JP5179038B2 - Method for treating hydrogen-generated oil mud and solid fuel - Google Patents

Method for treating hydrogen-generated oil mud and solid fuel Download PDF

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Publication number
JP5179038B2
JP5179038B2 JP2006274043A JP2006274043A JP5179038B2 JP 5179038 B2 JP5179038 B2 JP 5179038B2 JP 2006274043 A JP2006274043 A JP 2006274043A JP 2006274043 A JP2006274043 A JP 2006274043A JP 5179038 B2 JP5179038 B2 JP 5179038B2
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hydrogen
oil
waste
oil mud
powder
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JP2008086974A (en
Inventor
一志 和泉
規允 西島
義正 村岡
博幸 高野
浩文 森
誠 鏡田
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Taiheiyo Cement Corp
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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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-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
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/78Recycling of wood or furniture waste

Description

本発明は、水素発生油泥の処理方法に関し、特に、水素の発生を低減させる水素発生油
泥の処理方法、及び該処理方法によって得られた固体燃料に関するものである。
The present invention relates to a method for treating hydrogen-generated oil mud, and more particularly, to a method for treating hydrogen-generated oil mud that reduces the generation of hydrogen, and a solid fuel obtained by the method.

シリコンウエハーは、半導体デバイスや太陽光電池等の部材として有用であり、その需要は年々増大しつつある。かかるシリコンウエハーは、高純度シリコンの結晶体からウエハー状に切り出すことにより製造されるが、切断機の性能等の観点から、近年においてはワイヤソーによる切り出しが主流になりつつある。   Silicon wafers are useful as members for semiconductor devices, solar cells and the like, and their demand is increasing year by year. Such a silicon wafer is manufactured by cutting into a wafer form from a crystal of high-purity silicon, but in recent years, cutting with a wire saw is becoming mainstream from the viewpoint of the performance of a cutting machine.

このワイヤソーによる切り出しにおいては、切削用媒体として、通常平均粒径10μm
〜50μmの炭化珪素研削粒と鉱油又は水溶液とを含有するワイヤソーオイルが用いられ
る。このワイヤソーオイルは、使用を繰り返すことにより研削粒の摩耗、シリコン削分の
増加等により、切削能力が低下し、使用できなくなる。
そして、このように使用できなくなった廃ワイヤソーオイルは、現在においては、その
大部分が焼却され、産業廃棄物として処理されている。
In cutting with this wire saw, the average particle diameter is usually 10 μm as a cutting medium.
Wire saw oil containing ˜50 μm silicon carbide abrasive grains and mineral oil or aqueous solution is used. The wire saw oil cannot be used because its cutting ability is reduced due to wear of abrasive grains, an increase in silicon scraping, etc. due to repeated use.
And now, most of the waste wire saw oil that can no longer be used is incinerated and treated as industrial waste.

また、機械加工工場では、多数台の切削、研削若しくは研磨を行う装置を運転して金属
加工を行っているが、該金属加工の工程ではワークを冷却、潤滑するために多量の切削油
、研削油、研磨油を使用している。そして、これらの切削油等も循環使用され、劣化した
ものは抜き出され、廃切削油、廃研削油、廃研磨油としてその大部分はやはり焼却処分さ
れているのが現状である。
Moreover, in a machining factory, metal processing is performed by operating a large number of cutting, grinding, or polishing apparatuses. In the metal processing process, a large amount of cutting oil and grinding are used to cool and lubricate the workpiece. Oil and polishing oil are used. These cutting oils are also circulated and used, and the deteriorated ones are extracted, and most of them are incinerated as waste cutting oil, waste grinding oil and waste polishing oil.

ここで、上記した廃ワイヤソーオイル、廃切削油等の油泥は、高いエネルギーを有する
ため、産業廃棄物として焼却処分せずに、燃料として有効利用することが期待される。
しかし、一般に油泥は、高い粘稠性を有しているものや、常温で流動性がないものや、
固形分が沈降分離し固着するものなどがあるため、管路を介した輸送時等におけるハンド
リング性が悪く、燃料としての取り扱いが困難である。
Here, since oil mud such as the above-described waste wire saw oil and waste cutting oil has high energy, it is expected to be effectively used as fuel without being incinerated as industrial waste.
However, in general, oil mud has a high viscosity, does not flow at room temperature,
Since some solid matter settles and settles, it is difficult to handle as a fuel due to poor handling properties during transportation through a pipeline.

そこで、近年欧州では、原油スラッジ等の油泥を単独で用いるのではなく、該油泥とお
が屑とを混合して固体燃料とし、セメントキルンで代替燃料として使用することが提案さ
れ、また我が国でも、同様な固体燃料の製造方法が提案されている(例えば、特許文献1
,2,3等)。
Therefore, in recent years, in Europe, it has been proposed that oil sludge such as crude oil sludge is not used alone, but the oil mud and sawdust are mixed to form a solid fuel and used as an alternative fuel in a cement kiln. Have been proposed (for example, Patent Document 1).
, 2, 3 etc.).

