐庫⑴特別包 含-連串至少四個「熱回收」式練焦爐室，且其中： 這些煉焦爐庫被連結至一鍋爐系統，在該鍋爐系統中 利用來自煉焦爐庫的熱廢氣之熱能以產生蒸氣，且 藉由一焦煤推進機，以精確決定的時間間隔從正面側 推進並填充煉焦爐室，而進入一煉焦爐室的相反方向，而 :在推進之後立刻實施個別練焦爐室的重新填充及另一個 重新的煉焦猶環； 其特徵在於：在第一推進循環 一換隹Μ μ # 中起初推進並填充第 ’”、、-個煉焦爐室’而且’假如每個煉焦爐庫 201030137 的煉焦爐室之數量盍^ 煉焦爐庫的第一個話二連續推進並填充下二個 二個煉攀爐庫的第 ，直到已經推進並填充倒數第 尿焦爐庫的第一個煉焦爐室為止；且 :下個推進循環時’起初推進並填充此—連隹 爐庫的下-個煉焦爐庫的下一個煉焦爐： ❹ ❹ 煉焦爐室，直到已經庫的相同 一㈣隹、推進並填充此-連串煉焦爐庫的最後 個煉“.、爐庫的相同煉焦爐室為止；且 在一後續推進循環中，推進並填充此-連串煉焦爐廑 的第-煉焦爐庫的下二個煉焦爐室’且然後以連續；序推 進f填充此一連串煉焦爐庫的下二個煉焦爐庫的相同煉焦 2爐進並填充此一連串煉焦爐庫的最後-個 煉焦爐庫的相同煉焦爐室為止；且 的第亡炊進循環中，推進並填充此-連串煉焦爐庫 第「煉焦爐庫的最後-個煉焦爐室，而且然後以連續順 序推進並填充下二個煉焦爐庫的最後-個煉焦爐室，直到 已Μ進並填充此一連串煉焦爐庫的倒數第二個練焦爐庫 的最後一個煉焦爐室為止，致使 能夠以此方式將非常均句產生的廢熱傳遞至鋼爐設傷 内’藉此可以非常均勻地供應廢熱至鍋爐内。 在一較佳實施例中，Μ明的方法可以被設計如下： ㈣於煉焦爐庫，僅存在正好一半數量的鋼爐系統，致使 這些煉焦爐庫係成對地連結至鍋爐。 推進排程2* 本發明的方法之特徵在於：「推進排程2*χ/1* 11 201030137 (x+l)/2」’其中χ代表每個煉焦爐庫的煉焦爐室之數量； 「2*x」代表在以控制方式接近時煉焦爐室的數量差異，且 它意味著在第1號煉焦爐室之後，接近第29號煉焦爐室（差 異28 = 2*14)。如上所述，這是下二個煉焦爐室的第一個煉 焦爐庫。然後，在後續的填充循環中，接近下一個煉焦爐 庫的第二個煉焦爐室，亦即，第16號煉焦爐室（差異 15 = 1 *(14+1))❶最後，在後續的推進循環中，推進第一個練 焦爐庫的第三個煉焦爐室（2”）。藉由煉焦爐室的數量為Μ 個’則推進排程被稱之為28/15/2。 〇 可以改變上述推進排程，可以使燃燒氣體蒸氣到達大 致均勻化的程度。例如：也可以實行推進排程「2*χ/ι*χ/丨」， 如此意味著： 在第一推進循環中，起初推進並填充第一煉焦爐庫的 第一個煉焦爐室，且假如每個煉焦爐庫的煉焦爐室之數量 為偶數的話’則連續推進並填充下二個煉焦爐庫的第一個 煉焦爐室’直到已經推進並填充倒數第二個練焦爐庫的第 一個煉焦爐室為止；且 ❹ 在下一個推進循環時，起初推進並填充下一個煉焦爐 庫的第-個煉焦爐室’且然後以連續順序推進並填充下二 個煉焦爐庫的第-個煉焦爐室，直到已經推進並填充最後 -個煉焦爐庫的第—個煉焦爐室為止；且 在-後續推進循環中’推進並填充此一連串煉焦爐庫 的第一煉焦爐庫的下―棚― 個煉焦爐至’且然後以連續順序推 進並填充此一連串換隹μ* 煉“、、爐庫的下二個煉焦爐庫的相同煉焦 12 201030137 爐室，直到已經推進並填充此一連串煉焦爐庫的最後_個 煉焦爐庫的下一個煉焦爐室為止；且 在一最終推進循環中，推進並填充此一連串煉焦爐庫 的下;個煉焦爐庫的最後-煉焦爐室，且然後以連續順序 推進並填充下一個煉焦爐庫的最後一個煉焦爐室，直到已 經推進與填充此-連串煉焦爐庫的最後一個煉焦爐庫的最 後一個煉焦爐室為止。 纟肖佳實施例中’纟發明#方法可以被設計如下： 相對於煉焦爐庫，僅存在正好一半數量的鋼爐系統，致使 這些煉焦爐庫係成對地連結至鍋爐。 較簡單的-運作模式為每次接近下一個煉焦爐庫的第 一個煉焦爐室，此對應的推進排程被稱之為「以/2」，此 推進排程就填充機設備開支來說大致上耗費較少；然而， ^燒氣體流的均句化也會較小。同樣地，相鄰的煉焦爐室 是以更強力的方式注入熱量，此推進排程意味著： 〇 在第一推進循環中，起初推進並填充第一煉焦爐庫的 第一個煉焦爐室，而且假如每個練焦爐庫的練焦爐室之數 量為偶數的話’則連續推進並填充下一個煉焦爐庫的第一 個煉焦爐室，直到已經推進並填充為止最後一個練焦爐庫 的第一個煉焦爐室；且 在一後續推進循環中，推進並填充此一連串練焦爐庫 的下一個煉焦爐庫的下二個煉焦爐室，且然後以連續順序 推進並填充jfcb連串煉焦爐庫的下_個練焦爐庫的相同練 焦、爐室，直到推進並填充此一連串練焦爐庫的最後一個煉 13 201030137 焦爐庫的相同煉焦爐室為止；且 ,在一最終推進循環中’推進並填充第一煉焦爐庫的最 後個煉焦爐室，且然後以連續順序推進並填充下一個練 焦爐庫的最後—個煉焦爐室，直到已經推進並填充最後一 個煉焦爐庫的最後一個煉焦爐室為止。 在一較佳實施例中，本發明的方法可以被設計如下： :對於煉焦爐庫，僅存在正好一半數量的鍋爐系統，致使 這些煉焦爐庫係成對地連結至鋼爐。 同樣地，以此方式，可以實現燃燒氣體流的均勻化。〇 運用鍋爐產生蒸氣以帶動渦輪，此推進能量可以用任 何方式加以妥善運用，較佳地，此推進能量可以被用來產 生電氣能量。為此，鍋爐系統配備有適當的裝置這些裝 置包括加熱器、鍋爐、渦輪、蒸氣分離器、轉轴、及發電 機。假如欲以不同方式運用機械能量的話，也可以設置其 他補充的裝置。 八 當通過鍋爐系統時，較佳地，廢氣被供應至一個用於 清潔氣體的裝置内，以便將焦煤製造過程中所可能引起的 © 環境污染降至最低。特別地，在氣體清潔過程中，從廢氣 中移除掉含硫的化合物’所以，此氣體清潔設備最好是— 個脫硫設備（desulphurization facility)，例如可以是一個運 用氣體吸附溶劑的氣體洗滌單元。 為了執行填充步驟，藉由一煤炭填充車，將煤炭從正 面側填充到煉焦爐室内。由於先前執行的煉焦步驟’所以 煉焦爐室内仍然很熱，因而不需要其他煤炭碳化程序。在 14 201030137 煉焦步驟開始時，&焦爐室的門是關閉的。在煉焦步驟之 後’就從煉焦爐室中移出焦煤。根據煤塊的高度、填充密 度、及煉焦爐種類而定，煉焦步驟基本上要耗費20至90 個小時。在本發明的—個較佳實施例中，係朝向煉焦爐室 的另側實施推進’而煉焦爐的另一側上 易操作的煉焦爐室門。 W +The control of the combustion gases can be carried out in a simple manner by varying the number of cycles; based on cost considerations, it is preferable not to provide a plurality of storage tanks or accumulating devices for the combustion gases in the middle. Then, the number of cycles can only be changed by precisely controlling the chronological order close to the refining room. The order of the control scheme according to the conventional horizontal coking to the technology is called "pushing schedlUe", which is also determined by the time of the coking coal filling process and the maximum traveling speed of the coke oven machine. The advancement schedule drawn by the concentrate enables the flow of the combustion gas to be simple and uniform. Therefore, the object of the present invention is to propose a simple process and method for controlling the number of cycles and pushing the drain. Burning "the amount of gas. It is understandable that the combustion gas system is used to cover the gas that is completely combusted