JP2009148715A - Industrial waste treating method and industrial waste treating apparatus - Google Patents
Industrial waste treating method and industrial waste treating apparatus Download PDFInfo
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- JP2009148715A JP2009148715A JP2007329551A JP2007329551A JP2009148715A JP 2009148715 A JP2009148715 A JP 2009148715A JP 2007329551 A JP2007329551 A JP 2007329551A JP 2007329551 A JP2007329551 A JP 2007329551A JP 2009148715 A JP2009148715 A JP 2009148715A
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/20—Waste processing or separation
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/58—Construction or demolition [C&D] waste
Abstract
Description
本発明は一般ゴミ、古タイヤ、廃プラ、建築廃材、屎尿処理物、その他の可燃廃棄物を燃焼によって処理する可燃廃棄物排気ガスを処理する産業廃棄物処理方法(産業廃棄物処理装置)に関する物である。 The present invention relates to an industrial waste treatment method (industrial waste treatment apparatus) for treating combustible waste exhaust gas for treating general waste, old tires, waste plastic, building waste, manure waste, and other combustible waste by combustion. It is a thing.
可燃廃棄物を燃焼によって処理する技術は従来から種々あるが、
例えば特開2004−290840号公報には、排気ガスから煤塵を除去するために、集塵装置を使用している。
For example, Japanese Patent Application Laid-Open No. 2004-290840 uses a dust collector to remove dust from exhaust gas.
通常可燃廃棄物を燃焼すると必然的に発生する煙、排気ガス、等は大気中に拡散して公害の原因となり、又その装置は大型である為設置場所、費用、等の問題が発生した。 Smoke, exhaust gas, etc. that are inevitably generated when combustible waste is combusted are diffused into the atmosphere and cause pollution, and the equipment is large, resulting in problems such as installation location and cost.
特開2004−290840号公報に示すように焼却灰は集塵装置を使用して焼却灰を取っていて、粉末状態の為に管理型最終処分場の埋め立てや海洋投棄に依存していた。また、焼却灰のリサイクル率はおよそ6%程度の低い水準に留まっていた。 As shown in Japanese Patent Application Laid-Open No. 2004-290840, incineration ash is incinerated ash using a dust collector, and relies on landfill of a managed final disposal site or ocean dumping because of the powder state. The recycling rate of incinerated ash remained at a low level of about 6%.
本発明の目的は、排気ガスより二酸化炭素等を取り除くことの出来る、地球環境改善に貢献出来る環境改善を主体とした産業廃棄物処理方法(産業廃棄物処理装置)にすることにある。
また、本発明の第2の目的は、排気ガスの二酸化炭素等と焼却灰を固形化することにある。
An object of the present invention is to provide an industrial waste treatment method (industrial waste treatment apparatus) that mainly removes carbon dioxide and the like from exhaust gas and can contribute to the improvement of the global environment.
A second object of the present invention is to solidify exhaust gas such as carbon dioxide and incineration ash.
上記の目的を達成するために、本発明は排気ガスと水を含んだ第1吸収液とを混合させる噴霧吸収手段と、この噴霧液と第2吸収液との混合を計り、この混合液の洗浄ガスを排出し、この混合液を廃棄物処理行程に移行し、排気ガス中の2酸化炭素等を吸収して処理するものである。
また、焼却灰と排気ガスを吸収させたのち、脱水して固体化するものである。
In order to achieve the above-mentioned object, the present invention measures the mixing of the spray absorbing means for mixing the exhaust gas and the first absorbing liquid containing water, and the spray liquid and the second absorbing liquid. The cleaning gas is discharged, the mixed liquid is transferred to a waste treatment process, and carbon dioxide and the like in the exhaust gas are absorbed and processed.
Moreover, after absorbing incineration ash and exhaust gas, it dehydrates and solidifies.
本発明の産業廃棄物処理方法(産業廃棄物処理装置)によれば、吸収液を使用するで排ガスの中に含まれている二酸化炭素を取り除くことができる。
また2酸化炭素等の気体と焼却灰を吸収液で混合させ、さらに脱水して固体化することにより、管理型最終処分場の埋め立てや海洋投棄に依存しないで骨材の材料になり、地球環境(特に地球温暖化)に貢献できる。
According to the industrial waste processing method (industrial waste processing apparatus) of the present invention, carbon dioxide contained in the exhaust gas can be removed by using the absorbent.
In addition, by mixing gas such as carbon dioxide and incineration ash with absorption liquid, and dehydrating and solidifying, it becomes an aggregate material without depending on landfill of managed final disposal site or ocean dumping. (Especially global warming).
以下図面により本発明の実施例について説明する。 Embodiments of the present invention will be described below with reference to the drawings.
図1は本発明を実施した焼却灰と排気ガス吸収機械本体の縦図面で焼却灰と排気ガス及び吸収液の混合実施例を示し、本実施例による、焼却灰と排気ガス及び吸収液の流れを示す説明図(フローシート)を示す。 FIG. 1 is a longitudinal view of incineration ash and exhaust gas absorption machine main body embodying the present invention, showing an example of mixing incineration ash, exhaust gas, and absorption liquid. The explanatory view (flow sheet) which shows is shown.