特開昭54−39401号公報JP-A-54-39401 特開2002−323213号公報JP 2002-323213 A 特開2006−169376号公報JP 2006-169376 A

しかしながら、シリコンウエハーの切り出しに使用された廃ワイヤソーオイルは、多量
のシリコン粒子を含有していると共に、ワイヤソーの磨滅等に起因する鉄等の金属粒子も
含有していることから、これらのシリコン粒子及び/又は鉄等の金属粒子が水と反応して
例えば下記の反応式によって多量の水素が発生する憂いがある。
Si+2OH-+H2O → SiO3 2-+2H2
金属 + 酸 → 金属化合物 + 水素↑
また、廃切削油、廃研削油、廃研磨油も、多量のアルミ粒子や鉄等の金属粒子を含有して
いることから、同じく水素の発生が懸念される。
However, the waste wire saw oil used for cutting silicon wafers contains a large amount of silicon particles and also contains metal particles such as iron resulting from wear of the wire saw. There is a concern that metal particles such as iron react with water and a large amount of hydrogen is generated by the following reaction formula, for example.
Si + 2OH + H 2 O → SiO 3 2− + 2H 2
Metal + Acid → Metal Compound + Hydrogen ↑
Moreover, since waste cutting oil, waste grinding oil, and waste polishing oil contain a large amount of metal particles such as aluminum particles and iron, there is a concern about the generation of hydrogen.

上記のような水素の発生が懸念される廃ワイヤソーオイル、廃切削油等の油泥(本明細
書では、このような油泥を『水素発生油泥』と言う。)は、発生した水素への引火、爆発
のおそれがあることから、その輸送、貯留等の取扱いが特に困難であり、従来においては
その有効的な利用方法が見出されていなかった。
Oil mud such as waste wire saw oil, waste cutting oil and the like that are concerned about the generation of hydrogen as described above (in the present specification, such oil mud is referred to as “hydrogen generating oil mud”) is ignited to the generated hydrogen, Since there is a risk of explosion, handling such as transportation and storage is particularly difficult, and no effective use method has been found in the past.

本発明は、上述した背景技術が有する課題に鑑み成されたものであって、その目的は、
廃ワイヤソーオイル、廃切削油等の水素発生油泥からの水素発生量を低減させ、輸送、貯
留等の取扱性を良好なものとする水素発生油泥の処理方法、及び該処理方法によって得ら
れた取扱性の良好な固体燃料を提供することにある。
The present invention has been made in view of the problems of the background art described above, and its purpose is as follows.
A method for treating hydrogen-generated oil mud, which reduces the amount of hydrogen generated from hydrogen-generated oil mud such as waste wire saw oil and waste cutting oil, and improves handling, such as transportation and storage, and the handling obtained by the treatment method It is to provide a solid fuel with good properties.

本発明者等は、上記した課題を解決すべく鋭意研究を進めた結果、水素発生油泥に廃畳の粉砕物等のバイオマスを混合すれば、混合したバイオマスが水素発生油泥中の液分を吸収し、ハンドリング性が良好となると共に、水素の発生量を低減できることを見出し、本発明を完成した。
すなわち、本発明は、次の〔1〕〜〔6〕の水素発生油泥の処理方法及び固体燃料を提供するものである。
〔1〕平均粒径0.5mm以上で、かつ最大粒径10mm以下のバイオマス40〜95質量部と、前記バイオマスの平均粒径の1/2以下の平均粒径を有する有機質粉体60〜5質量部(但し、バイオマス+有機質粉体=100質量部)と、水素発生油泥30〜300質量部とを混合する水素発生油泥の処理方法。
〔2〕水素発生油泥が、水または水素原子含有化合物の還元によって水素を発生する、液状またはスラッジ状の油泥である前記〔1〕の水素発生油泥の処理方法。
〔3〕水素発生油泥が、シリコン粒子及び/又はアルミ粒子や金属粒子を含有した、廃ワイヤソーオイル、廃切削油、廃研削油、廃研磨油のいずれか一種以上である前記〔1〕の水素発生油泥の処理方法。
〔4〕バイオマスが、廃畳の破砕物、木材チップ、木粉、おが屑、紙屑のいずれか一種以上である前記〔1〕〜〔3〕のいずれかの水素発生油泥の処理方法。
〔5〕有機質粉体が、トナー、重油灰、微粉炭、活性炭粉末、肉骨粉、廃プラスチック粉末、紙粉、有機蒸留残渣粉末のいずれか一種以上である前記〔1〕〜〔4〕のいずれかの水素発生油泥の処理方法。
〔6〕前記〔1〕〜〔5〕のいずれかの水素発生油泥の処理方法によって得られた固体燃料。
As a result of intensive studies to solve the above-mentioned problems, the present inventors have mixed biomass such as crushed waste tatami into the hydrogen generating oil mud, and the mixed biomass absorbs the liquid content in the hydrogen generating oil mud. As a result, the inventors have found that the handling property is improved and the amount of hydrogen generated can be reduced, and the present invention has been completed.
That is, the present invention provides the following [1] to [6] hydrogen-generating oil mud treatment method and solid fuel.
[1] 40 to 95 parts by mass of biomass having an average particle size of 0.5 mm or more and a maximum particle size of 10 mm or less, and organic powders 60 to 5 having an average particle size of 1/2 or less of the average particle size of the biomass The processing method of the hydrogen generation oil mud which mixes a mass part (however, biomass + organic powder = 100 mass parts) and 30-300 mass parts of hydrogen generation oil mud.
[2] The method of treating a hydrogen-generating oil mud according to [1], wherein the hydrogen-generating oil mud is a liquid or sludge-like oil mud that generates hydrogen by reduction of water or a hydrogen atom-containing compound.
[3] Hydrogen according to [1], wherein the hydrogen-generating oil mud is at least one of waste wire saw oil, waste cutting oil, waste grinding oil, and waste polishing oil containing silicon particles and / or aluminum particles and metal particles. Treatment method of generated oil mud.
[4] The method for treating hydrogen-generated oil mud according to any one of [1] to [3], wherein the biomass is one or more of crushed waste timber, wood chips, wood flour, sawdust, and paper waste.
[5] Any of the above [1] to [4], wherein the organic powder is any one or more of toner, heavy oil ash, pulverized coal, activated carbon powder, meat and bone powder, waste plastic powder, paper powder, and organic distillation residue powder A method for treating such hydrogen-generated oil mud.
[6] A solid fuel obtained by the method for treating hydrogen-producing oil mud according to any one of [1] to [5].

