JPH11322381A - Method for forming municipal refuse-burned ash into cement raw material, and cement raw material obtained by the method - Google Patents
Method for forming municipal refuse-burned ash into cement raw material, and cement raw material obtained by the methodInfo
- Publication number
- JPH11322381A JPH11322381A JP10137186A JP13718698A JPH11322381A JP H11322381 A JPH11322381 A JP H11322381A JP 10137186 A JP10137186 A JP 10137186A JP 13718698 A JP13718698 A JP 13718698A JP H11322381 A JPH11322381 A JP H11322381A
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- municipal
- incineration ash
- cement raw
- cement
- 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
- 239000004568 cement Substances 0.000 title claims abstract description 114
- 239000002994 raw material Substances 0.000 title claims abstract description 100
- 238000000034 method Methods 0.000 title claims abstract description 39
- 239000000460 chlorine Substances 0.000 claims abstract description 103
- 229910052801 chlorine Inorganic materials 0.000 claims abstract description 102
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims abstract description 98
- 238000004056 waste incineration Methods 0.000 claims description 106
- 239000010813 municipal solid waste Substances 0.000 claims description 62
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 51
- 238000005406 washing Methods 0.000 claims description 26
- 239000002689 soil Substances 0.000 claims description 19
- 239000002699 waste material Substances 0.000 claims description 19
- 239000000463 material Substances 0.000 claims description 12
- 239000000126 substance Substances 0.000 claims description 7
- 239000003929 acidic solution Substances 0.000 claims description 4
- 238000005507 spraying Methods 0.000 claims 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 18
- 229910052742 iron Inorganic materials 0.000 abstract description 8
- 239000004927 clay Substances 0.000 abstract description 6
- 238000010304 firing Methods 0.000 abstract description 4
- 238000002156 mixing Methods 0.000 abstract description 4
- 229910001294 Reinforcing steel Inorganic materials 0.000 abstract description 3
- 239000004567 concrete Substances 0.000 abstract description 2
- 238000010298 pulverizing process Methods 0.000 abstract 1
- 239000002956 ash Substances 0.000 description 130
- 239000011398 Portland cement Substances 0.000 description 8
- 238000005554 pickling Methods 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000011521 glass Substances 0.000 description 4
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 150000001804 chlorine Chemical class 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 3
- 238000006703 hydration reaction Methods 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 229910017604 nitric acid Inorganic materials 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 229910004298 SiO 2 Inorganic materials 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 238000009933 burial Methods 0.000 description 2
- 229910052681 coesite Inorganic materials 0.000 description 2
- 229910052593 corundum Inorganic materials 0.000 description 2
- 229910052906 cristobalite Inorganic materials 0.000 description 2
- 238000010612 desalination reaction Methods 0.000 description 2
- 229910001653 ettringite Inorganic materials 0.000 description 2
- 239000010881 fly ash Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000011150 reinforced concrete Substances 0.000 description 2
- 230000003014 reinforcing effect Effects 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 229910052682 stishovite Inorganic materials 0.000 description 2
- 229910052905 tridymite Inorganic materials 0.000 description 2
- 229910001845 yogo sapphire Inorganic materials 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 1
- 235000017491 Bambusa tulda Nutrition 0.000 description 1
- 241001330002 Bambuseae Species 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 229910017344 Fe2 O3 Inorganic materials 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- KKCBUQHMOMHUOY-UHFFFAOYSA-N Na2O Inorganic materials [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 1
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 1
- 229910010413 TiO 2 Inorganic materials 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000011425 bamboo Substances 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- XFWJKVMFIVXPKK-UHFFFAOYSA-N calcium;oxido(oxo)alumane Chemical compound [Ca+2].[O-][Al]=O.[O-][Al]=O XFWJKVMFIVXPKK-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- 238000004737 colorimetric analysis Methods 0.000 description 1
- 239000010849 combustible waste Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 230000001186 cumulative effect Effects 0.000 description 1
- 238000011033 desalting Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000007730 finishing process Methods 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 238000007885 magnetic separation Methods 0.000 description 1
- 230000003387 muscular Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 238000000634 powder X-ray diffraction Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000010801 sewage sludge Substances 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B7/00—Hydraulic cements
- C04B7/36—Manufacture of hydraulic cements in general
- C04B7/38—Preparing or treating the raw materials individually or as batches, e.g. mixing with fuel
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
- C04B2111/00017—Aspects relating to the protection of the environment
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- 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】この発明は、ごみ焼却場から
排出される都市ごみ焼却灰中から塩素分および異物を除
去して、セメント原料の一部として利用することができ
るようにする都市ごみ焼却灰のセメント原料化方法およ
びこの方法から得られたセメント原料に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to municipal solid waste incineration that removes chlorine and foreign substances from municipal incineration ash discharged from a waste incineration plant and can be used as a part of cement raw materials. The present invention relates to a method for converting ash into a cement raw material and a cement raw material obtained by the method.