and flows out of the coke oven chamber. However, if it is broken in subsequent auxiliary equipment or boilers, these gases may also be localized. Coking gas. For the above tasks, the present invention proposes a device for forming a coke oven bank in combination with a specific number of "heat recovery" type coke oven chambers, and proposes a method that is controlled and close in the order determined by the fine break. These coke oven chambers are used for coking coal propulsion. Since the so-called "fill-coking-propulsion" cycle ends in the propulsion cycle, the entire cycle of the individual coke ovens is controlled at the end of the propulsion cycle. It is also possible to temporarily approach individual coke oven chambers so that they are distributed to all coke oven banks and all coke oven chambers during the filling and propulsion procedures performed without the presence of combustion gases in 201030137. Then, hot combustion gases are continuously generated in the coking cycle. Since the control of all the coke ovens and the coke oven chambers (4) is precisely controlled, the generation of the home gas is homogenized, so that control devices such as gas reservoirs, pipeline converters, or intermediate storage tanks are no longer needed. In order to implement the apparatus of the present invention, a plurality of coke oven chambers are also constructed to form a solid structure of a stable connection to form a coke oven reservoir, and the entire structure of the space can be completed by using even or an odd number of coke oven chambers. It is a structural enclosure of the coke oven chamber' but it can have any random structure, and it can have a brick structure or a protective cover around it, but it can also have an "intermediate wall." "Advance cycle" __ word is considered to mean Two parts of the advancement and filling in the coking cycle. Preferably, the coal is not preheated and is directly filled into the coke oven preheated by the previous coke. Nearly: [The coke oven chamber can be controlled by a filling machine and a propeller, so that n推 can be pushed to η | off (4). The machine 15 is filled and topped, and the filling machine is always combined with a quenching train to controllably approach the opening to be filled for propulsion. The implementation of the propulsion process is from the front side of the front side. The furnace is started to perform the filling process, and the process is started from the coke oven chamber on the front rear side. In this way, individual cycles can be made to have time-related but not slow performance. boiler. For example, if the coke oven contains ten coke ovens 201030137 2, the entire unit contains five kilns, which are used to generate the amount of helium and monthly b' and the hot coking gas from the coke oven bank is supplied to these boilers. Inside. This can be achieved by ', through the B road, which is connected to the individual coke oven chambers through a collection device. The control method for filling the individual coke oven chambers is as follows: initially approaching only one coke oven chamber in the individual coke oven bank, for example, the first coke oven chamber of the coke oven bank. In order to make the filling process more evenly distributed throughout the time course: ❹ Γ close to the first coke oven chamber of the first furnace, then close to the next two (third) coke ovens A coke oven chamber. This has the advantage that another boiler (second steel furnace) is connected to the third coke oven bank, thereby avoiding an additional maximum volume flow, which may cause the combustion gas to be uneven. Supply to the furnace. This action is applied to all coke oven chambers in the first coke oven chamber