上記した本発明によれば、水素発生油泥に混合したバイオマスが水素発生油泥中の液分
(油分及び水分)を吸収し、ハンドリング性が良好となると共に、該油泥中に存在するシ
リコン粒子及び/又は鉄等の金属粒子と水とが反応すること等によって発生する水素量を
低減でき、輸送、貯留等の取扱性及び安全性が良好な混合物に水素発生油泥を処理するこ
とができる。
そのため、従来においては廃棄処分されていた廃ワイヤソーオイル、廃切削油等の水素発
生油泥を、資源として有効に利用することが可能となる。
According to the present invention described above, the biomass mixed in the hydrogen-generating oil mud absorbs liquid components (oil and moisture) in the hydrogen-generating oil mud, the handling properties are improved, and the silicon particles present in the oil mud and / or Alternatively, the amount of hydrogen generated by the reaction of metal particles such as iron with water can be reduced, and the hydrogen-generating oil mud can be treated into a mixture having good handling and safety such as transportation and storage.
Therefore, it is possible to effectively use hydrogen-generated oil mud such as waste wire saw oil and waste cutting oil, which has been disposed of in the past, as a resource.

以下、上記した本発明に係る水素発生油泥の処理方法、及び該処理方法によって得られ
た固体燃料を詳細に説明する。
Hereinafter, the method for treating the hydrogen-generated oil mud according to the present invention and the solid fuel obtained by the method will be described in detail.

〔水素発生油泥〕
本発明において水素発生油泥とは、水又は水素原子含有化合物の還元によって水素を発
生する、液状又はスラッジ状の油泥をいう。具体的には、シリコンウエハーの切り出しに
使用されたシリコン粒子を含有する廃ワイヤソーオイル、各種金属工作機械においてワー
クの冷却、潤滑等に使用されたアルミ粒子や金属粒子を含有する廃切削油、廃研削油、廃
研磨油等が挙げられ、これらを単独でも、またこれらの二種以上を混ぜた物でも、更には
これらと他の油泥、例えば再生重油、廃溶剤、原油スラッジ、軽油残渣等を混ぜた物であ
ってもよい。
上記した中でも、シリコン粒子を含有した廃ワイヤソーオイルは、近年の半導体デイバ
イスや太陽光電池等の部材として有用であるシリコンウエハーの需要の増大から、大量に
発生しており、その処理が急務になっていると共に、アルカリ性、酸性の両状態において
水素の発生が懸念される取扱いの特に困難な油泥であることから、本発明において、水素
発生油泥として好適に用いられる。
[Hydrogen generating oil mud]
In the present invention, the hydrogen-generating oil mud refers to a liquid or sludge-like oil mud that generates hydrogen by reducing water or a hydrogen atom-containing compound. Specifically, waste wire saw oil containing silicon particles used for cutting silicon wafers, waste cutting oil containing aluminum particles and metal particles used for cooling and lubrication of workpieces in various metal machine tools, waste Grinding oil, waste polishing oil, etc. can be mentioned. These can be used alone or as a mixture of two or more of these, and also with other oil mud such as recycled heavy oil, waste solvent, crude oil sludge, diesel oil residue, etc. It may be a mixture.
Among the above, waste wire saw oil containing silicon particles has been generated in large quantities due to the recent increase in demand for silicon wafers that are useful as members for semiconductor devices, solar cells, etc., and its treatment has become an urgent task. In addition, since it is an oil mud that is particularly difficult to handle, the generation of hydrogen is concerned in both alkaline and acidic states, it is preferably used as the hydrogen generating oil mud in the present invention.

〔バイオマス〕
バイオマスの例としては、畳(使用済みの廃畳)の破砕物、木材チップ(例えば、建設
廃木材の破砕物)、木粉、おが屑、紙屑等が挙げられる。
なお、本発明においてバイオマスとは、燃料等として利用可能な、生物由来の有機質資
源(ただし、化石燃料を除く。)の総称をいう。
〔biomass〕
Examples of biomass include crushed tatami (used waste tatami), wood chips (for example, crushed trash from construction waste), wood flour, sawdust, and paper waste.
In the present invention, biomass refers to a generic name of biological organic resources (excluding fossil fuels) that can be used as fuel.