【0002】[0002]
【従来の技術】生活圏から排出された一般廃棄物である
都市ごみは、清掃車などにより収集され、その一部がご
み処理工場の焼却炉により焼却される。焼却後の焼却灰
の主成分は、ポルトランドセメントの原料、特に粘土原
料等に類似したSiO2,Al2O3,Fe2O3,C
aOなどである。しかしながら、都市ごみ焼却灰中に
は、セメントとしては不適合な成分も含まれている。そ
の代表成分が、鉄筋コンクリート中の鉄筋を溶損させる
塩素である。この塩素は、都市ごみ焼却灰、特にその飛
灰中に5〜10重量%前後も含まれている。したがっ
て、都市ごみ焼却灰は、珪素やアルミニウムの原料とし
ては有用であっても、そのままではポルトランドセメン
トの原料として用いることができない。2. Description of the Related Art Municipal waste, which is general waste discharged from a living area, is collected by a cleaning car or the like, and a part thereof is incinerated by an incinerator of a waste treatment plant. The main components of the incinerated ash after incineration are SiO 2 , Al 2 O 3 , Fe 2 O 3 , and C 2 similar to raw materials of Portland cement, particularly clay raw materials.
aO and the like. However, municipal solid waste incineration ash contains components that are incompatible with cement. A representative component is chlorine, which erodes the reinforcing steel in reinforced concrete. This chlorine contains about 5 to 10% by weight of municipal solid waste incineration ash, especially fly ash. Therefore, municipal solid waste incineration ash cannot be used as it is as a raw material for Portland cement, although it is useful as a raw material for silicon and aluminum.
【0003】そこで、従来、都市ごみ焼却灰を、乾燥し
た下水汚泥とともに乾式セメントキルン内へ投入して、
1350℃前後という比較的低い温度の焼成によりセメ
ントクリンカを中間製造するエコセメント(エコロジー
とセメントとの合成語)と称されるものが開発されてい
る。エコセメントは、ポルトランドセメントに含まれな
いカルシウムクロロアルミネート(C11A7・CaC
l2)が、セメントクリンカ中の隙間を埋める間隙相と
なって多量に存在する。反面、普通ポルトランドセメン
トに含まれるカルシウムアルミネート(C3A)がほと
んどない。これにより、エコセメントは、普通ポルトラ
ンドセメントの初期水和反応とは異なり、注水直後にエ
トリンガイトおよびフリーデル氏塩(C3A・CaCl
2・10H2O)を生成しながら水和反応が進行し、そ
の後、エトリンガイトの活発な水和が生じることにな
る。この結果、セメントの凝結時間が短縮し、強さ発現
の速硬性が得られる。Therefore, conventionally, municipal solid waste incineration ash has been put into a dry cement kiln together with dried sewage sludge,
A so-called eco-cement (synthetic term of ecology and cement) for intermediate production of cement clinker by firing at a relatively low temperature of about 1350 ° C. has been developed. Eco cement, calcium chloroaluminate not included in Portland cement (C 11 A 7 · CaC
l 2 ) is present in a large amount as a gap phase that fills gaps in the cement clinker. On the other hand, there is almost no calcium aluminate (C 3 A) normally contained in Portland cement. Thus, unlike the initial hydration reaction of ordinary Portland cement, Ecocement immediately after injection with ettringite and Friedel's salt (C 3 A.CaCl
The hydration reaction proceeds while producing 2 · 10H 2 O), followed by vigorous hydration of ettringite. As a result, the setting time of the cement is shortened, and the quick-hardening of strength development is obtained.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、このよ
うな従来技術におけるエコセメントは、その成分中に比
較的多量の塩素を有している。このため、鉄筋を用いな
い無筋系の分野にその用途が限定されていた。例えば、
漁礁、消波ブロックなどの海洋コンクリートや、地盤改
良材などである。この結果、セメントの用途の大半を占
める鉄筋構造物用としては利用することができなかっ
た。また、一方では、この都市ごみ焼却灰中には、例え
ば空き缶,鉄くず,未燃の電話帳,ガラス片,陶器片,
大小型のフォーク,釘,ボルト,ナット類など、多量の
異物を含んでいるので、都市ごみ焼却灰をセメント原料
化するには、この異物を除去する必要もあった。However, such an eco-cement in the prior art has a relatively large amount of chlorine in its components. For this reason, its use has been limited to the field of a non-muscular system that does not use a reinforcing bar. For example,
Marine concrete such as fishing reefs and wave-dissipating blocks, and ground improvement materials. As a result, it could not be used for reinforcing steel structures, which account for most of the uses of cement. On the other hand, in this municipal solid waste incineration ash, for example, empty cans, iron scraps, unburned telephone directories, glass pieces, pottery pieces,
Since it contains a large amount of foreign matter such as large and small forks, nails, bolts, nuts, etc., it was necessary to remove such foreign matter in order to convert municipal solid waste incineration ash into a raw material for cement.