of each of the next two coke oven banks until the first coke oven chamber of the penultimate coke oven reservoir has been filled and advanced. A push cycle. G Carry out other propulsion cycles to fill and propel other coke oven chambers. Then these coke oven chambers will serve as the next coke oven chamber for the next coke oven bank. In this manner, a second coke oven chamber of the second and each of the next coke oven chambers can be accessed by control until it is near the second coke oven chamber of the last coke oven bank. In the next propulsion cycle, the subsequent coke oven banks in the series of coke ovens are advanced and filled. For example, these are the third coke oven chambers for the first and every second coke oven bank. The control scheme close to the individual coke oven chambers is also related to the temperature gradient in the coke oven bank. Since the coal filling procedure initially causes the temperature in the coke oven to fall by 9 201030137, the adjacent calciner y+1 Xiao W does not operate immediately, but for the individual calorific temperature budget of the individual coke oven y. The coke oven y starts to operate after a few hours, so that the temperature of the entire coke oven reservoir can be lowered. The filling cycle can be selected so that the adjacent coke ovens y+Ι and yl can only Operate after at least 24 hours. If all the coke oven chambers have been advanced and filled except for the last few, the advancement and filling of the last coke oven chamber in the first and second coke oven banks is in the final cycle. carry out. In this way, in the time of all coking cycles, waste heat of a very uniform sentence can be generated, and this waste heat is transferred to the boiler equipment, so that waste heat can be supplied to the steel furnace in a very uniform manner. In particular, the present invention proposes a method for circulating a series of even or odd "heat recovery" type coke oven banks, and the coke oven bank has an even number or an odd number of coke oven chambers therein, wherein the coke oven The library (1) comprises in particular a series of at least four "heat recovery" type coke oven chambers, and wherein: the coke oven banks are connected to a boiler system in which the heat energy of the hot exhaust gases from the coke oven bank is utilized Producing steam, and propelling and filling the coke oven chamber from the front side at a precisely determined time interval by a coking coal propeller, entering the opposite direction of a coke oven chamber, and: implementing the individual coke oven chamber immediately after the propulsion Refilling and another re-coking loop; characterized by: initially advancing and filling the '', - coke oven chambers' in the first propulsion cycle 隹Μ μ # and 'if every coke oven bank The number of coke oven chambers in 201030137 盍^ The first two of the coke ovens are continuously propelled and filled with the next two of the two camping pits until they have been pushed and filled with the penultimate urine coke oven. The first coke oven chamber; and: the next propulsion cycle 'initial advancement and filling this—the next coke oven in the lower coke oven bank of the furnace: ❹ 炼 coke oven room, until the same library One (four) 隹, advance and fill this - the last refining of the coke oven warehouse "., the same coke oven chamber of the furnace warehouse; and in a subsequent propulsion cycle, advance and fill this - the series of coke ovens - the next two coke oven chambers of the coke oven bank' and then the same coke 2 furnace that fills the next two coke oven banks of the series of coke ovens and continuously fills the last one of the series of coke ovens In the same coke oven chamber of the