上記畳の破砕物の材料となる廃畳は、植物性の材料を少なくとも部分的に含むものであ
ればよく、具体的には、稲藁を畳床の材料とする本畳のみならず、ポリスチレンフォーム
板(ポリスチレン樹脂組成物に発泡剤を添加して膨張させて形成した板状の成形体)及び
インシュレーションボード(例えば、湿式法では、木材を水中で解砕し、接着剤等を加え
て抄造した後、乾燥して形成された軟質繊維板)を畳床の材料とする建材畳や、稲藁、ポ
リスチレンフォーム板を畳床の材料とする藁サンド畳も含む。
上記木材チップは、最大粒径(篩の残分が5質量%以内となる目開き寸法)が5mmを
超え、10mm以下である木材の破砕物または粉砕物をいう。
上記木粉とは、最大粒径(篩の残分が5質量%以内となる目開き寸法)が5mm以下で
ある木材の粉砕物をいう。
また、上記おが屑は、通常、0.5〜5mm程度の粒度分布を有するものである。上記
紙屑としては、例えばシュレッダー切断物等が用いられる。
The waste tatami used as the material of the crushed tatami mat may be any material as long as it contains at least a part of plant material. Specifically, not only the main tatami mat that uses rice straw as a tatami floor material, but also polystyrene. Foam board (plate-like molded body formed by adding a foaming agent to a polystyrene resin composition and expanding) and an insulation board (for example, in the wet method, wood is crushed in water, and an adhesive is added. Also included are building material tatami mats, which are made from a soft fiberboard that has been dried after being made, and tatami flooring materials, and paddy sand tatami mats, which are made from rice straw and polystyrene foam plates.
The above-mentioned wood chip refers to a crushed or crushed product of wood having a maximum particle size (mesh size with a sieve residue within 5% by mass) exceeding 5 mm and 10 mm or less.
The above-mentioned wood powder refers to a pulverized product of wood having a maximum particle size (a mesh size with a sieve residue within 5% by mass) of 5 mm or less.
The sawdust usually has a particle size distribution of about 0.5 to 5 mm. As the paper waste, for example, a shredder cut product or the like is used.

上記バイオマスの平均粒径(篩の残分が50質量%以内となる目開き寸法)は、0.5mm以上であるものとする。これは、該平均粒径が0.5mm未満では、粒子系全体が微細化するため流動性、分散性が低下し、ハンドリング性の向上等の効果を得ることが困難となると共に、水素発生油泥中の液分(油分及び水分)の吸収が困難となり、水素発生量の低減効果が得られないためである
また、上記バイオマスの最大粒径(篩の残分が5質量%以内となる目開き寸法)は、10mm以下、好ましくは5mm以下、より好ましくは3mm以下である。これは、該最大粒径が10mmを超えると、例えば本発明に係る水素発生油泥の処理方法で得られた混合物を燃料としてセメントキルンのバーナーで使用する場合、火炎(フレーム)を形成しにくく、燃料が着地した後も燃焼を継続するため、セメントクリンカーの品質を低下させるおそれがある。該最大粒径を5mm以下とすれば、着地燃焼する粒体の割合が少なくなり、燃料としての使用割合を大きくすることができるので好ましい。
The average particle size of the biomass (mesh size residue sieve is within 50 wt%) is assumed to be at 0.5mm or more. This is because when the average particle size is less than 0.5 mm, the entire particle system is miniaturized, so that fluidity and dispersibility are deteriorated, and it becomes difficult to obtain an effect such as improvement in handling properties, and hydrogen generation oil mud. absorption of liquid component (oil and water) is difficult in is because can not be obtained the effect of reducing the amount of hydrogen generation.
Further, the maximum particle size of the biomass (a mesh size in which the remainder of the sieve is within 5% by mass) is 10 mm or less, preferably 5 mm or less, more preferably 3 mm or less. When the maximum particle size exceeds 10 mm, for example, when the mixture obtained by the method for treating hydrogen-generated oil mud according to the present invention is used as a fuel in a cement kiln burner, it is difficult to form a flame (frame), Since the combustion continues even after the fuel has landed, the quality of the cement clinker may be deteriorated. If the maximum particle size is 5 mm or less, the proportion of particles that land and burn is reduced, and the use rate as fuel can be increased, which is preferable.

〔他の材料〕
水素発生油泥中の液分の吸収材として、上記バイオマスの他、有機質粉体が用いられ、さらに品質を損なわない限度において、その他の材料を配合することもできる。
有機質粉体の例としては、トナー、重油灰、微粉炭、活性炭粉末、肉骨粉、廃プラスチック粉末、紙粉、有機蒸留残渣粉末等が挙げられる。これらの有機質粉体は、一種を単独で用いてもよいし、二種以上を併用してもよい。
[Other materials]
In addition to the above-mentioned biomass, organic powder is used as an absorbent material for the liquid in the hydrogen-generating oil mud, and other materials can be blended as long as the quality is not impaired.
Examples of the organic powder include toner, heavy oil ash, pulverized coal, activated carbon powder, meat and bone powder, waste plastic powder, paper powder, and organic distillation residue powder. These organic powders may be used alone or in combination of two or more.

