JPH11101423A - Method of treating boiler combustion ash - Google Patents
Method of treating boiler combustion ashInfo
- Publication number
- JPH11101423A JPH11101423A JP9266350A JP26635097A JPH11101423A JP H11101423 A JPH11101423 A JP H11101423A JP 9266350 A JP9266350 A JP 9266350A JP 26635097 A JP26635097 A JP 26635097A JP H11101423 A JPH11101423 A JP H11101423A
- Authority
- JP
- Japan
- Prior art keywords
- boiler
- fuel
- combustion
- solid
- ash
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、重油や原油等の液
体燃料を燃焼させるボイラから発生する粉体状の燃焼生
成灰の処理方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating powdery combustion ash generated from a boiler for burning liquid fuel such as heavy oil or crude oil.
【0002】[0002]
【従来の技術】重油や原油を燃焼させるボイラからは粉
体状の燃焼生成灰が発生する。従来、この燃焼生成灰
は、廃棄物焼却炉において減容化処分(有価)するとと
もに、一部は「廃棄物の処理および清掃に関する法律」
に基づき産業廃棄物として処分しており、燃料などとし
ての再利用はされていない。2. Description of the Related Art Powdery combustion ash is generated from a boiler that burns heavy oil or crude oil. Conventionally, this combustion ash has been volume-reduced (valuable) in waste incinerators, and partly according to the "Law on the Treatment and Cleaning of Waste".
It is disposed of as industrial waste and is not reused as fuel.
【0003】この燃焼生成灰は、1kg当り2,000
〜6,000kcalの発熱量を有しており、これを産
業廃棄物などとして処分するのは資源の有効活用の面か
らも、また、廃棄物処分問題の観点からも好ましくな
い。また、このように大きな発熱量をもつ燃焼生成灰を
有効に活用しないと液体燃料を燃焼させるボイラの運転
コストが嵩むこととなり問題である。[0003] This combustion ash is 2,000 kg / kg.
It has a calorific value of up to 6,000 kcal, and it is not preferable to dispose of this as industrial waste from the viewpoint of effective use of resources and the problem of waste disposal. Further, unless the combustion ash having such a large calorific value is effectively used, the operating cost of the boiler for burning the liquid fuel increases, which is a problem.
【0004】[0004]
【発明が解決しようとする課題】本発明は、前記した従
来技術の状況に鑑み、重油や原油等の液体燃料を燃焼さ
せるボイラから発生する燃焼灰の再利用方法を提供する
ことを課題としている。SUMMARY OF THE INVENTION It is an object of the present invention to provide a method of recycling combustion ash generated from a boiler for burning a liquid fuel such as heavy oil or crude oil in view of the state of the prior art. .
【0005】[0005]
【課題を解決するための手段】本発明は、前記課題を解
決するため、液体燃料を燃焼させるボイラから発生する
燃焼生成灰を、造粒、乾燥して固形物とし、この固形物
を固体燃料を燃焼させるボイラに投入して再燃焼させる
ようにしたボイラ燃焼生成灰の処理方法を提供する。SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention is to granulate and dry a combustion ash generated from a boiler for burning a liquid fuel, and to convert the ash into a solid fuel. A method for treating boiler combustion ash, wherein the ash is supplied to a boiler for burning and then reburned.
【0006】重油や原油等を燃焼させるボイラから発生
する燃焼生成灰は比重が0.1程度と非常に軽く、しか
も微粉状であることからこのハンドリングが難しい。[0006] The combustion ash generated from a boiler for burning heavy oil, crude oil and the like has a very low specific gravity of about 0.1 and is in a fine powder form, so that it is difficult to handle the ash.
【0007】本発明では、燃焼生成灰に水等を加えて混
練する等、適宜の手法で燃焼生成灰を造粒する。これを
前記したように乾燥して固形物とし、これを石炭焚ボイ
ラ等の固体燃料を燃焼させるボイラに投入して燃料とし
て簡単、かつ、有効に利用するのである。In the present invention, the combustion ash is granulated by an appropriate method such as adding water or the like to the combustion ash and kneading the mixture. As described above, this is dried to form a solid, which is put into a boiler for burning a solid fuel such as a coal-fired boiler and used simply and effectively as fuel.