coke oven, and in the first cycle of the coke oven, advance and fill the last coke oven chamber of the coke oven bank, and then advance and fill in a continuous sequence The last coke oven chamber of the next two coke ovens until the last coke oven chamber of the penultimate coke oven library of the series of coke ovens has been broken and filled, so that it can be very uniform in this way Waste heat transmission Into the steel furnace, the waste heat can be supplied to the boiler very uniformly. In a preferred embodiment, the method of the invention can be designed as follows: (4) In the coke oven warehouse, only exactly half of the steel furnace is present. The system causes these coke oven banks to be coupled to the boiler in pairs. Propulsion Schedule 2* The method of the present invention is characterized by: "Advance schedule 2*χ/1* 11 201030137 (x+l)/2"' χ represents the number of coke oven chambers in each coke oven warehouse; “2*x” represents the difference in the number of coke oven chambers when approached in a controlled manner, and it means that after No. 1 coke oven chamber, approaching No. 29 Coke oven chamber (difference 28 = 2*14). As mentioned above, this is the first coke oven bank for the next two coke oven chambers. Then, in the subsequent filling cycle, approach the second coke oven chamber of the next coke oven bank, ie, the No. 16 coke oven chamber (difference 15 = 1 * (14 + 1)) ❶ finally, in the subsequent In the propulsion cycle, advance the third coke oven chamber (2") of the first coke oven bank. The number of coke oven chambers is Μ ', then the propulsion schedule is called 28/15/2. The above-mentioned propulsion schedule can be changed to make the combustion gas vapor reach a substantially uniform level. For example, the propulsion schedule "2*χ/ι*χ/丨" can also be implemented, which means: In the first propulsion cycle, Initially propelling and filling the first coke oven chamber of the first coke oven bank, and if the number of coke oven chambers in each coke oven bank is an even number, then continuously propelling and filling the first coking oven of the next two coke oven banks The furnace chamber 'until the first coke oven chamber of the penultimate coke oven reservoir has been advanced and filled; and the first coke oven chamber of the next coke oven reservoir is initially propelled and filled in the next propulsion cycle' And then advance and fill the next two coke ovens in sequential order The first coke oven chamber until the first coke oven chamber of the last coke oven bank has been advanced and filled; and in the subsequent propulsion cycle, the first coke oven bank that advances and fills the series of coke ovens The lower - shed - a coke oven to 'and then in a sequential order to advance and fill the series of 隹 * 炼,, the same coke 12 of the furnace coke oven 12 201030137 furnace chamber, until has been advanced and filled The next coke oven chamber of the last coke oven bank of the series of coke ovens; and in a final propulsion cycle, advancing and filling the bottom of the series of coke ovens; the final coke oven chamber of the coke oven bank, And then proceeding and filling the last coke oven chamber of the next coke oven bank in a sequential sequence until the last coke oven chamber of the last coke oven bank that has been filled with this series of coke ovens has been advanced. In the example, the '纟发明# method can be designed as follows: Compared to the coke oven bank, there are only exactly half the number of steel furnace systems, so that these coke oven banks are connected to the pot in pairs The simpler mode of operation is that each time it approaches the first coke oven chamber of the next coke oven bank, the corresponding