【0005】そこで、発明者らは、鋭意研究の結果、都
市ごみ焼却灰中に含まれる塩素を例えば水洗したりし
て、できるだけJIS規格のセメント原料中におけるの
塩素含有許容量の200ppm以下まで除去する(以
下、脱塩処理という場合がある)一方、例えばふるいを
用いた分級などにより、空き缶やボルトナット等の異物
を除去することで、ポルトランドセメントのセメント原
料中の粘土原料等に類似した成分とすることができるこ
とを見出し、この発明を開発するに至った。Therefore, as a result of intensive studies, the inventors have found that chlorine contained in municipal solid waste incineration ash is removed, for example, by washing with water to reduce the chlorine content allowable amount in cement raw materials of JIS standard to 200 ppm or less as much as possible. On the other hand, by removing foreign substances such as empty cans and bolts and nuts by, for example, classification using a sieve, a component similar to the clay raw material in the Portland cement cement raw material is performed. And found that the present invention was developed.
【0006】[0006]
【発明の目的】この発明は、都市ごみ焼却灰をセメント
原料の一部として利用することができる都市ごみ焼却灰
のセメント原料化方法、および、この方法から得られた
セメント原料を提供することを、その目的とする。ま
た、この発明は、都市ごみ焼却灰中からの異物除去や塩
素除去を比較的容易でかつ確実に行うことができる都市
ごみ焼却灰のセメント原料化方法を提供することを、そ
の目的とする。さらに、この発明は、都市ごみ焼却灰中
からの塩素分の除去を効果的に行うことができる都市ご
み焼却灰のセメント原料化方法を提供することを、その
目的とする。さらにまた、この発明は、比較的少ない設
備コストで、かつ比較的短期間に、この焼却灰中の塩素
濃度を低減することができる都市ごみ焼却灰のセメント
原料化方法を提供することを、その目的とする。そし
て、この発明は、セメント原料の一部として比較的多量
に利用可能な都市ごみ焼却灰のセメント原料化方法を提
供することを、その目的とする。また、この発明は、不
溶性塩素をも除去して都市ごみ焼却灰中の塩素分をさら
に除去することができる都市ごみ焼却灰のセメント原料
化方法を提供することを、その目的とする。An object of the present invention is to provide a method for converting municipal solid waste incineration ash into a cement raw material in which municipal solid waste incineration ash can be used as a part of the cement raw material, and to provide a cement raw material obtained by this method. And its purpose. Another object of the present invention is to provide a method for converting municipal waste incineration ash into a cement raw material, which can relatively easily and reliably remove foreign substances and chlorine from municipal waste incineration ash. A further object of the present invention is to provide a method for converting municipal waste incinerated ash into a raw material for cement, which can effectively remove chlorine from municipal waste incinerated ash. Still further, the present invention provides a method for converting municipal solid waste incineration ash into a cement material which can reduce the chlorine concentration in the incineration ash with a relatively small facility cost and in a relatively short period of time. Aim. An object of the present invention is to provide a method for converting municipal waste incineration ash into a cement raw material that can be used in a relatively large amount as a part of the cement raw material. Another object of the present invention is to provide a method for converting municipal waste incineration ash into a cement raw material, which can remove insoluble chlorine and further remove chlorine in the municipal waste incineration ash.
