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JP5058528B2 - Cement production fuel supply method and supply system - Google Patents
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JP5058528B2 - Cement production fuel supply method and supply system - Google Patents

Cement production fuel supply method and supply system Download PDF

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JP5058528B2
JP5058528B2 JP2006206298A JP2006206298A JP5058528B2 JP 5058528 B2 JP5058528 B2 JP 5058528B2 JP 2006206298 A JP2006206298 A JP 2006206298A JP 2006206298 A JP2006206298 A JP 2006206298A JP 5058528 B2 JP5058528 B2 JP 5058528B2
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flash point
cement
furnace
low flash
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健実 相沢
浩文 森
康徳 菅本
利丈 荒牧
博幸 高野
晃太郎 藤田
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Taiheiyo Cement Corp
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/10Production of cement, e.g. improving or optimising the production methods; Cement grinding
    • Y02P40/125Fuels from renewable energy sources, e.g. waste or biomass

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Description

本発明は、セメント製造用燃料供給方法及び供給システムに関し、特に、廃溶剤等の低引火点燃料をセメント製造用燃料として用いるための方法及びシステムに関する。   The present invention relates to a fuel supply method and supply system for cement production, and more particularly to a method and system for using a low flash point fuel such as a waste solvent as a fuel for cement production.

従来、セメント製造工程において、各種廃棄物を燃料の代替として用い、廃棄物の処理に資するとともに、セメント製造における高価な化石燃料の原単位を低減する試みがなされている。例えば、特許文献1には、廃プラスチックと廃油とを混合し、そのスラリー状混合物を、ロータリーキルンの主燃料(微粉炭)バーナの中心に挿入した補助燃料バーナに送給し、補助燃料バーナの補助燃料吹出口からロータリーキルン内に吹き出して燃焼させるセメントクリンカの製造方法等が提案されている。   Conventionally, attempts have been made to reduce the basic unit of expensive fossil fuels in cement production while using various wastes as substitutes for fuel in the cement production process, contributing to waste disposal. For example, in Patent Document 1, waste plastic and waste oil are mixed, and the slurry mixture is fed to an auxiliary fuel burner inserted in the center of a main fuel (pulverized coal) burner of a rotary kiln to assist the auxiliary fuel burner. A method of manufacturing a cement clinker that is blown into a rotary kiln from a fuel outlet and burned has been proposed.

一方、特許文献2には、タンカー等で発生した引火点の低い廃油を燃焼処理するにあたって、廃油に高引火点の油を添加して混合油を形成し、混合油の引火点を調べて目標の引火点以上のときはそのまま燃焼させ、目標の引火点未満のときは混合油に高引火点油を添加して引火点を高くした後燃焼させることを特徴とする廃油の燃焼方法が提案されている。
特開2003−192406号公報 特開昭57−2922号公報
On the other hand, in Patent Document 2, when a waste oil having a low flash point generated by a tanker or the like is subjected to a combustion treatment, a high flash point oil is added to the waste oil to form a mixed oil, and the flash point of the mixed oil is investigated to obtain a target. A combustion method for waste oil is proposed in which combustion is performed as it is when the flash point is higher than the target flash point, and when the flash point is lower than the target flash point, high flash point oil is added to the mixed oil to increase the flash point and then burned. ing.
JP 2003-192406 A JP 57-2922 A

上述のように、従来、セメント製造工程で各種廃棄物を燃料の代替として用いているが、アセトン、ガソリン、アルコール類、灯油、軽油等を含有する廃溶剤については、引火点が低く、防爆対策などを確実に行なう必要もあることから、セメント製造工程で燃料の代替とすることは困難であった。   As mentioned above, various types of waste have been used in the past as a substitute for fuel in the cement manufacturing process. However, waste solvents containing acetone, gasoline, alcohols, kerosene, light oil, etc. have a low flash point and are designed to prevent explosions. Therefore, it is difficult to replace the fuel in the cement manufacturing process.

そこで、本発明は、廃溶剤等の低引火点燃料についてもセメント製造工程において燃料の代替として用いることにより、廃棄物の処理と、セメント製造工程の燃料原単位の低減とを同時に達成することのできる燃料供給方法及びシステムを提供することを目的とする。   Therefore, the present invention achieves both waste treatment and reduction of fuel intensity in the cement manufacturing process by using low flash point fuel such as waste solvent as a substitute for fuel in the cement manufacturing process. An object of the present invention is to provide a fuel supply method and system.