propulsion schedule is called "by /2", and this propulsion schedule is based on the cost of filling the equipment. It is said that it is generally less expensive; however, the homogenization of the burning gas flow will be smaller. Similarly, the adjacent coke oven chamber injects heat in a more powerful manner. This propulsion schedule means: In the first propulsion cycle, the first coke oven chamber of the first coke oven reservoir is initially propelled and filled. Moreover, if the number of coke oven chambers in each coke oven warehouse is even, then the first coke oven chamber of the next coke oven warehouse is continuously propelled and filled until the last coke oven bank has been advanced and filled. a first coke oven chamber; and in a subsequent propulsion cycle, advancing and filling the next two coke oven chambers of the next coke oven bank of the series of coke ovens, and then advancing and filling the jfcb series of coking in a sequential sequence The same coke and furnace chamber of the lower furnace of the furnace, until the same coke oven chamber of the last refining 13 201030137 coke oven of the series of coke ovens is advanced and filled; and, in a final advancement In the cycle, 'propelling and filling the last coke oven chamber of the first coke oven bank, and then advancing and filling the last coke oven chamber of the next coke oven in a continuous sequence until it has been advanced and filled most The last coke oven chamber of the latter coke oven bank. In a preferred embodiment, the method of the present invention can be designed as follows: For a coke oven bank, there are only exactly half the number of boiler systems, such that the coke oven banks are linked in pairs to the steel furnace. Likewise, in this way, homogenization of the flow of combustion gases can be achieved.运用 Use a boiler to generate steam to drive the turbine. This propulsion energy can be used in any way. Preferably, this propulsion energy can be used to generate electrical energy. To this end, the boiler system is equipped with suitable means including heaters, boilers, turbines, steam separators, rotating shafts, and generators. If you want to use mechanical energy in different ways, you can also set up other supplements. 8. When passing through the boiler system, preferably, the exhaust gas is supplied to a device for cleaning the gas to minimize the possible environmental pollution caused by the coking coal manufacturing process. In particular, the sulfur-containing compound is removed from the exhaust gas during the gas cleaning process. Therefore, the gas cleaning device is preferably a desulphurization facility, for example, a gas scrubbing gas using a gas adsorbing solvent. unit. In order to perform the filling step, the coal is filled from the front side into the coke oven chamber by filling the car with a coal. Due to the previously performed coking step, the coke oven chamber is still hot and no other coal carbonization process is required. At the beginning of the 14 201030137 coking step, the door of the & coke oven chamber is closed. The coking coal is removed from the coke oven chamber after the coking step. Depending on the height of the coal block, the packing density, and the type of coke oven, the coking step takes essentially 20 to 90 hours. In a preferred embodiment of the invention, the coke oven chamber door that is easy to operate on the other side of the coke oven is implemented toward the other side of the coke oven chamber. W +