【0007】[0007]
【課題を解決するための手段】請求項1に記載の発明
は、都市ごみ焼却灰中から異物を除去する工程と、都市
ごみ焼却灰中に含まれる塩素分を除去する工程とを備え
た都市ごみ焼却灰のセメント原料化方法である。都市ご
みとは、都市などの生活圏から排出される一般廃棄物を
いう。すなわち、ここで取り扱う一般廃棄物の主なもの
には、ごみ処理工場で焼却処分される一般ごみの内、紙
類、ちゅうかい、繊維、木、竹類などの可燃ごみが挙げ
られる。なお、現実的な分別ごみの収集状況から、この
中には、一部のプラスチック、ゴム、金属、ガラス・陶
器類、雑物などの不燃・焼却不適ごみも含まれる。According to the first aspect of the present invention, there is provided a city having a step of removing foreign matter from municipal waste incineration ash and a step of removing chlorine contained in municipal waste incineration ash. This is a method for converting waste incineration ash into cement raw material. Municipal waste refers to municipal waste discharged from living areas such as cities. That is, the main types of general waste handled here include combustible waste such as papers, chunks, fibers, wood, and bamboo among general wastes incinerated at a waste treatment plant. In addition, based on the actual situation of collection of sorted garbage, this includes some non-combustible and non-burnable garbage such as plastic, rubber, metal, glass and ceramics, and miscellaneous materials.
【0008】都市ごみ焼却灰中の塩素は、通常、焼却灰
(飛灰)の全体の5〜10重量%を占める。脱塩処理後
の都市ごみ焼却灰の塩素濃度の低減値は、当然ながら0
が最も好ましいものの、その数値は限定されない。ただ
し、できるだけJIS規格のセメント原料の塩素含有許
容量である200ppm以下とした方が好ましい。塩素
分が少なくなるほど、この都市ごみ焼却灰から得られた
物質が、セメント原料の一部に代替えされる割合が増加
する。[0008] Chlorine in municipal solid waste incineration ash usually accounts for 5 to 10% by weight of the entire incineration ash (fly ash). Naturally, the reduction value of chlorine concentration in municipal solid waste incineration ash after desalination treatment is zero.
Is most preferable, but the numerical value is not limited. However, it is preferable that the chlorine content is set to 200 ppm or less, which is the allowable amount of chlorine contained in the cement raw material according to the JIS standard. The lower the chlorine content, the greater the proportion of materials from this municipal solid waste incineration ash that will be replaced by some of the cement raw materials.
【0009】都市ごみ焼却灰中の異物の除去は、例えば
請求項2のようなふるいを用いた分級の他にも、例えば
磁力により選別する磁選や、この都市ごみ焼却灰中に含
まれる有用な灰成分と、不要な金属類成分とを比重の差
を利用して選別する比重選別などが挙げられる。また、
都市ごみ焼却灰のセメント原料化処理の順番は、請求項
3に示したような異物除去工程→塩素除去工程に限定さ
れず、これと反対の塩素除去工程→異物除去工程でもよ
い。The foreign matter in the municipal waste incineration ash can be removed, for example, by classification using a sieve as described in claim 2, for example, magnetic separation by magnetic force, or useful trash contained in the municipal waste incineration ash. Specific gravity selection, which separates an ash component and an unnecessary metal component using a difference in specific gravity, may be used. Also,
The order of the process of converting the municipal waste incineration ash into a cement raw material is not limited to the foreign matter removing step → chlorine removing step as described in claim 3, but may be the reverse chlorine removing step → contaminant removing step.
【0010】請求項2に記載の発明は、上記異物除去工
程が都市ごみ焼却灰の分級により行われ、上記塩素除去
工程が都市ごみ焼却灰の水洗により行われる請求項1に
記載の都市ごみ焼却灰のセメント原料化方法である。都
市ごみ焼却灰の分級には、例えば65mm(空き缶,鉄
くず,未燃の電話帳などを除去)→20mm(空き缶,
ガラス,陶器片,大型のフォークなどを除去)→5mm
(釘,ボルト・ナット類,小型フォークなどを除去)と
いった、網目の大きさが異なるふるいを使う方法を採用
することができる。分級後の粒径は、このように5mm
以下が好ましい。5mmを超えると、セメント製造設備
の仕上げ工程に配備された仕上げミルなどで粉砕するこ
とができない物質(例えばフォークやステンレス片類)
が残るおそれがある。According to a second aspect of the present invention, the foreign matter removing step is performed by classifying the municipal waste incineration ash, and the chlorine removing step is performed by washing the municipal waste incineration ash with water. This is a method for converting ash into a cement material. For classification of municipal solid waste incineration ash, for example, 65 mm (removing empty cans, iron scraps, unburned telephone directories, etc.) → 20 mm (empty cans,
Remove glass, pottery pieces, large forks, etc.) → 5mm
A method using a sieve having a different mesh size, such as removing nails, bolts and nuts, and a small fork, can be adopted. The particle size after classification is 5 mm
The following is preferred. If it exceeds 5 mm, substances that cannot be crushed by a finishing mill or the like provided in the finishing process of cement manufacturing equipment (for example, forks and stainless steel pieces)
May remain.
