JP2007254863A - Sintered material with the use of organic waste, method for producing the sintered material, and refining method - Google Patents

Sintered material with the use of organic waste, method for producing the sintered material, and refining method Download PDF

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JP2007254863A
JP2007254863A JP2006083225A JP2006083225A JP2007254863A JP 2007254863 A JP2007254863 A JP 2007254863A JP 2006083225 A JP2006083225 A JP 2006083225A JP 2006083225 A JP2006083225 A JP 2006083225A JP 2007254863 A JP2007254863 A JP 2007254863A
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carbide
mixture
organic waste
calcium oxide
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Yusuke Aoyanagi
祐介 青柳
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Osaka Gas Co Ltd
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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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel
    • 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
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Abstract

<P>PROBLEM TO BE SOLVED: To provide a sintered material which can be produced at a reduced fuel cost, by more flexibly using a material for thermal energy in a sintering furnace to reduce an amount of coke used for treatment in a blast furnace, when organic waste is used in refining treatment. <P>SOLUTION: A carbide is produced by the steps of: charging the organic waste containing calcium oxide such as municipal solid waste, sewage sludge and industrial waste into a carbonizing apparatus 1 for heating materials at a high temperature; supplying a flue gas sent from a combustion apparatus 3 and further an exhaust gas generated in an incineration facility and an in-house power generating station to the carbonizing apparatus 1; and roasting the organic matter at 400 to 700°C. The sintered material of a mixture of the carbide and sintered ore is produced by the steps of: supplying the carbide obtained in the carbonizing apparatus 1 and fine iron ore to an external heating type sintering furnace 4 for heating materials at a high temperature; and heating the mixture at 900°C or higher from the external part with hot blast such as the flue gas sent from the combustion apparatus 3 to bake the mixture of carbide and calcium oxide and the fine iron ore. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、一般ごみ、産業廃棄物、下水汚泥といった酸化カルシウムを含んだ有機性廃棄物を利用した焼結物、および、その焼結物の製造方法、ならびに、精錬処理方法に関する。   The present invention relates to a sintered product using organic waste containing calcium oxide such as general waste, industrial waste, and sewage sludge, a method for producing the sintered product, and a refining treatment method.

有機性廃棄物の処理については社会的関心が高く、従来、高炉用焼結鉱の製造に利用するものが知られている。
すなわち、都市ごみ、家庭ごみ、産業廃棄物、一般廃棄物、シュレッダーダストなどのごみから、ガラス、陶磁器類、金属類を除去し、その後、得られた可燃物を主体とするごみを、破砕もしくは粉砕してから乾燥する。その乾燥後のごみを再度破砕もしくは粉砕した後、脱塩素剤、水分除去剤、固化剤を必要に応じて添加した後に、例えば、外形がクレヨン状のごみ固形燃料を製造する。そのごみ固形燃料を炭化工程に搬送し、炭化装置で乾留してごみ固形燃料の炭化物を製造し、その炭化物を製鉄所の焼結工場に輸送し、焼結機で使用する粉コークスの代替として用いるように構成されている(特許文献1参照)。
特開2000−109935号公報
Regarding the treatment of organic waste, there is a great social interest, and what is used for the production of sintered ore for blast furnaces has been known.
In other words, glass, ceramics, and metals are removed from municipal waste, household waste, industrial waste, general waste, shredder dust, etc., and then the waste mainly composed of combustible materials is crushed or Grind and dry. After the dried waste is crushed or pulverized again, a dechlorinating agent, a water removing agent, and a solidifying agent are added as necessary, and then, for example, a solid waste fuel having a crayon-like outer shape is produced. The waste solid fuel is transported to the carbonization process, carbonized to produce carbonized solid waste fuel, transported to a sintering plant at the steel mill, and used as an alternative to the powder coke used in the sintering machine. It is comprised so that it may be used (refer patent document 1).
JP 2000-109935 A

しかしながら、従来例の場合、焼結時の粉コークスの代替とするために、焼結処理を点火炉で行い、その焼結処理の際にごみ固形燃料の炭化物を燃焼させてしまうものであり、高炉での還元処理に際しては、得られた焼結物に新たに多量のコークスを加える必要があった。   However, in the case of the conventional example, in order to replace the powder coke at the time of sintering, the sintering process is performed in an ignition furnace, and the solid fuel carbide is burned during the sintering process, During the reduction treatment in the blast furnace, it was necessary to add a large amount of coke to the obtained sintered product.