在填充時，熱焦煤被推入一焦煤淬火車内。為了實施 本發明’彳以個別地接近單個煉焦爐室。焦煤淬火車可以 設有-冷卻設備’但為了能夠快速地執行㈣卸除步驟， 較佳地設有一個預防高溫的設備。在推進與卸除熱焦煤之 後’較㈣’使淬火車進人—完全冷卻設備内，例如了此 冷卻設備可以是一焦煤淬火塔，但它也可以 乾式淬火設備。 係 為了執行本發明的方法’以偶數或奇數個煉焦爐室組 合成煉焦爐庫。在本發明的實施例中，較佳地，練焦爐庫 ❿含有6個到34個煉焦爐室。在本發明的_個特殊㈣實施 例中’煉焦爐庫確切地包含14個煉焦爐室。為了將熱廢氣 供應至鋼爐或鋼爐設備内，這些銷爐或鋼爐設備最好' = 地連結至煉焦爐庫，可藉由管線與適當的收集設備 上述連結。然而，理論上，也可以構思出將鋼爐 備連結至每三個煉焦爐庫，但在此 — ^ 钟傲π 月升乂中’熱氣體的分佑 ^更為困難。較佳地’一個鋼壚連結到兩個煉。 的個或更多 15 201030137 本發明的方法其優點在於：能夠均勻地供應熱燃燒氣 體至煉焦爐系統的鍋爐或鍋爐系統内。因&，鍋爐系統的 蒸氣產生情形可以更加均勻4匕。因此，更容易產生電氣能 量，因此顯著地減少從煉焦爐系統排出的污染物與污染 源。假如電氣能量是由本發明的方法產生的話，則電力的 產生也會均勻化及最佳化。 藉由五個圖面詳細說明本發明用於煤炭碳化的方法構 成，然而，本發明的方法並未侷限於此實施例。 圖1顯示一般在煉焦循環中從煉焦爐所產生的粗煤氣 (raw gas)之份量。 圖2顯不用於成對連結至鍋爐系統的多個煉焦爐室的 填充程序之循環排程，該循環排程係根據「2*χ/1*(χ+1)/2，，」 推進排程而設定。 圖3顯示用於成對連結至鍋爐系統的多個煉焦爐室的 填充程序之循環排程，該循環排程係根據「2*χ/1*χ/1，，」推 進排程而設定。 圖4顯示用於成對連結至鍋爐系統的多個煉焦爐室的 填充程序之循環排程，該循環排程係根據「丨*χ/2„」推進排 程而設定。 圖5顯示本發明在一煉焦系統中的多個煉焦爐庫之配 置，其中具有鍋爐及設置於下游處的辅助設備。 圖1顯示在煤炭碳化時焦煤塊上方所產生的煉焦氣體 之粗煤氣(raw gas)的份量，其主要包含有：氫氣、一氧化碳、 甲燒、及水蒸氣組合物。在此煉焦循環的整個時間内，係 201030137 以每小時標準立方公尺的體積單位而決定粗煤氣的份量， 該粗煤氣的份量係直接與完全燃燒的煉焦氣體的份量成正 比’而完全燃燒的煉焦氣體從一煉焦爐室中被注入作為燃 燒氣體。 ❹ ❿ 圖2顯示用於「填充一煉焦—推進」的循環且具有 「28/15/2”」推進排程的循環排程。每一個小矩形方塊代表 配置於煉焦爐庫内的一個練焦爐室，在整個圖式的第一行 中編有個別煉焦爐庫的數字且以樑柱垂直限定，因而產生 出1到的編號。每個煉焦爐庫包含14個煉焦爐室，這 些煉焦爐室是在整個圖式的第二行中編有i到14〇的號 ’圖式的第二行及第四行指出個別循環的時間週期（不足 「小時的部分、及多個小時的部份，均以分鐘表示從右 邊的第二欄從第五欄顯示推進機的動作循環❶首先，推進 =一煉焦爐庫的第-個煉焦爐室；然後依序是第三煉焦爐 個煉焦爐室，第五煉焦爐庫的第_個煉焦爐室， =焦爐庫的第一個煉焦爐室；最後，#進第九煉焦爐 :的第-個煉焦爐室。接著，開始第二推進循㉟ 二 煉的第二個煉焦爐室開始進#;S後依序推進第四 煉…、爐庠的第二個煉焦爐室當 推進循環。第-推耗m 時則開始第三 哀第二推進循環從第一煉焦爐庫的 室開始進杆。备你，产县依 —個煉焦爐 進仃。最後，在最後一個推進循 焦爐庫的备祕 /«. ^ jjfe 推進第一煉 早的最後-個煉焦爐t，最終推進 後一個煉焦爐室（編號為第126號的煉 ’、、爐庫的最 可以在整個煉焦設備上達成非常均勻的循環：以此… 17 201030137 圖3顯示用於「填充-煉焦-推進」的循環且具有 「’’28/14/1’’」推進排程的循環排程。首先，推進第一 爐庫的第-個煉焦爐室；然後依序是第三煉焦爐庠：第二 個煉焦爐室五煉焦爐庫的第一個煉焦爐室第七 爐庫的第-個煉焦爐室；最後，推進第九煉二 個煉焦爐室。接著，開始第二推進猶環，"二練 的第-個煉焦爐室開始進行；㈣依序推進第四煉=爐 的第一個煉焦爐室；當此循環結束時則開始第三推、進 環。第三推進循環從第一煉焦爐庫的第二個煉焦爐室開始 進行°最終’在最後-個推進循環時，推進第二煉焦 的最後-個㈣、爐室，最終，推進最後—個煉焦爐:的最 後一個煉焦爐室（編號為第14〇號的煉焦爐室）。以此方弋 也可以在整個煉焦設備上達成非常均勾的循環分佈。工’At the time of filling, the hot coking coal is pushed into a coke quench train. In order to practice the invention, the individual coke oven chambers are individually accessed. The coking coal quenching train may be provided with a - cooling device', but in order to be able to perform the (4) unloading step quickly, it is preferable to provide a device for preventing high temperature. After advancing and discharging the hot coke coal, the 'cure train' is brought into the person-completely cooled equipment. For example, the cooling device may be a coking coal quenching tower, but it may also be a dry quenching device. In order to perform the method of the present invention, a coke oven bank is assembled in an even or odd number of coke oven chambers. In an embodiment of the invention, preferably, the coke oven bank contains from 6 to 34 coke oven chambers. In the special (four) embodiment of the present invention, the coke oven bank contains exactly 14 coke oven chambers. In order to supply hot exhaust gases to steel furnaces or steel furnace equipment, these pin furnaces or steel furnace equipment are preferably connected to the coke oven bank by means of a pipeline connected to appropriate collection equipment. However, in theory, it is also conceivable to connect the steel furnace to every three coke ovens, but it is more difficult to use the 'hot gas' in the 傲 π 乂 乂 乂. Preferably, a steel crucible is joined to two refinings. One or more 15 201030137 The method of the present invention has the advantage of being able to uniformly supply hot combustion gases into a boiler or boiler system of a coke oven system. Due to &, the steam generation of the boiler system can be more uniform. Therefore, it is easier to generate electrical energy, thus significantly reducing pollutants and pollution sources discharged from the coke oven system. If electrical energy is produced by the method of the present invention, the generation of electricity is also homogenized and optimized. The method of the present invention for coal carbonization is described in