上記目的を達成するため、本発明は、低引火点燃料と他の液状燃料とを、管路の途上で合流させ、該合流させた両燃料と固体粉末燃料とを、各々別々の管路を介し、同一のバーナから、セメント焼成炉又は仮焼炉に吹き込むセメント製造用燃料供給方法であって、前記低引火点燃料と前記他の液状燃料との合流を、前記セメント焼成炉又は前記仮焼炉への吹込装置の先端部から5m以上、50m以内の位置で行なうことを特徴とする。ここで、低引火点燃料とは、引火点70℃未満の物質を含有するものであり、アセトン、ガソリン、アルコール類、灯油、軽油等を含有する廃溶剤等が該当する。形態としては、液体、エマルジョン、スラリー等の状態のものがある。また、引火点が21℃未満の消防法で規定する第1石油類に分類される可燃性液体を含有するものを含むものとする。他の液状燃料とは、高引火点の液状燃料(液体、エマルジョン、スラリー等を含む)又は該低引火点燃料と異なる種類の低引火点燃料をいう。また、固体粉末燃料としては、微粉炭、粉末オイルコークス等を用いることができる。 In order to achieve the above object, the present invention combines a low flash point fuel and another liquid fuel in the middle of a pipeline, and the merged fuel and solid powder fuel are respectively provided in separate pipelines. Through the same burner, a method for supplying fuel for cement production, which is blown into a cement firing furnace or a calcining furnace , wherein the low flash point fuel and the other liquid fuel are combined into the cement firing furnace or the calcining furnace. It is characterized by being carried out at a position within a range of 5 m or more and 50 m or less from the tip of the blowing device into the furnace . Here, the low flash point fuel contains a substance having a flash point of less than 70 ° C., and corresponds to a waste solvent containing acetone, gasoline, alcohols, kerosene, light oil and the like. Forms include liquid, emulsion, slurry and the like. Moreover, the thing containing the combustible liquid classified into the 1st petroleum prescribed | regulated by the Fire Service Act whose flash point is less than 21 degreeC is included. Other liquid fuels refer to high flash point liquid fuels (including liquids, emulsions, slurries, etc.) or low flash point fuels of a type different from the low flash point fuels. Moreover, pulverized coal, powdered oil coke, etc. can be used as solid powder fuel.

そして、本発明によれば、低引火点燃料と、他の液状燃料と、固体粉末燃料とをセメント焼成炉又は仮焼炉に吹き込むことにより、低引火点燃料としての廃溶剤等の廃棄物処理と、セメント製造工程の燃料原単位の低減を同時に図ることができる。
また、前記低引火点燃料と前記他の液状燃料とを、管路の途上で合流させ、前記セメント焼成炉又は前記仮焼炉に吹き込むことで、炉内のフレームを適正に形成することができるとともに、バーナーの製作や、耐火物の施工に関するコストを低減することができる。また、貯蔵タンク等において、低引火点燃料と他の液状燃料と混合したのでは、化学反応が起って爆発したり、危険な物質に変質したり、取り扱いが困難になる場合があるが、管路の途上で合流させることにより、これらの危険性等を回避することができる。
さらに、前記低引火点燃料と前記他の液状燃料との合流を、前記セメント焼成炉又は仮焼炉への吹込装置の先端部から5m以上、50m以内の位置で行なうことができ、この距離は、吹込装置の先端部からの直線距離ではなく、管路に沿って測定した長さをいう。低引火点燃料と他の液状燃料を合流させると、上述のように、場合によっては、両燃料間で化学反応が起って爆発等の危険性が高まることとなるが、セメント焼成炉又は仮焼炉へ吹き込む直前で合流させることによって、化学反応が進行する前に両燃料をセメント焼成炉等に吹込んで燃焼させることができるため、より安全に低引火点燃料をセメント製造用燃料として用いることができる。
また、固体粉末燃料を、低引火点燃料と同一バーナの別管路で吹き込むことにより、炉内のフレームを適正に形成することができるとともに、バーナの製作や、耐火物の施工に関するコストを低減することができる。
さらに、固体粉末燃料と低引火点燃料とを並行して吹き込むことにより、固体粉末燃料の揮発分が増加した形となり、固体粉末燃料の燃焼性を向上させながら、低引火点燃料をセメント製造用燃料として用いることができる。
Then, according to the present invention, waste processing such as waste solvent as low flash point fuel is obtained by blowing low flash point fuel , other liquid fuel, and solid powder fuel into a cement firing furnace or calcining furnace. In addition, it is possible to simultaneously reduce the fuel intensity in the cement manufacturing process.
In addition, the low flash point fuel and the other liquid fuel can be merged in the middle of a pipeline and blown into the cement firing furnace or the calcining furnace, so that a frame in the furnace can be appropriately formed. At the same time, it is possible to reduce costs related to the production of burners and the construction of refractories. In addition, if a low flash point fuel and other liquid fuels are mixed in a storage tank, etc., a chemical reaction may occur and it may explode, or it may become a hazardous substance, and handling may be difficult. These dangers can be avoided by merging in the middle of the pipeline.
Furthermore, the merging of the low flash point fuel and the other liquid fuel can be performed at a position within 5 m and within 50 m from the tip of the blowing device to the cement baking furnace or calcining furnace. , Not the linear distance from the tip of the blowing device, but the length measured along the pipeline. When the low flash point fuel and other liquid fuel are merged, as described above, a chemical reaction may occur between the two fuels and the risk of an explosion may increase. By merging just before blowing into the furnace, both fuels can be blown into the cement firing furnace and burned before the chemical reaction proceeds, so the low flash point fuel should be used as a safer fuel for cement production. Can do.
In addition, by blowing solid powder fuel in a separate conduit of the same burner as the low flash point fuel, it is possible to properly form the frame inside the furnace, and to reduce costs related to burner production and refractory construction can do.
Furthermore, by blowing the solid powder fuel and the low flash point fuel in parallel, the volatile matter of the solid powder fuel is increased, and the low flash point fuel is used for cement production while improving the combustibility of the solid powder fuel. It can be used as fuel.