焼却灰と排気ガスの混ざった廃棄物(1)にスプレー(2)からの吸収液を噴霧し、排気ガス路(4)で混合する。排気ガス路(4)内には、廻転している網の目のスクリューコンベアーがあり、この時吸収液(水100%又は水70%+水蒸気30%)を噴霧し混合する。排気ガス路(4)は、焼却灰と排気ガスと噴霧された吸収液の流れの圧力の損出を助けるだけ事の出来る円筒状であり、焼却灰と排気ガスと噴霧された吸収液の必要に応じた安定した量を流す。
第1回目の混合を図り渦巻状態になった混合物を吸収溜液(水100%)槽(7)に渦巻状態で流入させ、第2回の混合を図る。
Absorbing liquid from the spray (2) is sprayed on the waste (1) mixed with incineration ash and exhaust gas, and mixed in the exhaust gas passage (4). In the exhaust gas passage (4), there is a rotating mesh screw conveyor. At this time, the absorbing liquid (100% water or 70% water + 30% water vapor) is sprayed and mixed. The exhaust gas passage (4) has a cylindrical shape that can only help the pressure loss of the flow of incinerated ash, exhaust gas and sprayed absorption liquid, and requires the incineration ash, exhaust gas and sprayed absorption liquid A stable amount according to the flow.
The mixture mixed in the first time and swirled is allowed to flow into the absorption reservoir (100% water) tank (7) in a swirled state, and second mixing is performed.
排気ガス路(4)内の焼却灰と排気ガスを吸収液に混合することは、排気ガスの中にある二酸化炭素などは、水に溶けやすい性質の為に二回の混合により高い吸収率を特徴とし期待出来、洗浄ガスは清浄ガス路(6)より大気に出す。 Mixing incinerated ash and exhaust gas in the exhaust gas passage (4) with the absorption liquid means that carbon dioxide in the exhaust gas is easily dissolved in water, so it has a high absorption rate by mixing twice. The cleaning gas is discharged to the atmosphere through the clean gas passage (6).
図に示すように混合された液体はスクリーン(13)へ投入し1mm以上の鉄片等は取り除き、1mm以下の混合液を混合液貯留槽(14)に入れる。この時、凝固剤液槽(15)より凝固剤を適度に投入し吸収液と分離液(二酸化炭素と焼却灰のフロック状態の物)に第一回目の分離を図り、吸収液は吸収液槽(17)へ送り、この吸収液は排気ガス路(4)に戻されて再度使用される。
貯留層(14)は脱水機械(16)に必要に応じた安定量を送り込む為のものである。
混合液貯留槽(14)の分離液を脱水機械(16)に投入する。使用する脱水機械(16)には、濾布を使用する物と遠心分離機械がある。
又使用する機械と排気ガスと焼却灰によっては凝固剤を使用しない時もあるが、ここの実施例では使用する。
As shown in the figure, the mixed liquid is put into the screen (13), iron pieces of 1 mm or more are removed, and the mixed liquid of 1 mm or less is put into the mixed liquid storage tank (14). At this time, the coagulant is appropriately added from the coagulant liquid tank (15), and the absorption liquid and the separation liquid (carbon dioxide and incinerated ash in a floc state) are separated for the first time. (17), the absorbed liquid is returned to the exhaust gas passage (4) and used again.
The reservoir (14) is for feeding a stable amount as required to the dehydrating machine (16).
The separated liquid in the mixed liquid storage tank (14) is charged into the dehydrating machine (16). The dehydrating machine (16) to be used includes a filter cloth and a centrifuge.
Depending on the machine used, the exhaust gas, and the incineration ash, a coagulant may not be used, but it is used in this embodiment.
脱水機械は遠心分離方式と濾過機方式と濾布、濾板方式がありここの実施例では遠心分離方式とする。 The dehydrating machine includes a centrifugal separation method, a filtration method, a filter cloth, and a filter plate method. In this embodiment, a centrifugal separation method is used.
脱水機械(16)で脱水された吸収液を取り除いた物(二酸化炭素と焼却灰のフロック状態の物)、つまり脱水ケーキ(二酸化炭素と焼却灰と吸収液30%)はリサイクルにより骨材の材料にする。脱水ケーキの吸収率約30%は運送を容易にし作業環境に良くリサイクル材料つまり骨材の材料として利用していくのに使用しやすい。脱水された吸収液は吸収液槽(17)にもどし再度使用する。 The material from which the absorption liquid dehydrated by the dehydration machine (16) has been removed (carbon dioxide and incinerated ash in a flock state), that is, the dehydrated cake (carbon dioxide, incinerated ash, and absorption liquid 30%) is recycled into aggregate material. To. A dehydrated cake absorption rate of about 30% is easy to transport and good for the work environment, and is easy to use as a recycled material, that is, an aggregate material. The dehydrated absorbent is returned to the absorbent tank (17) and used again.
本発明は上記の実施例に限定されることなくその精神を逸脱しない範囲で種々の設計変更が可能である。 The present invention is not limited to the above-described embodiments, and various design changes can be made without departing from the spirit thereof.