detail by five drawings, however, the method of the present invention is not limited to this embodiment. Figure 1 shows the amount of raw gas produced from a coke oven in a coking cycle. Figure 2 is not used for the cyclical scheduling of the filling procedure of a plurality of coke oven chambers connected in pairs to the boiler system, the cycle schedule is based on "2*χ/1*(χ+1)/2," Set up. Fig. 3 shows a cyclic schedule for a filling procedure for a plurality of coke oven chambers connected in pairs to a boiler system, the cycle schedule being set according to "2*χ/1*χ/1," pushing the schedule. Fig. 4 shows a cycle schedule for a filling procedure for a plurality of coke oven chambers connected in pairs to a boiler system, the cycle schedule being set according to a "丨*χ/2„" propulsion schedule. Figure 5 shows the configuration of a plurality of coke oven banks in a coking system of the present invention having a boiler and ancillary equipment disposed downstream. Figure 1 shows the amount of raw gas of coking gas generated above the coking coal during carbonization of coal, which mainly comprises: hydrogen, carbon monoxide, methane, and steam compositions. During the entire time of the coking cycle, 201030137 determines the amount of crude gas in a volume unit of standard cubic meters per hour. The amount of the crude gas is directly proportional to the fraction of the fully combusted coking gas' and is completely combusted. Coking gas is injected from a coke oven chamber as a combustion gas. ❹ ❿ Figure 2 shows the cyclic schedule for the “filling a coking-propulsion” cycle with a “28/15/2” propulsion schedule. Each small rectangular square represents a coke oven chamber disposed in the coke oven warehouse. The number of individual coke oven banks is numbered in the first row of the entire drawing and is defined vertically by the beam and column, thus producing a number of 1 to . Each coke oven bank contains 14 coke oven chambers, which are numbered i to 14 in the second row of the drawing. The second and fourth rows of the pattern indicate the time of individual cycles. The period (the part of the hour and the part of the hour that is not enough) is expressed in minutes. From the second column on the right, the action cycle of the propeller is displayed from the fifth column. First, the propulsion = the first coking of the coke oven bank The furnace chamber; then the third coke oven chamber, the first coke oven chamber of the fifth coke oven, the first coke oven chamber of the coke oven; and finally, the #9 coke oven: The first coke oven chamber. Then, the second coke oven chamber starting the second propulsion cycle starts to enter #; S, then the fourth refining furnace is sequentially advanced... and the second coke oven chamber of the furnace is pushed forward. Cycle. When the first-pushing m is started, the third spurt second propulsion cycle starts from the chamber of the first coke oven warehouse. Prepare you, the county to enter the coke oven. Finally, in the last propulsion cycle The secret of the furnace /«. ^ jjfe advances the last of the first refining - a coke oven t, and finally promotes a refining The coke oven chamber (No. 126, Refining', and the furnace bank can achieve a very uniform cycle over the entire coking plant: this... 17 201030137 Figure 3 shows the cycle for "fill-coking-propulsion" and The cycle schedule with "''28/14/1''" propulsion schedule. First, advance the first coke oven chamber of the first furnace; then the third coke oven: the second coke oven The first coke oven chamber of the seventh furnace warehouse of the first coke oven chamber of the five coke ovens; finally, the second coke oven chamber of the ninth refining furnace. Then, the second