さらに、本発明は、低引火点燃料の供給管路と、他の液状燃料の供給管路と、
両供給管路の合流点と、固体粉末燃料の供給管路と、前記合流点で合流した両燃料と、前記供給管路からの固体粉末燃料を別々に、同一のバーナを介して、セメント焼成炉又は仮焼炉へ吹き込む吹込装置とを備えるセメント製造用燃料供給システムであって、前記合流点は、前記セメント焼成炉又は仮焼炉への吹込装置の先端部から5m以上、50m以内に位置することを特徴とする。
Furthermore, the present invention provides a low flash point fuel supply line, another liquid fuel supply line,
And confluence of the two supply lines, a supply pipe of a solid powder fuel, a double fuel merge at the merging point, separately and solid powder fuel from the supply line, via the same burner, cement A fuel supply system for cement production comprising a blowing apparatus for blowing into a firing furnace or a calcining furnace, wherein the junction is within 5 m to 50 m from the tip of the blowing apparatus to the cement firing furnace or calcining furnace It is characterized by being located .

そして、本発明によれば、上記発明と同様に、低引火点燃料としての廃溶剤等の廃棄物処理と、セメント製造工程の燃料原単位の低減を同時に図ることができるとともに、炉内のフレームを適正に形成することができ、さらに、バーナの製作や、耐火物の施工に関するコストを低減することができる。
これに加え、固体粉末燃料と低引火点物質とを並行して吹き込むことにより、固体粉末燃料の揮発分が増加した形となり、固体粉末燃料の燃焼性を向上させながら、低引火点燃料をセメント製造用燃料として用いることができる。
また、低引火点燃料と、他の液状燃料とを合流させて同一の管路から吹込むことにより、炉内のフレームを適正に形成することができるとともに、バーナーの製作や、耐火物の施工に関するコストを低減することができる。
さらに、前記合流点を、前記セメント焼成炉又は前記仮焼炉への吹込装置の先端部から5m以上、50m以内に位置させることで、上述のように、低引火点燃料と他の液状燃料との化学反応が進行する前に両燃料をセメント焼成炉等に吹込んで燃焼させることができるため、より安全に低引火点燃料をセメント製造用燃料として用いることができる。
According to the present invention, as in the case of the above-mentioned invention, waste processing such as waste solvent as a low flash point fuel can be simultaneously performed and reduction of the fuel intensity in the cement manufacturing process can be achieved simultaneously. Can be formed appropriately, and furthermore, the costs for the production of the burner and the construction of the refractory can be reduced.
In addition, the solid powder fuel and the low flash point substance are blown in parallel to increase the volatile content of the solid powder fuel, and the low flash point fuel is cemented while improving the combustibility of the solid powder fuel. It can be used as a production fuel.
In addition, by combining low-flash point fuel and other liquid fuels and blowing them from the same pipe, it is possible to properly form the frame inside the furnace, as well as burner production and refractory construction The cost regarding can be reduced.
Further, as described above, the junction point is located within 5 m or more and 50 m or less from the tip of the blowing device to the cement firing furnace or the calcining furnace, and as described above, the low flash point fuel and the other liquid fuel Since both fuels can be blown into a cement firing furnace and burned before the chemical reaction proceeds, a low flash point fuel can be used more safely as a cement production fuel.