上記トナーは、コピー機、ファクシミリ機、プリンター等の事務機器における乾式現像
剤であり、7〜11μm程度の粒径を有する粉体であり、通常、廃棄物である廃トナーが
用いられる。トナーは、非常に小さな粒径を有し、かつ粒度分布が狭いため、得られる混
合物(固体燃料)の比重の増大、及び水素発生油泥の処理量の増大に大きく寄与すること
ができ、好ましく用いられる。
上記重油灰は、1〜30μm程度の粒径を有する粉体であり、小さな粒径を有するため
、やはり、得られる混合物(固体燃料)の比重の増大、及び水素発生油泥の処理量の増大
に寄与することができるため、好ましく用いられる。
上記微粉炭は、10〜100μm程度の粒径を有する粉体であり、セメントキルン等の
焼成炉における固体燃料として知られている。
上記活性炭粉末及び肉骨粉としては、通常、1mm以下の平均粒径を有するものが用い
られる。上記廃プラスチック粉末としては、例えば、廃ペレット等が用いられる。上記紙
粉としては、例えば、サンダーダスト等が用いられる。上記有機蒸留残渣粉末としては、
例えば、フタル酸蒸留残渣等が用いられる。
The toner is a dry developer used in office equipment such as a copying machine, a facsimile machine, and a printer, and is a powder having a particle size of about 7 to 11 μm. Usually, waste toner that is waste is used. Since the toner has a very small particle size and a narrow particle size distribution, it can greatly contribute to an increase in the specific gravity of the resulting mixture (solid fuel) and an increase in the throughput of the hydrogen-generated oil mud, which is preferably used. It is done.
The above heavy oil ash is a powder having a particle size of about 1 to 30 μm and has a small particle size. Therefore, it also increases the specific gravity of the resulting mixture (solid fuel) and increases the throughput of the hydrogen generating oil mud. Since it can contribute, it is preferably used.
The pulverized coal is a powder having a particle size of about 10 to 100 μm and is known as a solid fuel in a firing furnace such as a cement kiln.
As said activated carbon powder and meat-and-bone powder, what has an average particle diameter of 1 mm or less is used normally. For example, waste pellets are used as the waste plastic powder. As the paper powder, for example, thunder dust or the like is used. As the organic distillation residue powder,
For example, phthalic acid distillation residue or the like is used.

上記有機質粉体の平均粒径は、上記バイオマスの平均粒径に対し、1/2以下、好まし
くは1/3以下である。これは、該比が1/2を超えると、バイオマスと有機質粉体との
粒径の差が小さくなり、水素発生油泥の処理量の増大、ハンドリング性の向上等の効果を
得ることが困難となる。
上記有機質粉体の中で、固定炭素で構成される活性炭粉末などでは、平均粒径が300
μmを超えると着地燃焼する粒子が増大し、セメントクリンカーの品質が低下することが
あるので、好ましくは平均粒径が300μm以下、より好ましくは100μm以下のもの
を使用する。有機質粉体の粒径の下限値は、特には限定されないが、通常、1μm以上で
ある。
The average particle size of the organic powder is ½ or less, preferably 1 / or less of the average particle size of the biomass. If the ratio exceeds 1/2, the difference in particle size between the biomass and the organic powder becomes small, and it is difficult to obtain effects such as an increase in the amount of hydrogen-generated oil mud and an improvement in handling properties. Become.
Among the above organic powders, the average particle size of the activated carbon powder composed of fixed carbon is 300.
If it exceeds μm, the number of particles that land and burn increases, and the quality of the cement clinker may deteriorate. Therefore, the average particle size is preferably 300 μm or less, more preferably 100 μm or less. The lower limit of the particle size of the organic powder is not particularly limited, but is usually 1 μm or more.

〔配合割合〕
上記各材料の配合割合は、先ず吸収材であるバイオマスと有機質粉体については、バイ
オマスと有機質粉体の質量比は、40/60〜95/5、好ましくは50/50〜80/
20である。これは、該質量比が40/60未満では、バイオマスの配合量が小さいため
、バイオマスの粒体の間隙を有機質粉体が埋めてしまい、混合物(固体燃料)の流動性が
著しく低下することがある。逆に該質量比が95/5を超えると、有機質粉体の配合量が
小さいため、混合物(固体燃料)の比重の増大等の効果を十分に得ることができない。
[Combination ratio]
The blending ratio of each of the above materials is as follows. First, for the biomass and the organic powder that are absorbents, the mass ratio of the biomass and the organic powder is 40/60 to 95/5, preferably 50/50 to 80 /
20. This is because when the mass ratio is less than 40/60, the blending amount of biomass is small, so that the organic powder fills the gaps between the granules of the biomass, and the fluidity of the mixture (solid fuel) is significantly reduced. is there. On the other hand, when the mass ratio exceeds 95/5, since the blending amount of the organic powder is small, effects such as an increase in the specific gravity of the mixture (solid fuel) cannot be obtained sufficiently.