本発明は、このような事情に鑑みてなされたものであって、請求項1および2に係る発明は、焼結炉での熱エネルギー面での自由度を高めて高炉での処理に際してのコークスの使用量を減少し、有機性廃棄物を利用して精錬処理を行う上で燃料費を安価にできる焼結物を提供できるようにすることを目的とし、請求項3に係る発明は、焼結物を安価に製造できるようにすることを目的とする。また、請求項4に係る発明は、銑鉄を安価に製造できるようにすることを目的とし、請求項5に係る発明は、リン含有鋼を安価に製造できるようにすることを目的とする。   The present invention has been made in view of such circumstances, and the invention according to claims 1 and 2 increases the degree of freedom in terms of thermal energy in a sintering furnace, and coke during processing in a blast furnace. The invention according to claim 3 aims to provide a sintered product that can reduce the fuel cost when refining treatment using organic waste. The object is to make it possible to produce the product at a low cost. Further, the invention according to claim 4 aims to make it possible to produce pig iron at a low cost, and the invention according to claim 5 aims to make it possible to produce phosphorus-containing steel at a low cost.

請求項1に係る発明の有機性廃棄物を利用した焼結物は、上述のような目的を達成するために、
酸化カルシウムを含んだ有機性廃棄物を炭化処理して生成させた炭化物と酸化カルシウムとの混合物と、鉄鉱石の粉鉱石とが焼き固めて生成されて成ることを特徴としている。
酸化カルシウムを含んだ有機性廃棄物の代表的なものとしては、雑多な一般ごみ、生活排水を処理した下水汚泥、産業廃棄物などが挙げられるが、酸化カルシウムを含む有機性物質、酸化カルシウムを含む無機物質と有機性物質の混合物、または、酸化カルシウムを含む有機性物質と有機性物質の混合物など、酸化カルシウムと有機性成分を含む物質、または、酸化カルシウムを含む物質(有機性物質を含む)と有機性成分を含む物質の混合物であっても良い。
酸化カルシウムを含んだ有機性廃棄物を炭化処理して生成させた炭化物とは、酸化カルシウムを含んだ有機性廃棄物を炭化処理、ガス化処理または熱分解した後の炭化物のことをいう。
In order to achieve the object as described above, the sintered product using the organic waste of the invention according to claim 1
It is characterized in that a mixture of a carbide and calcium oxide produced by carbonizing an organic waste containing calcium oxide and iron ore powder ore are baked and solidified.
Typical organic waste containing calcium oxide includes miscellaneous general waste, sewage sludge treated from domestic wastewater, industrial waste, etc., but organic substances containing calcium oxide, calcium oxide Substances containing calcium oxide and organic components, or substances containing calcium oxide (including organic substances), such as a mixture of inorganic and organic substances, or a mixture of organic substances and organic substances containing calcium oxide ) And a substance containing an organic component.
The carbide produced by carbonizing an organic waste containing calcium oxide refers to a carbide after carbonizing, gasifying or pyrolyzing an organic waste containing calcium oxide.

(作用・効果)
請求項1に係る発明の有機性廃棄物を利用した焼結物の構成によれば、有機性廃棄物を炭化処理して生成させた混合物中の酸化カルシウムが焼結の際にガラス相を形成し、それを焼結剤に利用して鉄鉱石の粉鉱石を造粒して焼き固めることができる。
したがって、焼結の際に、外部からの加熱によって焼き固め、炭化物を燃焼させないから、その炭化物を高炉での処理に際しての燃料として利用することができるとともに、炭化物中の炭素が鉄鉱石中の酸素と結合して二酸化炭素となることで還元剤として利用でき、焼結処理において、従来のような粉コークスやその代替品としての炭化物を用いずに、各種処理で発生する可燃性ガスや、都市ガスなどの外部燃料、更には排熱を利用するなど、各種の加熱熱源を用いることができ、焼結処理での熱エネルギー面での自由度を高めるとともに炭化物を高炉での燃料および還元剤として利用し、高炉での処理に際してのコークスの使用量を減少し、有機性廃棄物を利用して精錬処理を行う上で燃料費を安価にできる焼結物を提供できる。
(Action / Effect)
According to the structure of the sintered product using the organic waste of the invention according to claim 1, calcium oxide in the mixture produced by carbonizing the organic waste forms a glass phase during sintering. Then, it can be granulated into iron ore powder ore by using it as a sintering agent and baked.
Therefore, during sintering, the carbides are not baked and hardened by heating from the outside, so that the carbides can be used as a fuel for processing in the blast furnace, and the carbon in the carbides is oxygen in the iron ore. It can be used as a reducing agent by combining with carbon dioxide and can be used as a reducing agent. In the sintering process, combustible gas generated in various processes without using conventional powder coke and carbide as an alternative, and city Various heating heat sources can be used, such as using external fuel such as gas, and exhaust heat, increasing the degree of freedom in terms of thermal energy in the sintering process, and using carbide as fuel and reducing agent in the blast furnace It is possible to provide a sintered product that can reduce the amount of coke used in processing in a blast furnace and reduce the fuel cost when performing refining processing using organic waste.