【0008】このようにして、本発明のボイラ燃焼生成
灰処理方法によれば、燃焼生成灰に含まれる資源を有効
に活用し、併せて廃棄物処分問題を緩和することができ
る。As described above, according to the boiler combustion ash treatment method of the present invention, the resources contained in the combustion ash can be effectively used, and at the same time, the problem of waste disposal can be mitigated.
【0009】[0009]
【発明の実施の形態】以下、本発明によるボイラ燃焼生
成灰の処理方法を図1に示した実施の一形態に基づいて
具体的に説明する。図1において、1は、重油や原油を
燃焼させる重原油焚ボイラ、2は空気予熱器、3は電気
集塵機でその燃焼排ガスから燃焼生成灰4等を捕集す
る。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, a method for treating boiler combustion ash according to the present invention will be described in detail with reference to an embodiment shown in FIG. In FIG. 1, 1 is a heavy crude oil boiler for burning heavy oil or crude oil, 2 is an air preheater, 3 is an electric precipitator, and collects combustion ash 4 and the like from the combustion exhaust gas.
【0010】6は、固形物化処理装置で、造粒装置8と
乾燥装置9を備えている。10はホッパで、固形物化さ
れた燃焼生成灰を受け入れる。12はミルで、燃焼生成
灰を固形化した固体燃料と石炭の供給をバンカ11から
受けてそれを破砕、混合する。13は石炭焚ボイラを示
し、14は脱硝装置、15は空気予熱器、16は電気集
塵機である。Reference numeral 6 denotes a solidification treatment device, which includes a granulating device 8 and a drying device 9. A hopper 10 receives the solidified combustion ash. Reference numeral 12 denotes a mill, which receives a supply of solid fuel obtained by solidifying the combustion ash and coal from the bunker 11, crushes and mixes them. Reference numeral 13 denotes a coal-fired boiler, 14 denotes a denitration device, 15 denotes an air preheater, and 16 denotes an electric dust collector.
【0011】図1のシステムにおいて、重原油焚ボイラ
1には重原油が燃料として供給され、その燃焼排ガスは
空気予熱器2で熱回収が行われた後、電気集塵機3へ導
かれる。In the system shown in FIG. 1, heavy crude oil is supplied to heavy crude oil-fired boiler 1 as fuel, and the combustion exhaust gas is led to electric precipitator 3 after heat recovery in air preheater 2.
【0012】電気集塵機3では燃焼排ガス中から燃焼生
成灰である重原油灰4が捕集されホッパ5に集められ
る。捕集された重原油灰4は固形物化処理装置6に送ら
れ、まず、造粒装置8において水7が添加されて混練・
造粒が行われる。造粒された重原油灰は乾燥装置9に送
られて硬質、小塊の固形物とされる。In the electric dust collector 3, heavy crude oil ash 4, which is combustion ash, is collected from the combustion exhaust gas and collected in the hopper 5. The collected heavy crude oil ash 4 is sent to a solidification treatment device 6, and first, water 7 is added to a granulating device 8 to knead and knead the mixture.
Granulation is performed. The granulated heavy crude ash is sent to the drying device 9 to be hard and small solids.
【0013】以上のように燃焼生成灰を固形化するに
は、燃焼生成灰「1」に対し水を「0.2〜0.4」
(重量比)の割合で添加・混練のうえ、造粒機で造粒す
ることにより容易に小塊になり、さらに乾燥工程を経る
ことにより、比重0.1程度の微粉状であった燃焼生成
灰が、比重0.5〜0.6の塊状となり、容量も1/5
程度まで減容化でき、ハンドリングが容易となる。As described above, in order to solidify the combustion ash, water is added to the combustion ash “1” by “0.2 to 0.4”.
(Weight ratio) After addition and kneading at the ratio of (weight ratio), it was easily formed into small lumps by granulation with a granulator, and further passed through a drying process, resulting in a fine powder having a specific gravity of about 0.1. Ash becomes lumps with specific gravity of 0.5-0.6, and capacity is 1/5
The volume can be reduced to the extent and handling becomes easy.