以上のように、本発明によれば、廃溶剤等の低引火点燃料についてもセメント製造工程において燃料の代替として用いることができ、廃棄物の処理と、セメント製造工程の高価な化石燃料の原単位の低減とを同時に達成することが可能となる。   As described above, according to the present invention, a low flash point fuel such as a waste solvent can also be used as a fuel substitute in the cement manufacturing process, and the raw material for waste treatment and the expensive fossil fuel in the cement manufacturing process can be used. Unit reduction can be achieved at the same time.

次に、本発明の実施の形態について、図面を参照しながら説明する。   Next, embodiments of the present invention will be described with reference to the drawings.

図1は、本発明にかかるセメント製造用燃料供給システムの一実施の形態を示し、このシステム1は、大別して、低引火点燃料槽2と、高引火点燃料槽3と、混合器4と、バーナ5とで構成され、セメント焼成炉10及びクリンカクーラ11を備えるセメント焼成設備に燃料を供給するために備えられる。   FIG. 1 shows an embodiment of a cement production fuel supply system according to the present invention. This system 1 is roughly divided into a low flash point fuel tank 2, a high flash point fuel tank 3, a mixer 4 and The burner 5 is provided to supply fuel to a cement firing facility including a cement firing furnace 10 and a clinker cooler 11.

低引火点燃料槽2は、低引火点燃料を一時的に貯蔵するために備えられ、低引火点燃料としての廃溶剤等が貯蔵される。尚、低引火点燃料槽2に低引火点燃料を長期間貯蔵すると、他の物質と混合されて危険な物質となったり、析出、固化等により取り扱いが困難となるため、貯蔵期間は短期間とすることが好ましい。この低引火点燃料槽2には、低引火点燃料を混合器4を経てバーナ5に供給するためのポンプ8と、管路6とが付設される。   The low flash point fuel tank 2 is provided for temporarily storing the low flash point fuel, and stores a waste solvent or the like as the low flash point fuel. In addition, if the low flash point fuel is stored in the low flash point fuel tank 2 for a long period of time, it becomes a dangerous substance by mixing with other substances, and it becomes difficult to handle due to precipitation, solidification, etc., so the storage period is short. It is preferable that The low flash point fuel tank 2 is provided with a pump 8 for supplying low flash point fuel to the burner 5 through the mixer 4 and a pipe 6.

高引火点燃料槽3は、液状の高引火点燃料を一時的に貯蔵するために備えられ、高引火点燃料としての廃油等が貯蔵される。高引火点燃料槽3には、高引火点燃料を混合器4を経てバーナ5に供給するためのポンプ9と、管路7とが付設される。   The high flash point fuel tank 3 is provided for temporarily storing liquid high flash point fuel, and stores waste oil or the like as the high flash point fuel. The high flash point fuel tank 3 is provided with a pump 9 for supplying high flash point fuel to the burner 5 through the mixer 4 and a pipe 7.

混合器4は、高引火点燃料2から供給される高引火点燃料と、低引火点燃料槽2から供給される低引火点燃料とをセメント焼成炉10の直前で混合するため、バーナ5の先端部から5m以上、50m以内、好ましくは5m以上、30m以内、より好ましくは5m以上、20m以内に配置する。また、混合器4を管路6、7の合流点に配置せずに、管路6、7の合流点とバーナ5との間に配置してもよい。この混合器4には、静止型混合器、インラインミキサー等を用いることができる。   The mixer 4 mixes the high flash point fuel supplied from the high flash point fuel 2 and the low flash point fuel supplied from the low flash point fuel tank 2 immediately before the cement firing furnace 10. It arrange | positions from 5 m or more and 50 m or less from a front-end | tip part, Preferably it is 5 m or more and 30 m or less, More preferably, it is 5 m or more and 20 m or less. Further, the mixer 4 may be arranged between the junction of the pipelines 6 and 7 and the burner 5 without being arranged at the junction of the pipelines 6 and 7. The mixer 4 can be a static mixer, an in-line mixer, or the like.