また、請求項2に係る発明の有機性廃棄物を利用した焼結物の製造方法は、前述のような目的を達成するために、
酸化カルシウムを含んだ有機性廃棄物を炭化処理して炭化物と酸化カルシウムとの混合物を生成させ、前記混合物と鉄鉱石の粉鉱石とを外熱型焼結炉で焼き固めるように構成する。
Moreover, the manufacturing method of the sintered compact using the organic waste of the invention according to claim 2 is to achieve the object as described above.
An organic waste containing calcium oxide is carbonized to produce a mixture of carbide and calcium oxide, and the mixture and iron ore powder ore are baked and hardened in an externally heated sintering furnace.

(作用・効果)
請求項2に係る発明の有機性廃棄物を利用した焼結物の製造方法の構成によれば、有機性廃棄物を炭化処理して生成させた混合物中の酸化カルシウムが外熱型焼結炉での焼結の際にガラス相を形成し、それを焼結剤に利用して鉄鉱石の粉鉱石を造粒して焼き固めることができる。
したがって、焼結の際に、外部からの加熱によって焼き固め、炭化物を燃焼させないから、その炭化物を高炉での処理に際しての燃料として利用することができるとともに、炭化物中の炭素が鉄鉱石中の酸素と結合して二酸化炭素となることで還元剤として利用でき、焼結処理において、従来のような粉コークスやその代替品としての炭化物を用いずに、各種処理で発生する可燃性ガスや、都市ガスなどの外部燃料、更には排熱を利用するなど、外熱型焼結炉で各種の加熱熱源を用いることができ、焼結処理での熱エネルギー面での自由度を高めるとともに炭化物を高炉での燃料および還元剤として利用し、高炉での処理に際してのコークスの使用量を減少し、有機性廃棄物を利用して精錬処理を行う上で燃料費を安価にできる焼結物を提供できる。
(Action / Effect)
According to the structure of the method for producing a sintered product using the organic waste of the invention according to claim 2, the calcium oxide in the mixture produced by carbonizing the organic waste is converted into an external heating type sintering furnace. A glass phase is formed during sintering at, and iron ore fine ore can be granulated and baked by using it as a sintering agent.
Therefore, during sintering, the carbides are not baked and hardened by heating from the outside, so that the carbides can be used as a fuel for processing in the blast furnace, and the carbon in the carbides is oxygen in the iron ore. It can be used as a reducing agent by combining with carbon dioxide and can be used as a reducing agent. In the sintering process, combustible gas generated in various processes without using conventional powder coke and carbide as an alternative, and city Various heat sources such as gas and other external fuels and exhaust heat can be used in an external heating type sintering furnace, increasing the degree of freedom in terms of thermal energy in the sintering process and carburizing the carbide Sinter that can be used as a fuel and reducing agent in the blast furnace, reduce the amount of coke used in blast furnace treatment, and reduce the fuel cost for refining treatment using organic waste Kill.

また、請求項3に係る発明は、前述のような目的を達成するために、
請求項2に記載の有機性廃棄物を利用した焼結物の製造方法において、
炭化処理で発生する未燃炭素のガス成分を外熱型焼結炉の加熱熱源の燃料として用いるように構成する。
In order to achieve the above-described object, the invention according to claim 3
In the manufacturing method of the sintered compact using the organic waste of Claim 2,
The gas component of unburned carbon generated in the carbonization process is used as a fuel for a heating heat source of the external heating type sintering furnace.

(作用・効果)
請求項3に係る発明の有機性廃棄物を利用した焼結物の製造方法の構成によれば、炭化処理で発生する未燃炭素のガス成分を外熱型焼結炉の加熱熱源の燃料に利用するから、外熱型焼結炉に使用する専用の燃料の消費量を低減でき、焼結物を安価に製造できる。
(Action / Effect)
According to the structure of the manufacturing method of the sintered compact using the organic waste of the invention according to claim 3, the gas component of unburned carbon generated in the carbonization process is used as the fuel of the heating heat source of the external heating type sintering furnace. Since it uses, the consumption of the fuel for exclusive use used for an external-heating-type sintering furnace can be reduced, and a sintered compact can be manufactured cheaply.

また、請求項4に係る発明の精錬処理方法は、前述のような目的を達成するために、
酸化カルシウムを含んだ有機性廃棄物を炭化処理して炭化物と酸化カルシウムとの第1の混合物を生成させ、前記第1の混合物と鉄鉱石の粉鉱石とを外熱型焼結炉で加熱処理して炭化物と焼結鉱との第2の混合物を生成させ、前記第2の混合物とコークスとを高炉で加熱処理して銑鉄を製造するように構成する。
Further, the refining treatment method of the invention according to claim 4 is to achieve the above-described object,
An organic waste containing calcium oxide is carbonized to produce a first mixture of carbide and calcium oxide, and the first mixture and iron ore powder ore are heat-treated in an externally heated sintering furnace. Then, a second mixture of carbide and sintered ore is produced, and the second mixture and coke are heated in a blast furnace to produce pig iron.