【0014】以上の工程で得られた重原油灰からなる固
体燃料は石炭焚ボイラ13の設置されているところに輸
送される。その固体燃料は、石炭焚ボイラ13の燃料と
なる石炭と共にバンカ11へ供給され、バンカ11から
ミル12に供給して粉砕して石炭焚ボイラ13に供給さ
れ燃焼される。The solid fuel composed of heavy crude ash obtained in the above steps is transported to a place where the coal-fired boiler 13 is installed. The solid fuel is supplied to the bunker 11 together with the coal serving as the fuel for the coal-fired boiler 13, supplied from the bunker 11 to the mill 12, pulverized, supplied to the coal-fired boiler 13, and burned.
【0015】燃焼生成灰を、その発生元である重油・原
油等を燃料とするボイラで再利用しようとすると、燃料
燃焼設備全体の大幅な改造が必要である。これに対し、
前記したように石炭焚ボイラ等固形物を燃料とする燃焼
設備で燃焼させることは、わずかの設備改造で簡単に燃
料消費系統に混入でき燃焼させることが可能である。[0015] If the combustion ash is to be reused in a boiler that uses heavy oil, crude oil, or the like as a fuel, the fuel combustion equipment must be largely remodeled. In contrast,
As described above, burning with a combustion facility using solid matter as a fuel, such as a coal-fired boiler, can be easily mixed into a fuel consuming system and burned with slight equipment modification.
【0016】石炭焚ボイラ13の燃焼排ガスは、脱硝装
置14、空気予熱器15、及び電気集塵機16を経て外
部に排出される。The combustion exhaust gas from the coal-fired boiler 13 is discharged outside through a denitration device 14, an air preheater 15, and an electric dust collector 16.
【0017】以上、本発明を図示した実施形態に基づい
て具体的に説明したが、本発明がこれらの実施形態に限
定されず特許請求の範囲に示す本発明の範囲内で、その
具体的構造、構成に種々の変更を加えてよいことはいう
までもない。As described above, the present invention has been specifically described based on the illustrated embodiments. However, the present invention is not limited to these embodiments, and specific structures within the scope of the present invention are set forth in the appended claims. Needless to say, various changes may be made to the configuration.
【0018】例えば、上記実施形態では、液体燃料を燃
焼させるボイラから発生する燃焼生成灰を造粒、乾燥し
て得た固形物を石炭焚ボイラの燃料としているが、これ
は石炭焚ボイラに限らず、他の固形燃料を使用するボイ
ラであってよい。For example, in the above embodiment, solids obtained by granulating and drying combustion ash generated from a boiler for burning liquid fuel are used as fuel for a coal-fired boiler, but this is not limited to a coal-fired boiler. Instead, the boiler may use another solid fuel.
【0019】[0019]
【発明の効果】以上説明したように、本発明によるボイ
ラ燃焼生成灰の処理方法は、ボイラ燃焼生成灰を造粒、
乾燥して固形物とするのでハンドリングが容易となる。As described above, the method for treating boiler combustion ash according to the present invention comprises the steps of:
Since it is dried to be a solid, handling becomes easy.
【0020】そして、得られた固形物を固体燃料を燃焼
させるボイラで燃焼させるので、そのボイラの燃料との
混合も極めて容易であり、既存設備を有効に活用でき
る。Since the obtained solid is burned in a boiler for burning solid fuel, mixing with the fuel of the boiler is extremely easy, and the existing equipment can be effectively used.
【0021】このようにして、本発明のボイラ燃焼生成
灰の処理方法によれば、液体燃料のもつエネルギーを有
効に活用し、廃棄物処理問題を緩和すると共に、ボイラ
の運転コストを低減することができる。As described above, according to the method for treating boiler combustion ash of the present invention, it is possible to effectively utilize the energy of liquid fuel, alleviate the waste disposal problem, and reduce the operating cost of the boiler. Can be.
【図1】本発明の実施の一形態を示すボイラ燃焼灰処理
システムの系統図。FIG. 1 is a system diagram of a boiler combustion ash treatment system showing one embodiment of the present invention.