水素発生油泥の配合量は、上記バイオマスと有機質粉体の合計量100質量部に対して
、30〜300質量部、好ましくは50〜200質量部、より好ましくは80〜150質
量部、特に好ましくは100〜140質量部である。これは、該配合量が30質量部未満
では、水素発生油泥の処理量が少なく、水素発生油泥の利用を促進しようとする本発明の
趣旨に合致しなくなる。逆に、該配合量が300質量部を超えると、水素発生油泥中の液
分、特に水分を混合したバイオマスによって吸収しきれず、水素発生の低減効果が得られ
ない場合があり、また、混合物(固体燃料)の粒子表面に油が残留して、粒子表面に光沢
及び付着性が生じ、ハンドリング性が低下することがある。
The blending amount of the hydrogen generating oil mud is 30 to 300 parts by mass, preferably 50 to 200 parts by mass, more preferably 80 to 150 parts by mass, particularly preferably 100 parts by mass of the total amount of the biomass and the organic powder. 100 to 140 parts by mass. When the blending amount is less than 30 parts by mass, the amount of hydrogen-generated oil mud is small and does not meet the gist of the present invention to promote the use of hydrogen-generated oil mud. On the other hand, when the blending amount exceeds 300 parts by mass, it may not be absorbed by the liquid component in the hydrogen-generating oil mud, particularly the biomass mixed with water, and the reduction effect of hydrogen generation may not be obtained. Oil may remain on the particle surface of the solid fuel), resulting in gloss and adhesion on the particle surface, and handling properties may be reduced.

〔混 合〕
混合は、上記各材料を、上記配合割合で混合機に投入して行うことができる。
この際、空気を混合機内に導入し、発生した水素を爆発下限濃度未満まで希釈した状態
で混合を行うことが好ましい。これは、上記した水素発生油泥とバイオマス等とを混合す
ると、特にその混合初期の段階、即ち、混合したバイオマス等が水素発生油泥中の液分を
未だ十分に吸収していない段階にあっては、水素発生油泥から水素が発生し、該水素に混
合機の回転部等で発生した火花が引火し、爆発を起こす危険があるためである。
そこで、空気を混合機内に導入し、発生した水素の濃度を爆発を起こさない濃度、即ち
爆発下限濃度である4%未満まで確実に希釈させることが好ましい。具体的な空気の混合
機内への導入量は、発生する水素の量、さらには混合機の容積、混合物の量等によって適
宜決定されるが、無料の空気で希釈するものであることから、必要十分な量の空気を、混
合機内に導入することとすればよい。
〔mixture〕
Mixing can be performed by putting the above materials into a mixer at the above mixing ratio.
At this time, it is preferable to perform mixing in a state where air is introduced into the mixer and the generated hydrogen is diluted to less than the lower explosion lower limit concentration. This is because when the above-described hydrogen generating oil mud and biomass are mixed, particularly at the initial stage of mixing, that is, at the stage where the mixed biomass or the like has not yet sufficiently absorbed the liquid in the hydrogen generating oil mud. This is because hydrogen is generated from the hydrogen-generating oil mud, and sparks generated in the rotating part of the mixer or the like are ignited and explode.
Therefore, it is preferable to introduce air into the mixer and reliably dilute the generated hydrogen concentration to a concentration that does not cause an explosion, that is, lower than the explosion lower limit concentration of 4%. The specific amount of air introduced into the mixer is appropriately determined depending on the amount of hydrogen generated, the volume of the mixer, the amount of the mixture, etc., but is necessary because it is diluted with free air. A sufficient amount of air may be introduced into the mixer.

また、混合機は、単に攪拌羽根が設けられているものではなく、その混合容器自体をも
回転する構造のものを使用することが好ましい。これは、水素発生油泥のように粘稠性の
高い材料とバイオマス等のかさ密度の低い材料とを良好に混合できると共に、容器が回転
することにより発生した水素が流動し、容器の一部に溜まることがなく、導入された空気
によって容易かつ確実に希釈させられるためである。
このような容器自体をも回転する構造の混合機としては、アイリッヒ社製のインテンシ
ブミキサー等が挙げられる。
Moreover, it is preferable to use a mixer that is not simply provided with stirring blades but also has a structure that rotates the mixing container itself. This is because a highly viscous material such as hydrogen-generating oil mud and a material with low bulk density such as biomass can be mixed well, and the hydrogen generated by the rotation of the container flows and flows into a part of the container. This is because it does not accumulate and can be easily and reliably diluted by the introduced air.
Examples of the mixer having such a structure that also rotates the container itself include an intensive mixer manufactured by Eirich.

また、混合機には、常時水素の濃度を検知する水素検出器を設け、万一所定以上の濃度
の水素が検出された場合には、直ちに混合操作を停止し、混合機内への空気導入量を増加
する構成、或いは場合によっては二酸化炭素等の不活性なガスを混合機内へ導入する構成
を更に設けることが、爆発等の事故を確実に防止できるために好ましい。
In addition, the mixer is equipped with a hydrogen detector that constantly detects the concentration of hydrogen, and if a hydrogen concentration higher than a predetermined level is detected, the mixing operation is immediately stopped and the amount of air introduced into the mixer In order to prevent accidents such as explosions with certainty, it is preferable to further provide a configuration for increasing the flow rate or a configuration for introducing an inert gas such as carbon dioxide into the mixer.