(作用・効果)
請求項4に係る発明の精錬処理方法の構成によれば、有機性廃棄物を炭化処理して生成させた第1の混合物中の酸化カルシウムが外熱型焼結炉での焼結の際にガラス相を形成し、それを焼結剤に利用して鉄鉱石の粉鉱石を造粒して焼き固めることができる。その鉄鉱石の粉鉱石を造粒して焼き固めた焼結鉱と炭化物とから成る第2の混合物とコークスとを高炉で加熱処理し、焼結処理で燃焼させなかった炭化物を高炉で精錬時のコークスの代替品に利用して、炭化物およびコークス中の炭素により酸化鉄を還元し、銑鉄を製造することができる。
したがって、焼結の際に、外部からの加熱によって焼き固め、炭化物を燃焼させないから、その炭化物を高炉での処理に際しての燃料として利用することができるとともに、炭化物中の炭素が鉄鉱石中の酸素と結合して二酸化炭素となることで還元剤として利用でき、焼結処理において、従来のような粉コークスやその代替品としての炭化物を用いずに、各種処理で発生する可燃性ガスや、都市ガスなどの外部燃料、更には排熱を利用するなど、外熱型焼結炉で各種の加熱熱源を用いることができ、焼結処理での熱エネルギー面での自由度を高めるとともに炭化物を高炉での燃料および還元剤として利用し、高炉での処理に際してのコークスの使用量を減少でき、有機性廃棄物を有効利用して、銑鉄を安価に製造できる。
(Action / Effect)
According to the configuration of the refining treatment method of the invention according to claim 4, the calcium oxide in the first mixture produced by carbonizing the organic waste is subjected to sintering in the external heating type sintering furnace. A glass phase is formed, and it can be used as a sintering agent to granulate and sinter iron ore powder ore. When the iron ore powder ore is granulated and baked, the second mixture of sintered ore and carbide and coke are heated in a blast furnace, and the carbide not burned by the sintering process is refined in the blast furnace. It is possible to produce pig iron by reducing iron oxide with carbide and carbon in coke.
Therefore, during sintering, the carbides are not baked and hardened by heating from the outside, so that the carbides can be used as a fuel for processing in the blast furnace, and the carbon in the carbides is oxygen in the iron ore. It can be used as a reducing agent by combining with carbon dioxide and can be used as a reducing agent. In the sintering process, combustible gas generated in various processes without using conventional powder coke and carbide as an alternative, and city Various heat sources such as gas and other external fuels and exhaust heat can be used in an external heating type sintering furnace, increasing the degree of freedom in terms of thermal energy in the sintering process and carburizing the carbide It can be used as a fuel and a reducing agent in the blast furnace, the amount of coke used in the treatment in the blast furnace can be reduced, and pig iron can be manufactured at low cost by effectively using organic waste.

また、請求項5に係る発明は、前述のような目的を達成するために、
請求項4に記載の精錬処理方法において、
第1の混合物が、下水汚泥を炭化処理した下水汚泥炭化物と、下水汚泥以外の有機性廃棄物を炭化処理した炭化物とから成り、前記下水汚泥炭化物の含有量を調整するように構成する。
In order to achieve the above-described object, the invention according to claim 5
In the refining processing method according to claim 4,
The first mixture includes sewage sludge carbide obtained by carbonizing sewage sludge and carbide obtained by carbonizing organic waste other than sewage sludge, and is configured to adjust the content of the sewage sludge carbide.

(作用・効果)
請求項5に係る発明の精錬処理方法の構成によれば、下水汚泥を炭化処理した下水汚泥炭化物に含まれるリン酸を有効利用し、その含有量を調整することでリン含有鋼の製造に対応することができる。
したがって、リン含有鋼を製造する上で、リンを使用せずに済み、あるいは、使用するにしても使用量を低減でき、リン含有鋼を安価に製造できる。
(Action / Effect)
According to the configuration of the refining treatment method of the invention according to claim 5, the phosphoric acid contained in the sewage sludge carbide obtained by carbonizing the sewage sludge is effectively used, and the content is adjusted to cope with the production of phosphorus-containing steel. can do.
Therefore, when manufacturing phosphorus-containing steel, it is not necessary to use phosphorus, or even if it is used, the amount of use can be reduced, and phosphorus-containing steel can be manufactured at low cost.