1 重原油焚ボイラ 2 空気予熱器 3 電気集塵機 4 重原油灰 5 ホッパ 6 固形物化処理装置 7 水 8 造粒装置 9 乾燥装置 10 ホッパ 11 バンカ 12 ミル 13 石炭焚ボイラ 14 脱硝装置 15 空気予熱器 16 電気集塵機 DESCRIPTION OF SYMBOLS 1 Heavy crude oil boiler 2 Air preheater 3 Electric dust collector 4 Heavy crude ash 5 Hopper 6 Solidification processing apparatus 7 Water 8 Granulation apparatus 9 Drying apparatus 10 Hopper 11 Bunker 12 Mill 13 Coal fired boiler 14 Denitration apparatus 15 Air preheater 16 Electric dust collector
フロントページの続き (72)発明者 石村 安延 愛媛県西条市喜多川853 四国電力株式会 社西条発電所内 (72)発明者 和泉 光則 香川県坂出市番の州町2 四国電力株式会 社坂出発電所内 (72)発明者 小野 正司 香川県坂出市番の州町2 四国電力株式会 社坂出発電所内 (72)発明者 川下 幸信 香川県高松市丸の内2番5号 四国電力株 式会社内 (72)発明者 西浦 大補 神戸市兵庫区和田崎町一丁目1番1号 三 菱重工業株式会社神戸造船所内Continuing from the front page (72) Inventor Ishimura Yasunobu 853 Kitagawa, Saijo-shi, Ehime Prefecture Shikoku Electric Power Company Saijo Power Plant (72) Inventor Mitsunori Izumi 2 Sakaide-city Banshu-cho, Kagawa Prefecture Shikoku Electric Power Company Sakaide Power Plant (72) Inventor Shoji Ono 2 Bannoshu-cho, Sakaide-shi, Kagawa Prefecture Inside Sakaide Power Station of Shikoku Electric Power Company (72) Inventor Yukinobu No. 2-5 Marunouchi, Takamatsu-shi, Kagawa Prefecture Inside Shikoku Electric Power Company (72) Inventor Daisuke Nishiura Kobe 1-1-1, Wadazakicho, Hyogo-ku, Yokohama
Claims (1)
る燃焼生成灰を、造粒、乾燥して固形物とし、この固形
物を固体燃料を燃焼させるボイラに投入して再燃焼させ
ることを特徴とするボイラ燃焼生成灰の処理方法。1. A combustion product ash generated from a boiler for burning liquid fuel is granulated and dried to form a solid, and the solid is put into a boiler for burning solid fuel and re-burned. To treat boiler combustion ash.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP09266350A JP3082842B2 (en) | 1997-09-30 | 1997-09-30 | Treatment method of boiler combustion ash |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP09266350A JP3082842B2 (en) | 1997-09-30 | 1997-09-30 | Treatment method of boiler combustion ash |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH11101423A true JPH11101423A (en) | 1999-04-13 |
JP3082842B2 JP3082842B2 (en) | 2000-08-28 |
Family
ID=17429727
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP09266350A Expired - Fee Related JP3082842B2 (en) | 1997-09-30 | 1997-09-30 | Treatment method of boiler combustion ash |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3082842B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009074771A (en) * | 2007-09-21 | 2009-04-09 | Chugoku Electric Power Co Inc:The | Coal fired power generation system and method of reducing elution of hexavalent chromium |
JP2015190727A (en) * | 2014-03-28 | 2015-11-02 | 住友重機械工業株式会社 | Combustion apparatus, operation method of combustion apparatus and ash circulation system |
WO2020218534A1 (en) * | 2019-04-26 | 2020-10-29 | 川崎重工業株式会社 | Method and system for processing combustion ash, and petroleum-based fuel combustion plant |
-
1997
- 1997-09-30 JP JP09266350A patent/JP3082842B2/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009074771A (en) * | 2007-09-21 | 2009-04-09 | Chugoku Electric Power Co Inc:The | Coal fired power generation system and method of reducing elution of hexavalent chromium |
JP2015190727A (en) * | 2014-03-28 | 2015-11-02 | 住友重機械工業株式会社 | Combustion apparatus, operation method of combustion apparatus and ash circulation system |
WO2020218534A1 (en) * | 2019-04-26 | 2020-10-29 | 川崎重工業株式会社 | Method and system for processing combustion ash, and petroleum-based fuel combustion plant |
JP2020182890A (en) * | 2019-04-26 | 2020-11-12 | 川崎重工業株式会社 | Processing method and system for combustion ashes, and, petroleum-based fuel combustion plant |
KR20210150544A (en) * | 2019-04-26 | 2021-12-10 | 카와사키 주코교 카부시키 카이샤 | Combustion ash treatment method and system, and petroleum fuel combustion plant |
Also Published As
Publication number | Publication date |
---|---|
JP3082842B2 (en) | 2000-08-28 |
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