propulsion of the Yuhuan ring began, & The first coke oven chamber begins; (4) the fourth coke oven chamber of the fourth refining furnace is sequentially advanced; when the cycle ends, the third push and the inlet ring are started. The third propulsion cycle is from the first coke oven bank. The second coke oven chamber begins the final 'in the last - one propulsion cycle, the second - (four), the furnace chamber, and finally the final coke oven: the last coke oven chamber It is the coke oven chamber of the 14th nickname.) This square can also be used throughout the coking plant. Prepare a very uniform loop distribution.
Q ，，圖4顯示用於「填充-煉焦-推進」的循環且具有 「14/1，，」推進排程的另一循環排程。首先，推進第一練焦 爐庫的第一個煉焦爐室；然後，推進並填充第二煉焦爐； 的第：個練焦爐室，直到已經推進最後一個煉焦爐庫的第 -個煉焦爐室為止。接著’開始第二推進循環，從 焦爐庫的第三個煉焦爐室開始進行，最終推進最後一 焦爐庫的最後-個煉焦爐室（編號為帛Μ冑的練焦爐 室P運用此推進排程’可以用—簡單的模式操作推進機， 且在整輯焦設備上可以達成均勻的循環分佈。 圏5顯示本發明钟練焦爐配置’其中包括錯爐系絶及 相關的輔助裝置。在此㈣有煉峨庫⑴，以及 18 201030137 有關的鋼爐設備⑺…。這些•爐設傷透過供應 借（）而成對地連結到煉焦爐庫⑴，包括相關的供應設 ’用以供應熱廢氣到鋼爐設備（2)。_(2)供應蒸氣能量 愛位於下游處的渴輪。從鋼爐發出的冷卻廢氣經由廢氣管 線⑷而流人—氣體清潔設備⑺内，風扇⑹產生—股負壓以 ^進脫離流線方向（〇ff_streaming)、然後，廢氣通過一條廢 氣管線而進入一廢氣煙囪（7)。圖式亦顯示有填充機，用 ❹以供應煤炭至煉焦爐庫（2)的煉焦爐室（1)，將來自壓實設備 (9)及煤炭儲存槽（10)的煤炭供應至該填充機内。填充機（8) 的後面接著是一推進機（1丨），用以從煉焦爐室推擠焦煤。最 後’圖式也顯示焦煤淬火車（12)，用以卸除個別焦爐室内的 焦煤且將焦煤載運至一焦煤淬火塔（13)内。可以在下游處設 置適當的儲存設備（14)。 [ 主要元件符號說明 1 煉焦爐庫 2 鍋爐 3 供應管線 4 廢氣線路 5 氣體清潔設備 6 風扇 7 廢氣煙囪 8 填充機 9 壓實設備 10 煤炭儲存容器 19 201030137 11 推進機 12 焦煤淬火車 13 焦煤淬火塔 14 儲存設備Q , Figure 4 shows another cycle schedule for the "fill-coking-propulsion" cycle with a "14/1,," advance schedule. First, advance the first coke oven chamber of the first coke oven warehouse; then, advance and fill the second coke oven; the first coke oven chamber until the first coke oven that has advanced the last coke oven bank Until now. Then 'start the second propulsion cycle, starting from the third coke oven chamber of the coke oven warehouse, and finally pushing the last coke oven chamber of the last coke oven bank (the coke oven chamber P numbered 帛Μ胄 applies this) Advance scheduling can operate the propeller in a simple mode, and a uniform circulation distribution can be achieved on the entire coke device. 圏5 shows the configuration of the bell-coke oven of the present invention, which includes the wrong furnace system and related auxiliary devices. In this (4) there are refining warehouses (1), and 18 201030137 related steel furnace equipment (7).... These furnaces are connected to the coke ovens (1) in pairs, including the relevant supply facilities. Supply hot exhaust gas to steel furnace equipment (2). _ (2) Supply steam energy loves the thirsty wheel located downstream. Cooling exhaust gas from the steel furnace flows through the exhaust gas line (4) - gas cleaning equipment (7), fan (6) - The negative pressure of the strand is removed from the streamline direction (〇ff_streaming), and then the exhaust gas enters an exhaust stack (7) through an exhaust line. The figure also shows a filling machine for supplying coal to the coke oven bank ( 2) The coke oven chamber (1) supplies coal from the compacting device (9) and the coal storage tank (10) to the filling machine. The filling machine (8) is followed by a propeller (1丨) for The coke oven chamber pushes coking coal. Finally, the figure also shows a coking coal quenching train (12) for removing coking coal from individual coke oven chambers and carrying coking coal into a coking coal quenching tower (13). Storage equipment (14) [ Description of the main components 1 Coking furnace 2 Boiler 3 Supply pipeline 4 Exhaust gas line 5 Gas cleaning equipment 6 Fan 7 Exhaust gas chimney 8 Filling machine 9 Compaction equipment 10 Coal storage container 19 201030137 11 Propulsion machine 12 Coking coal quenching train 13 coking coal quenching tower 14 storage equipment