以上の説明から明らかなように、請求項1に係る発明の有機性廃棄物を利用した焼結物によれば、有機性廃棄物を炭化処理して生成させた混合物中の酸化カルシウムが焼結の際にガラス相を形成し、それを焼結剤に利用して鉄鉱石の粉鉱石を造粒して焼き固めることができる。
したがって、焼結の際に、外部からの加熱によって焼き固め、炭化物を燃焼させないから、その炭化物を高炉での処理に際しての燃料として利用することができるとともに、炭化物中の炭素が鉄鉱石中の酸素と結合して二酸化炭素となることで還元剤として利用でき、焼結処理において、従来のような粉コークスやその代替品としての炭化物を用いずに、各種処理で発生する可燃性ガスや、都市ガスなどの外部燃料、更には排熱を利用するなど、各種の加熱熱源を用いることができ、焼結処理での熱エネルギー面での自由度を高めるとともに炭化物を高炉での燃料および還元剤として利用し、高炉での処理に際してのコークスの使用量を減少し、有機性廃棄物を利用して精錬処理を行う上で燃料費を安価にできる焼結物を提供できる。
As apparent from the above description, according to the sintered product using the organic waste of the invention according to claim 1, calcium oxide in the mixture produced by carbonizing the organic waste is sintered. In this case, a glass phase is formed, and the iron ore powder ore can be granulated and baked by using it as a sintering agent.
Therefore, during sintering, the carbides are not baked and hardened by heating from the outside, so that the carbides can be used as a fuel for processing in the blast furnace, and the carbon in the carbides is oxygen in the iron ore. It can be used as a reducing agent by combining with carbon dioxide and can be used as a reducing agent. In the sintering process, combustible gas generated in various processes without using conventional powder coke and carbide as an alternative, and city Various heating heat sources can be used, such as using external fuel such as gas, and exhaust heat, increasing the degree of freedom in terms of thermal energy in the sintering process, and using carbide as fuel and reducing agent in the blast furnace It is possible to provide a sintered product that can reduce the amount of coke used in processing in a blast furnace and reduce the fuel cost when performing refining processing using organic waste.

次に、本発明の実施例を図面に基づいて詳細に説明する。   Next, embodiments of the present invention will be described in detail with reference to the drawings.

図1は、本発明に係る有機性廃棄物を利用した焼結物の製造方法および精錬処理方法を示す実施例のフローシートであり、ロータリーキルンなどの高温加熱用の炭化装置1に、乾燥装置2と燃焼装置3とが接続されている。乾燥装置2には、雑多な一般ごみ、生活排水を処理した下水汚泥、産業廃棄物などの酸化カルシウムを含んだ有機性廃棄物が投入され、その乾燥後の有機性廃棄物が炭化装置1に投入されるようになっている。   FIG. 1 is a flow sheet of an embodiment showing a method for producing a sintered product and a refining treatment method using an organic waste according to the present invention. A carbonizing apparatus 1 for high-temperature heating such as a rotary kiln is provided with a drying apparatus 2. And the combustion device 3 are connected. The drying apparatus 2 is charged with organic waste containing calcium oxide such as miscellaneous general waste, sewage sludge treated with domestic wastewater, and industrial waste, and the organic waste after drying is input to the carbonization apparatus 1. It comes to be thrown in.

燃焼装置3には、都市ガス等の外部燃料、廃棄物焼却施設で発生した可燃性ガス、炭化装置1での炭化処理で発生する未燃炭素のガス成分、外熱型焼結炉4で発生する未燃炭素のガス成分、下水処理場で発生した消化ガスなどが供給され、空気予熱器5を介して供給される燃焼用空気とによって燃焼されるように構成されている。燃焼装置3からの燃焼排ガス、更には、焼却施設や自家発電設備で発生した排ガスなどが、炭化装置1および外熱型焼結炉4での加熱処理における熱源および雰囲気ガスとして炭化装置1および外熱型焼結炉4に供給されるようになっている。   Combustion device 3 includes an external fuel such as city gas, a combustible gas generated in a waste incineration facility, a gas component of unburned carbon generated by carbonization in carbonization device 1, and generated in external heating type sintering furnace 4. The gas component of the unburned carbon, the digestion gas generated in the sewage treatment plant, etc. are supplied and combusted by the combustion air supplied through the air preheater 5. Combustion exhaust gas from the combustion apparatus 3 and further exhaust gas generated in an incineration facility or in-house power generation facility are used as a heat source and an atmospheric gas in the heat treatment in the carbonization apparatus 1 and the external heat sintering furnace 4, and the carbonization apparatus 1 and the outside It is supplied to the thermal sintering furnace 4.

炭化装置1には、廃棄物焼却施設で発生した可燃性ガス、炭化処理で発生した可燃性ガスの燃焼設備(上記燃焼装置3をも含む)で発生した蒸気や自家発電設備の廃熱回収用ボイラからの蒸気などが供給され、酸化カルシウムを含んだ有機性廃棄物を温度400〜700℃で蒸し焼き(炭化処理)し、揮発成分を放出して炭化物と酸化カルシウムとの混合物(請求項4の第1の混合物に相当する)が得られるように構成されている。   The carbonization device 1 is used for recovering waste heat from combustible gas generated at a waste incineration facility, combustion equipment for combustible gas generated by carbonization (including the combustion device 3), and private power generation equipment. Steam from an boiler is supplied, and organic waste containing calcium oxide is steamed (carbonized) at a temperature of 400 to 700 ° C. to release volatile components and a mixture of carbide and calcium oxide (claim 4). Corresponding to the first mixture).