次に、上記構成を有するセメント製造用燃料供給システム1の動作について、図1を参照しながら説明する。   Next, operation | movement of the fuel supply system 1 for cement manufacture which has the said structure is demonstrated, referring FIG.

低引火点燃料及び高引火点燃料を受け入れ、低引火点燃料槽2及び高引火点燃料槽3に一時的に貯蔵した後、セメント焼成炉10の運転時に、各々、ポンプ8及び管路6、ポンプ9及び管路7とを介して混合器4に供給する。   After receiving the low flash point fuel and the high flash point fuel and temporarily storing them in the low flash point fuel tank 2 and the high flash point fuel tank 3, when operating the cement firing furnace 10, the pump 8 and the pipeline 6, The mixture is supplied to the mixer 4 through the pump 9 and the pipe line 7.

混合器4において、両燃料を混合する。これにより、セメント焼成炉又は仮焼炉における均一な燃焼を図ることができる。尚、混合器4における低引火点燃料と高引火点燃料との混合により、両者が反応し、爆発しやすい状態となるなど、何らかの問題が発生するおそれもあるが、混合器4における混合後、両燃料の混合物は即座にバーナ5に供給されてセメント焼成炉10に吹込まれて燃焼するため安全である。   In the mixer 4, both fuels are mixed. Thereby, the uniform combustion in a cement baking furnace or a calcining furnace can be aimed at. In addition, there is a possibility that some problems may occur, such as the reaction of both of the low flash point fuel and the high flash point fuel in the mixer 4 and the possibility of explosion, but after mixing in the mixer 4, The mixture of both fuels is safe because it is immediately supplied to the burner 5 and blown into the cement firing furnace 10 for combustion.

両燃料の混合物を、バーナ5からセメント焼成炉10に吹き込み、セメント焼成に利用する。これによって、廃溶剤等の低引火点燃料についてもセメント製造工程において燃料の代替として用いることができ、廃棄物の処理と、セメント製造工程の高価な化石燃料の原単位の低減という効果を同時に得ることができる。   A mixture of both fuels is blown from the burner 5 into the cement firing furnace 10 and used for cement firing. As a result, low flash point fuels such as waste solvents can be used as a substitute for fuel in the cement manufacturing process, and the effects of waste treatment and reduction in the basic unit of expensive fossil fuel in the cement manufacturing process can be obtained at the same time. be able to.

尚、上記実施の形態においては、低引火点燃料と高引火点燃料とをセメント焼成炉10に吹き込む場合について説明したが、上記と同様のシステムを用い、セメント焼成設備の仮焼炉にバーナを介して吹き込むこともでき、上記と同様の効果を奏することができる。   In the above embodiment, the case where the low flash point fuel and the high flash point fuel are blown into the cement firing furnace 10 has been described. However, a burner is used in the calcining furnace of the cement firing facility using the same system as described above. Can be blown through, and the same effects as described above can be obtained.

また、上記実施の形態においては、低引火点燃料と高引火点燃料とを混合する場合について説明したが、全燃料中の低引火点燃料の割合は、0を超え100%までの広い範囲から選択することができる。   In the above embodiment, the case where the low flash point fuel and the high flash point fuel are mixed has been described. However, the ratio of the low flash point fuel in the total fuel ranges from 0 to 100% in a wide range. You can choose.

さらに、上記実施の形態においては、低引火点燃料と高引火点燃料とをセメント焼成炉等に吹き込む場合について説明したが、異なる種類の低引火点燃料同士を合流させて吹き込むこともできる。例えば、第1の低引火点燃料としての廃アルコールと、第2の低引火点燃料としてのトルエン系廃溶剤とを合流させて吹き込むことができる。   Furthermore, in the above-described embodiment, the case where the low flash point fuel and the high flash point fuel are blown into a cement firing furnace or the like has been described. However, different types of low flash point fuels may be joined together and blown. For example, waste alcohol as the first low flash point fuel and toluene-based waste solvent as the second low flash point fuel can be merged and blown.