〔混合物及びその使用方法〕
上記水素発生油泥とバイオマス等との混合操作により得られた混合物は、水素発生油泥
中の液分、特に水分がバイオマス等に吸収されていることから、水素発生油泥中のシリコ
ン粒子及び/又は鉄等の金属粒子が水と反応すること等によって発生する水素の発生量を
低減でき、輸送、貯留等の安全性が高いものとなる。
上記に加えて、得られた混合物は、高いエネルギーを有する水素発生油泥と燃焼し易い
バイオマス等との混合物であることから、取扱性の良好な固体燃料として好適に用いるこ
とができるものとなる。
[Mixtures and their use]
Since the mixture obtained by the mixing operation of the hydrogen generating oil mud and the biomass is absorbed by the biomass, etc., particularly the liquid content in the hydrogen generating oil mud, the silicon particles and / or iron in the hydrogen generating oil mud are absorbed. The amount of hydrogen generated due to the reaction of metal particles such as water with water can be reduced, and the safety of transportation, storage, etc. is high.
In addition to the above, since the obtained mixture is a mixture of hydrogen-generating oil mud having high energy and easily combustible biomass, it can be suitably used as a solid fuel with good handleability.

上記した本発明に係る水素発生油泥の処理方法によって得られた混合物(固体燃料)の
使用方法の一例としては、管路を介して焼成炉内に該混合物を投入し、燃料として燃焼さ
せる使用方法が挙げられる。
ここで、焼成炉としては、クリンカを製造するためのセメントキルンや、生石灰や軽量
骨材を焼成するためのキルン等が挙げられる。
As an example of the method of using the mixture (solid fuel) obtained by the above-described method for treating hydrogen-generating oil mud according to the present invention, the method of using the mixture charged into a firing furnace via a pipe and burning as fuel Is mentioned.
Here, examples of the firing furnace include a cement kiln for producing a clinker and a kiln for firing quick lime and lightweight aggregate.

1.使用材料
(1)水素発生油泥
種々の水素発生油泥(廃ワイヤソーオイルA,B,C,D及び廃切削油A,B)の処理
を行った。
なお、廃ワイヤソーオイルA,B,C,Dはシリコン粒子及び鉄粒子を含有する水素発
生油泥で、概ね表1に示した成分組成のものであった。また、廃切削油A,Bは鉄粒子及
びアルミ粒子を含有する水素発生油泥で、概ね表1に示した成分組成のものであった。

Figure 0005179038
(2)バイオマス
本畳の破砕物を用いて処理を行った。本畳の破砕物は、次の方法にて調整した。
一軸式破砕機(ロストルの目開き:15mm)を用いて本畳を破砕し、平均粒径が0.
5mm以上であり、かつ、目開き寸法が10mmである篩の残分が5質量%以下である本
畳の破砕物を調製した。 1. Materials used (1) Hydrogen generating oil mud Various hydrogen generating oil muds (waste wire saw oil A, B, C, D and waste cutting oil A, B) were treated.
Waste wire saw oils A, B, C, and D are hydrogen-generating oil muds containing silicon particles and iron particles, and generally have the component compositions shown in Table 1. Further, the waste cutting oils A and B are hydrogen-generating oil muds containing iron particles and aluminum particles, and generally have the component compositions shown in Table 1.
Figure 0005179038
(2) Biomass Processing was performed using the crushed material of the main tatami mat. The crushed tatami mat was prepared by the following method.
The tatami mat was crushed using a uniaxial crusher (roost opening: 15 mm), and the average particle size was 0.
A crushed material of a main tatami mat having a mesh size of 5 mm or more and an opening size of 10 mm and a residue of 5% by mass or less was prepared.

2.水素発生油泥の処理
上記各種の水素発生油泥400gに、それぞれ上記本畳の破砕物400g(水素発生油
泥:本畳の破砕物の質量比1:1)を小型インテンシブミキサーに投入し、2分間撹拌す
ることにより、各種水素発生油泥とバイオマス等との混合物800gをそれぞれ得た。
2. Treatment of hydrogen-generated oil mud 400 g of the above-mentioned various hydrogen-generated oil muds are each charged with 400 g of the above-mentioned crushed material (hydrogen-generated oil mud: mass ratio of crushed material of the main tatami mat 1: 1) in a small intensive mixer and stirred for 2 minutes. As a result, 800 g of a mixture of various hydrogen generating oil muds and biomass was obtained.

3.水素発生量の測定
得られた水素発生油泥とバイオマス等との混合物について、それぞれ水素発生量を測定
した。該混合物100gをテドラーバッグに密封し、発生した水素をガスクロマトグラフ
で定量する方法にて、3日間の間にそれぞれの混合物から発生した水素量を測定した。
その測定結果を、400kgの混合物から発生する水素量に換算し、表2に実施例品とし
て記載する。
また、比較のために、バイオマス等との混合処理を行っていないそれぞれの水素発生油
泥30gについて、上記と同様の方法で水素発生量を測定した。その測定結果を、実施例
品の結果と比較するため、200kgの水素発生油泥から発生する水素量に換算し、表2
に水素発生油泥として併記する。

Figure 0005179038
3. Measurement of hydrogen generation amount The hydrogen generation amount was measured for each of the obtained hydrogen generation oil mud and biomass and the like. 100 g of the mixture was sealed in a Tedlar bag, and the amount of hydrogen generated from each mixture was measured for 3 days by a method of quantifying the generated hydrogen with a gas chromatograph.
The measurement result is converted into the amount of hydrogen generated from a 400 kg mixture, and listed in Table 2 as an example product.
For comparison, the amount of hydrogen generation was measured in the same manner as described above for each 30 g of hydrogen-generating oil mud that was not mixed with biomass or the like. In order to compare the measurement result with the result of the example product, it was converted into the amount of hydrogen generated from 200 kg of hydrogen generating oil mud, and Table 2
Is also described as hydrogen-generating oil mud.
Figure 0005179038

4.まとめ
表2から、本発明に係る水素発生油泥の処理方法によって、水素の発生量を著しく低減
できることが分かる。この本実施例で示された効果は、当然に実機にスケールアップした
場合にも有効と考えられ、このことから本発明によって、輸送、貯留等の安全性が良好な
混合物に水素発生油泥を処理することができることが分かった。
4). Summary From Table 2, it can be seen that the amount of hydrogen generated can be remarkably reduced by the method for treating hydrogen-generating oil mud according to the present invention. The effect shown in this embodiment is naturally considered to be effective even when scaled up to an actual machine. Therefore, according to the present invention, hydrogen-generated oil mud is treated into a mixture having good safety such as transportation and storage. I found out that I can do it.