空気予熱器5には、自家発電設備で発生した排ガスの一部、更には、炭化装置1および外熱型焼結炉4で発生した廃熱などが供給され、各種の排熱によって、炭化処理における燃焼排ガス生成用の燃焼装置3に対する燃焼用空気を加熱するように構成されている。   The air preheater 5 is supplied with a part of the exhaust gas generated in the private power generation facility, and further, waste heat generated in the carbonization apparatus 1 and the external heating type sintering furnace 4. The combustion air for the combustion apparatus 3 for generating combustion exhaust gas in is heated.

炭化装置1で得られた炭化物と酸化カルシウムとの混合物と、鉄鉱石の粉鉱石とが、ロータリーキルンなどの高温加熱用の外熱型焼結炉4に供給されるようになっている。外熱型焼結炉4では、燃焼装置3からの燃焼排ガスなどの熱風によって外部から900℃以上で加熱処理し、炭化物と酸化カルシウムの混合物と鉄鉱石の粉鉱石とを焼き固め、炭化物と焼結鉱とが混合した焼結物(請求項4の第2の混合物に相当する)を生成するように構成されている。以上の構成までが、本発明の焼結物の製造方法に相当する。   A mixture of carbide and calcium oxide obtained in the carbonization apparatus 1 and iron ore powder ore are supplied to an external heating type sintering furnace 4 for high-temperature heating such as a rotary kiln. In the external heating type sintering furnace 4, heat treatment is performed at 900 ° C. or more from the outside with hot air such as combustion exhaust gas from the combustion device 3, and a mixture of carbide and calcium oxide and iron ore powder ore are baked and hardened, and the carbide and A sintered product (corresponding to the second mixture of claim 4) mixed with the ore is formed. Up to the above configuration corresponds to the method for producing a sintered product of the present invention.

外熱型焼結炉4で生成された炭化物と焼結鉱との混合物である焼結物と、コークスとが高炉に供給され、高炉において、1000〜1200℃の熱風を吹き込むことにより、炭化物およびコークス中の炭素と熱風とが反応して還元ガスが生成され、還元ガスが焼結鉱中の酸素と反応し、二酸化炭素となることで、還元溶融が進み、銑鉄を製造するように構成されている。同時に酸化カルシウム等はスラグとなり、炉床部(図示せず)から炉外に排出される。   A sintered product, which is a mixture of carbide and sintered ore generated in the external heating type sintering furnace 4, and coke are supplied to the blast furnace, and in the blast furnace, hot air of 1000 to 1200 ° C. is blown to blow the carbide and The carbon in the coke reacts with the hot air to produce reducing gas, and the reducing gas reacts with oxygen in the sintered ore to become carbon dioxide, so that reductive melting proceeds and pig iron is produced. ing. At the same time, calcium oxide or the like becomes slag and is discharged out of the furnace from the hearth (not shown).

空気予熱器5を経た排ガスは、排ガス処理装置6に供給され、脱硫や脱硝処理などの無害化処理を施されるとともに塵埃を集塵装置(図示せず)で回収した後に、煙突7により大気中に放出されるようになっている。   The exhaust gas that has passed through the air preheater 5 is supplied to the exhaust gas treatment device 6, subjected to detoxification treatment such as desulfurization and denitration treatment, and dust is collected by a dust collector (not shown), and then is discharged to the atmosphere by the chimney 7. To be released inside.

上述した酸化カルシウムを含んだ有機性廃棄物として、下水汚泥を例にして、その原料、炭化物および焼結物の組成(いずれも重量%である)を挙げれば、次表の(a)に示す通りである。また、一般ごみを例にして、その炭化物および焼結物の組成(いずれも重量%である)を挙げれば、次表の(b)に示す通りである。

Figure 2007254863
As an example of organic waste containing calcium oxide, sewage sludge is taken as an example, and the composition of raw materials, carbides, and sintered products (all are in weight percent) is shown in (a) of the following table. Street. Taking the general waste as an example, the composition of the carbide and sintered product (both are in% by weight) is as shown in (b) of the following table.
Figure 2007254863

通常、下水汚泥等の含水率の高い物質は、炭化物とするための加熱処理をする前処理として、脱水処理とその後の乾燥処理等が行なわれ、この前処理によって含水率を40%以下にしてから加熱処理される。表中の下水汚泥を例にとると、脱水処理で含水率80%の脱水ケーキにした後、乾燥処理によって含水率30%の乾燥汚泥にし、その後、これを原料として加熱処理で炭化物を得ている。
また、一般ごみで、厨芥ごみ等の含水率50〜80%の原料にあっては、乾燥処理によって含水率を40%以下に低下させた後、加熱処理で炭化物を得るようにされる。
表中において、炭化物および焼結物中におけるカルシウムは主として酸化カルシウムある。
Usually, substances having a high water content such as sewage sludge are subjected to a dehydration process and a subsequent drying process as a pre-treatment for heat treatment to obtain a carbide, and this pre-treatment reduces the water content to 40% or less. Heat treatment. Taking the sewage sludge in the table as an example, a dehydrated cake with a moisture content of 80% is obtained by dehydration treatment, and then dried to a dry sludge with a moisture content of 30%, and then this is used as a raw material to obtain a carbide by heat treatment. Yes.
Moreover, in the case of raw materials having a moisture content of 50 to 80% such as garbage, the carbide is obtained by heat treatment after the moisture content is reduced to 40% or less by drying treatment.
In the table, the calcium in the carbide and sintered product is mainly calcium oxide.