また、上記実施の形態においては、低引火点燃料と液状の高引火点燃料とを合流させる場合について説明したが、異なる種類の低引火点燃料同士を合流させてもよい。   Moreover, in the said embodiment, although the case where a low flash point fuel and a liquid high flash point fuel were merged was demonstrated, you may merge different types of low flash point fuels.

さらに、2つの燃料を合流させずに、各々別々の供給管路からセメント焼成炉等に吹き込むようにしてもよく、低引火点燃料と液状の高引火点燃料とを、又は、低引火点燃料と固体の高引火点燃料とを、又は異なる種類の低引火点燃料同士を合流させずに吹き込むことができる。この際、各々別々の供給管路を同一のバーナに備えてもよく、各々の供給管路を別々のバーナに備えるように構成することもできる。特に、低引火点燃料と、高引火点の固体粉末燃料とを同一バーナーで別々の管路を介して吹き込むことで、炉内のフレームを適正に形成することができるとともに、バーナーの製作や、耐火物の施工に要するコストを低減することができる。   Further, the two fuels may not be merged but may be blown into a cement firing furnace or the like from separate supply pipes, and a low flash point fuel and a liquid high flash point fuel or a low flash point fuel may be used. And solid high flash point fuel, or different types of low flash point fuels can be blown together. At this time, the separate supply pipelines may be provided in the same burner, or the respective supply pipelines may be provided in separate burners. In particular, by blowing low-flash-point fuel and high-flash-point solid powder fuel through separate pipes with the same burner, it is possible to properly form the flame in the furnace, The cost required for the construction of the refractory can be reduced.

本発明にかかるセメント製造用燃料供給システムの一実施の形態を示す概略図である。It is the schematic which shows one Embodiment of the fuel supply system for cement manufacture concerning this invention.

符号の説明Explanation of symbols

1 セメント製造用燃料供給システム
2 低引火点燃料槽
3 高引火点燃料槽
4 混合器
5 バーナ
6 管路
7 管路
8 ポンプ
9 ポンプ
10 セメント焼成炉
11 クリンカクーラ
1 Fuel supply system for cement production 2 Low flash point fuel tank 3 High flash point fuel tank 4 Mixer 5 Burner 6 Pipe line 7 Pipe line 8 Pump 9 Pump 10 Cement firing furnace 11 Clinker cooler

Claims (2)

低引火点燃料と他の液状燃料とを管路の途上で合流させ、該合流させた両燃料と固体粉末燃料とを、各々別々の管路を介し、同一のバーナから、セメント焼成炉又は仮焼炉に吹き込むセメント製造用燃料供給方法であって、
前記低引火点燃料と前記他の液状燃料との合流を、前記セメント焼成炉又は前記仮焼炉への吹込装置の先端部から5m以上、50m以内の位置で行なうことを特徴とするセメント製造用燃料供給方法。
The low flash point fuel and the other liquid fuel are merged in the middle of the pipeline, and the merged fuel and the solid powder fuel are respectively sent from the same burner through a separate pipeline to a cement firing furnace or temporary A fuel supply method for manufacturing cement to be blown into a furnace ,
For the production of cement, the merging of the low flash point fuel and the other liquid fuel is performed at a position within a range of 5 m to 50 m from the tip of the blowing device into the cement firing furnace or the calcining furnace . Fuel supply method.
低引火点燃料の供給管路と、
他の液状燃料の供給管路と、
両供給管路の合流点と、
固体粉末燃料の供給管路と、
前記合流点で合流した両燃料と、記供給管路からの固体粉末燃料を別々に、同一のバーナを介して、セメント焼成炉又は仮焼炉へ吹き込む吹込装置とを備えるセメント製造用燃料供給システムであって、
前記合流点は、前記セメント焼成炉又は前記仮焼炉への吹込装置の先端部から5m以上、50m以内に位置することを特徴とするセメント製造用燃料供給システム。
A low flash point fuel supply line;
Other liquid fuel supply lines;
The confluence of both supply lines,
A solid powder fuel supply line;
And both fuel merge at the merging point, before and separately solid powder fuels Campanulaceae supply conduit or al, via the same burner, cement production and a blowing device for blowing to a cement burning furnace or calciner Fuel supply system,
The cement supply fuel supply system according to claim 1, wherein the junction is located within a range of 5 m to 50 m from a tip portion of a blowing device into the cement baking furnace or the calcining furnace .
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