1 ・・・・焼却灰と排気ガス
2 ・・・・スプレー
3 ・・・・吸収液
4 ・・・・円筒内に網の目状のスクリューコンベア-構造(廻転式)
5 ・・・・吸収留液
6 ・・・・清浄ガス路
7 ・・・・槽
8 ・・・・円筒廻転動力
9 ・・・・給水及び水立調整機
10 ・・・・ 貯留槽へ送る弁
11 ・・・・ 排水口(清浄ガス路)
12・・・・焼却灰と排気ガス吸収機械
13・・・・スクリーン
14・・・・焼却灰と排気ガスと吸収液貯留槽
15・・・・凝固剤液槽
16・・・・脱水機械
17・・・・吸収液槽
1 ・ ・ ・ ・ Incineration ash and exhaust gas
2 ・ ・ ・ ・ Spray
3 ・ ・ ・ ・ Absorbing liquid
4 ··· Net-shaped screw conveyor in cylinder (structure)
5 ··· Absorption distillate
6 ・ ・ ・ ・ Clean gas path
7 ··· Tank
8 ・ ・ ・ ・ Cylinder rotation power
9 ・ ・ ・ ・ Water supply and water conditioner
10 ・ ・ ・ ・ Valves to be sent to the storage tank
11 ··· Drain outlet (clean gas passage)
12 .... Incineration ash and exhaust gas absorption machine
13 ... Screen
14 ... Incineration ash, exhaust gas, and absorption liquid storage tank
15 ... Coagulant bath
16 ... Dehydration machine
17 ... Absorber tank
Claims (6)
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JP2007329551A JP2009148715A (en) | 2007-12-21 | 2007-12-21 | Industrial waste treating method and industrial waste treating apparatus |
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JP2007329551A JP2009148715A (en) | 2007-12-21 | 2007-12-21 | Industrial waste treating method and industrial waste treating apparatus |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110141923A (en) * | 2019-06-26 | 2019-08-20 | 成都周祥环保科技有限公司 | A kind of train internal combustion engine tail gas discharge processing equipment |
WO2020213313A1 (en) * | 2019-04-16 | 2020-10-22 | 株式会社福岡建設合材 | Carbon dioxide concentration reduction method and carbon dioxide concentration reduction device |
CN113319101A (en) * | 2021-05-24 | 2021-08-31 | 龙净能源发展有限公司 | Kitchen waste pretreatment system and pretreatment method thereof |
WO2021193476A1 (en) * | 2020-03-27 | 2021-09-30 | 三菱パワー株式会社 | Device and method pertaining to combustion exhaust gas purification treatment |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005279370A (en) * | 2004-03-29 | 2005-10-13 | Ebara Corp | Method and apparatus for washing incinerated ash and cement kiln dust with water |
WO2007023937A1 (en) * | 2005-08-26 | 2007-03-01 | Taiheiyo Cement Corporation | Apparatus and method for dissolution/reaction |
JP2007083144A (en) * | 2005-09-21 | 2007-04-05 | Mitsubishi Heavy Ind Ltd | Ash treating method and system |
WO2007106372A2 (en) * | 2006-03-10 | 2007-09-20 | Comrie Douglas C | Carbon dioxide sequestration materials and processes |
-
2007
- 2007-12-21 JP JP2007329551A patent/JP2009148715A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005279370A (en) * | 2004-03-29 | 2005-10-13 | Ebara Corp | Method and apparatus for washing incinerated ash and cement kiln dust with water |
WO2007023937A1 (en) * | 2005-08-26 | 2007-03-01 | Taiheiyo Cement Corporation | Apparatus and method for dissolution/reaction |
JP2007083144A (en) * | 2005-09-21 | 2007-04-05 | Mitsubishi Heavy Ind Ltd | Ash treating method and system |
WO2007106372A2 (en) * | 2006-03-10 | 2007-09-20 | Comrie Douglas C | Carbon dioxide sequestration materials and processes |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020213313A1 (en) * | 2019-04-16 | 2020-10-22 | 株式会社福岡建設合材 | Carbon dioxide concentration reduction method and carbon dioxide concentration reduction device |
JP2020175318A (en) * | 2019-04-16 | 2020-10-29 | 株式会社福岡建設合材 | Carbon dioxide concentration reduction method and carbon dioxide concentration reduction device |
CN110141923A (en) * | 2019-06-26 | 2019-08-20 | 成都周祥环保科技有限公司 | A kind of train internal combustion engine tail gas discharge processing equipment |
WO2021193476A1 (en) * | 2020-03-27 | 2021-09-30 | 三菱パワー株式会社 | Device and method pertaining to combustion exhaust gas purification treatment |
JP2021154231A (en) * | 2020-03-27 | 2021-10-07 | 三菱パワー株式会社 | Device and method for flue gas clarification treatment |
CN113319101A (en) * | 2021-05-24 | 2021-08-31 | 龙净能源发展有限公司 | Kitchen waste pretreatment system and pretreatment method thereof |
CN113319101B (en) * | 2021-05-24 | 2023-01-03 | 龙净能源发展有限公司 | Kitchen waste pretreatment system and pretreatment method thereof |
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