以上の構成により、酸化カルシウムを含んだ有機性廃棄物を炭化装置1で炭化処理して炭化物と酸化カルシウムとの混合物を生成させ、その混合物と鉄鉱石の粉鉱石とを外熱型焼結炉4で加熱処理して炭化物と焼結鉱とが混合した焼結物を製造し、更に、その焼結物とコークスとを高炉で加熱処理して銑鉄を製造できるようになっている。   With the above configuration, the organic waste containing calcium oxide is carbonized by the carbonization apparatus 1 to form a mixture of carbide and calcium oxide, and the mixture and the iron ore powder ore are externally heated. A sintered product in which carbide and sintered ore are mixed is manufactured by heat treatment in No. 4, and then the sintered product and coke are heated in a blast furnace to produce pig iron.

上述のように、酸化カルシウムの濃度が高い一般ごみを炭化処理した炭化物を焼結剤として用いることで、ケイ酸や酸化アルミニウムの含有量が高い焼結鉱でも融液の流動性が維持され、これまで需要の低かったケイ酸および酸化アルミニウムの含有量の高い微粉鉄鉱石も製鋼材料として利用することが可能となる利点を有している。   As described above, by using a carbide obtained by carbonizing general waste having a high calcium oxide concentration as a sintering agent, the fluidity of the melt is maintained even in sintered ore having a high content of silicic acid and aluminum oxide, Fine iron ore having a high content of silicic acid and aluminum oxide, which has been low in demand, has an advantage that it can be used as a steelmaking material.

例えば、鉄鉱石の粉鉱石100トンに対し、約5トン以上の酸化カルシウムがあれば融液の流動性を確保でき、ケイ酸および酸化アルミニウムが存在しても一定の製品歩留を確保することができる。
有機性廃棄物を炭化処理して得られた炭化物10トン中には、上記表から明らかなように、多い場合に約1トンの酸化カルシウムが含有しており、鉄鉱石の粉鉱石100トンに対し、約50トンの炭化物があれば有用な焼結物を得ることができる。
For example, with respect to 100 tons of iron ore powder ore, the fluidity of the melt can be secured if there is about 5 tons or more of calcium oxide, and a certain product yield can be secured even if silicic acid and aluminum oxide are present. Can do.
As is clear from the above table, about 10 tons of calcium oxide is contained in 10 tons of carbide obtained by carbonizing organic waste, and in 100 tons of iron ore powder ore. On the other hand, if there is about 50 tons of carbide, a useful sintered product can be obtained.

一般的な鉄鋼の精錬処理方法である高炉法では、銑鉄100トンを製造するために、約10トンのコークスが消費される。焼結物の炭化物50トン中に存在する炭素は10〜50重量%であり、この炭素を燃料および還元剤として消費することで、投入するコークスの量を削減できる。特に、鉄鉱石の粉鉱石を酸化カルシウムのみで焼結した後コークスを点火する方法では、焼結鉱が鉱石のみで構成されるために熱量が低くなり、その結果、歩留が低下する問題点があるのに対し、炭化物を焼結剤に用いることで、歩留の向上も期待できる。   In the blast furnace method, which is a general steel refining method, about 10 tons of coke is consumed to produce 100 tons of pig iron. The carbon present in 50 tons of sintered carbide is 10 to 50% by weight, and the amount of coke to be charged can be reduced by consuming this carbon as a fuel and a reducing agent. In particular, in the method of igniting coke after sintering iron ore powder ore with only calcium oxide, the amount of heat is low because the sintered ore is composed only of ore, resulting in a decrease in yield. On the other hand, the yield can be improved by using carbide as a sintering agent.