Claims (6)

平均粒径0.5mm以上で、かつ最大粒径10mm以下のバイオマス40〜95質量部と、前記バイオマスの平均粒径の1/2以下の平均粒径を有する有機質粉体60〜5質量部(但し、バイオマス+有機質粉体=100質量部)と、水素発生油泥30〜300質量部とを混合することを特徴とする、水素発生油泥の処理方法。 40 to 95 parts by mass of biomass having an average particle size of 0.5 mm or more and a maximum particle size of 10 mm or less, and 60 to 5 parts by mass of organic powder having an average particle size of 1/2 or less of the average particle size of the biomass ( However, biomass + organic powder = 100 parts by mass) and 30 to 300 parts by mass of hydrogen-generating oil mud are mixed. 上記水素発生油泥が、水または水素原子含有化合物の還元によって水素を発生する、液状またはスラッジ状の油泥であることを特徴とする、請求項1に記載の水素発生油泥の処理方法。 The method for treating a hydrogen-generating oil mud according to claim 1, wherein the hydrogen-generating oil mud is a liquid or sludge-like oil mud that generates hydrogen by reducing water or a hydrogen atom-containing compound. 上記水素発生油泥が、シリコン粒子及び/又はアルミ粒子や金属粒子を含有した、廃ワイヤソーオイル、廃切削油、廃研削油、廃研磨油のいずれか一種以上であることを特徴とする、請求項1に記載の水素発生油泥の処理方法。 The hydrogen generating oil mud is at least one of waste wire saw oil, waste cutting oil, waste grinding oil, and waste polishing oil containing silicon particles and / or aluminum particles and metal particles. The method for treating hydrogen-producing oil mud according to 1. 上記バイオマスが、廃畳の破砕物、木材チップ、木粉、おが屑、紙屑のいずれか一種以上であることを特徴とする、請求項1〜3のいずれかに記載の水素発生油泥の処理方法。   The method for treating hydrogen-generated oil mud according to any one of claims 1 to 3, wherein the biomass is at least one of waste crushed material, wood chips, wood flour, sawdust, and paper waste. 上記有機質粉体が、トナー、重油灰、微粉炭、活性炭粉末、肉骨粉、廃プラスチック粉末、紙粉、有機蒸留残渣粉末のいずれか一種以上であることを特徴とする、請求項1〜4のいずれかに記載の水素発生油泥の処理方法。 The organic powder is any one or more of toner, heavy oil ash, pulverized coal, activated carbon powder, meat and bone powder, waste plastic powder, paper powder, and organic distillation residue powder. The processing method of the hydrogen generation oil mud in any one. 上記請求項1〜5のいずれかに記載の水素発生油泥の処理方法によって得られた固体燃料。   The solid fuel obtained by the processing method of the hydrogen generation oil mud in any one of the said Claims 1-5.
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JP2000160185A (en) * 1998-12-02 2000-06-13 Kyodo Yushi Co Ltd Water soluble oil agent for cut processing
JP2002323213A (en) * 2001-04-26 2002-11-08 Nippon Steel Corp Incineration method for oil-containing sludge
JP2003137620A (en) * 2001-10-29 2003-05-14 Mitsubishi Materials Corp Method for manufacturing cement clinker
JP2004121886A (en) * 2002-07-31 2004-04-22 Kurita Water Ind Ltd Method for treating organohalogen compound pollutant
JP2004169166A (en) * 2002-11-22 2004-06-17 Kawatetsu Techno Res Corp Method for utilizing waste silicon sludge
JP4421882B2 (en) * 2003-12-04 2010-02-24 日本磁力選鉱株式会社 Effective utilization of oil-impregnated SiC sludge
JP4306469B2 (en) * 2004-01-23 2009-08-05 株式会社Ihi Inert gas sealing method and apparatus for sealed waste incineration equipment
JP2005342557A (en) * 2004-05-31 2005-12-15 Japan Organo Co Ltd Method of treating chemically contaminated matter
JP4316486B2 (en) * 2004-12-15 2009-08-19 太平洋セメント株式会社 Fuel and its use
JP4319991B2 (en) * 2005-01-18 2009-08-26 太平洋セメント株式会社 Fuel and its use
JP5179037B2 (en) * 2006-10-05 2013-04-10 太平洋セメント株式会社 Method for mixing hydrogen-generating oil mud and method for producing solid fuel
JP2008086975A (en) * 2006-10-05 2008-04-17 Taiheiyo Cement Corp Method for treating hydrogen generating oil sludge and method for using hydrogen generating oil sludge

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