具体的な配合の割合として、酸化カルシウムが5〜30重量%となることが望ましい。5重量%未満の場合、造粒が抑制され、焼結剤として十分に機能せず、一方、30重量%を超えると、焼結鉱の熱量が低下し、歩留を低下させるからである。
5〜30重量%であれば、ケイ酸および酸化アルミニウムは共に鉄酸化物粒子間の結合相を増加させるため、酸化カルシウムのみで焼結させる場合に懸念される、還元粉化性を抑えることができる。
一般ごみの焼結物中の酸化カルシウムは5〜20重量%程度と予想されるので、鉄鉱石の粉鉱石100トンに対して配合する焼結物は20〜100トンとなる。
As a specific blending ratio, calcium oxide is desirably 5 to 30% by weight. If it is less than 5% by weight, the granulation is suppressed and it does not function sufficiently as a sintering agent. On the other hand, if it exceeds 30% by weight, the calorie of the sintered ore is lowered and the yield is lowered.
If it is 5 to 30% by weight, both silicic acid and aluminum oxide increase the binding phase between the iron oxide particles, so that the reduced powdering property, which is a concern when sintered only with calcium oxide, can be suppressed. it can.
Since calcium oxide in the sintered product of general waste is expected to be about 5 to 20% by weight, the sintered product to be blended with respect to 100 ton of iron ore powder ore is 20 to 100 ton.

また、リン酸を豊富に含有する下水汚泥炭化物を下水汚泥以外の有機性廃棄物を炭化処理した炭化物に一定量含有させ、焼結物中のリン酸含有率を0.01〜0.1重量%とすることで、伸びを維持したまま一定の強度を確保できるリン含有鋼を製造することができる。また、炭化処理温度を1000〜1400℃とすることで、リン酸を黄リンとして回収できるので、炭化処理によりリン酸含有量を調整することも可能である。   Further, a certain amount of sewage sludge carbide containing abundant phosphoric acid is contained in a carbonized carbonized organic waste other than sewage sludge, and the phosphoric acid content in the sintered product is 0.01 to 0.1 weight. By setting it as%, it is possible to produce phosphorus-containing steel that can ensure a certain strength while maintaining elongation. Moreover, since it can collect | recover phosphoric acid as yellow phosphorus by setting carbonization temperature to 1000-1400 degreeC, it is also possible to adjust phosphoric acid content by carbonization.

本発明に係る有機性廃棄物を利用した焼結物の製造方法および精錬処理を示す実施例のフローシートである。It is the flow sheet of the Example which shows the manufacturing method and refining process of the sintered compact using the organic waste which concerns on this invention.

符号の説明Explanation of symbols

1…炭化装置
4…外熱型焼結炉

DESCRIPTION OF SYMBOLS 1 ... Carbonization apparatus 4 ... External heating type sintering furnace

Claims (5)

酸化カルシウムを含んだ有機性廃棄物を炭化処理して生成させた炭化物と酸化カルシウムとの混合物と、鉄鉱石の粉鉱石とが焼き固めて生成されて成ることを特徴とする有機性廃棄物を利用した焼結物。   An organic waste comprising a mixture of carbide and calcium oxide produced by carbonizing an organic waste containing calcium oxide and iron ore powder ore is baked and solidified. Used sintered product. 酸化カルシウムを含んだ有機性廃棄物を炭化処理して炭化物と酸化カルシウムとの混合物を生成させ、前記混合物と鉄鉱石の粉鉱石とを外熱型焼結炉で焼き固めることを特徴とする有機性廃棄物を利用した焼結物の製造方法。   An organic waste characterized by carbonizing an organic waste containing calcium oxide to form a mixture of carbide and calcium oxide, and baking the mixture and iron ore powder ore in an externally heated sintering furnace For manufacturing sintered products using toxic waste. 請求項2に記載の有機性廃棄物を利用した焼結物の製造方法において、
炭化処理で発生する未燃炭素のガス成分を外熱型焼結炉の加熱熱源の燃料として用いるものである有機性廃棄物を利用した焼結物の製造方法。
In the manufacturing method of the sintered compact using the organic waste of Claim 2,
A method for producing a sintered product using organic waste, in which a gas component of unburned carbon generated by carbonization is used as a fuel for a heating heat source of an external heating type sintering furnace.
酸化カルシウムを含んだ有機性廃棄物を炭化処理して炭化物と酸化カルシウムとの第1の混合物を生成させ、前記第1の混合物と鉄鉱石の粉鉱石とを外熱型焼結炉で加熱処理して炭化物と焼結鉱との第2の混合物を生成させ、前記第2の混合物とコークスとを高炉で加熱処理して銑鉄を製造することを特徴とする精錬処理方法。   An organic waste containing calcium oxide is carbonized to produce a first mixture of carbide and calcium oxide, and the first mixture and iron ore powder ore are heat-treated in an externally heated sintering furnace. Then, a second mixture of carbide and sintered ore is produced, and the second mixture and coke are heated in a blast furnace to produce pig iron. 請求項4に記載の精錬処理方法において、
第1の混合物が、下水汚泥を炭化処理した下水汚泥炭化物と、下水汚泥以外の有機性廃棄物を炭化処理した炭化物とから成り、前記下水汚泥炭化物の含有量を調整するものである精錬処理方法。

In the refining processing method according to claim 4,
A refining treatment method in which the first mixture is composed of sewage sludge carbide obtained by carbonizing sewage sludge and carbide obtained by carbonizing organic waste other than sewage sludge, and adjusting the content of the sewage sludge carbide. .

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