【0011】また、都市ごみ焼却灰の水洗の種類として
は、請求項4に示す管理型処分場の土中への埋設の他に
も、例えば通常の土中へ埋設したり、盛り土したりして
雨水にさらす方法が挙げられる。また、このような雨さ
らし法に加えて、スプリンクラーまたは散水車などによ
り強制散水し、より短期間に所定値まで塩素分を除去す
るようにしてもよい。さらに、請求項4でいうその他の
散水設備として、例えば都市ごみ焼却灰を大型の洗浄槽
へ投入し、この槽内で散水を行ったり、都市ごみ焼却灰
をベルトコンベアなどにより搬送し、この中途部で散水
するようにしてもよい。[0011] In addition to the types of municipal waste incineration ash that can be washed with water, in addition to the embedding in the soil of a managed disposal site as set forth in claim 4, for example, the incineration ash may be buried in the normal soil or embanked. And exposing it to rainwater. Further, in addition to such a rain exposure method, water may be forcibly sprinkled with a sprinkler or a water sprinkler to remove chlorine to a predetermined value in a shorter time. Further, as another watering equipment as described in claim 4, for example, municipal waste incineration ash is put into a large washing tank, and water is sprinkled in this tank, or the municipal waste incineration ash is transported by a belt conveyor or the like. Water may be sprayed at the part.
【0012】請求項3に記載の発明は、上記都市ごみ焼
却灰のセメント原料化処理が、上記異物除去工程を行っ
た後、上記塩素除去工程を行う請求項1または請求項2
に記載の都市ごみ焼却灰のセメント原料化方法である。
異物除去した後に塩素除去工程を行うと、その分、土中
へ埋設される都市ごみ焼却灰の量が減少し、比較的狭い
スペースで効率よく短期間で脱塩処理を行うことができ
る。According to a third aspect of the present invention, in the process of converting the municipal solid waste incineration ash into a cement material, the chlorine removing step is performed after the foreign matter removing step.
The method for converting municipal solid waste incineration ash into a cement raw material as described in (1).
If the chlorine removal step is performed after removing foreign matter, the amount of municipal waste incineration ash buried in the soil is reduced by that amount, and desalination can be efficiently performed in a relatively narrow space in a short period of time.
【0013】請求項4に記載の発明は、上記塩素除去工
程は、表面に覆土を被せた状態で都市ごみ焼却灰を管理
型処分場の土中に埋設し、その後、雨水にさらす以外
に、スプリンクラー、散水車またはその他の散水設備に
よって強制散水する請求項1〜請求項3のうちのいずれ
か1項に記載の都市ごみ焼却灰のセメント原料化方法で
ある。管理型処分場を用いることは、この都市ごみ焼却
灰を一般的な埋設場に埋設する場合より、好ましい。こ
れは、管理型処分場では、洗浄後、塩素分を含む処理水
を無害化するための二次的な設備が整っているからであ
る。この土中への埋設期間は、都市ごみ焼却灰の成分割
合、その埋設量、土中への埋設深さ、また覆土の深さ
や、覆土および都市ごみ焼却灰の透水性、降雨量、散水
量などの各種の条件によっても異なる。According to a fourth aspect of the present invention, in the chlorine removing step, the municipal solid waste incineration ash is buried in the soil of the controlled disposal site with the surface covered with soil, and then exposed to rainwater. The method for converting municipal solid waste incineration ash into a cement raw material according to any one of claims 1 to 3, wherein water is forcibly sprayed by a sprinkler, a watering machine or other watering equipment. The use of a managed landfill is preferable to the case where this municipal solid waste incineration ash is buried in a general landfill. This is because the controlled disposal site is equipped with secondary facilities for detoxifying the treated water containing chlorine after cleaning. During the burial period in the soil, the composition ratio of municipal solid waste incineration ash, the amount buried, the depth of burial in the soil, the depth of the soil cover, the permeability of the soil and municipal incineration ash, the amount of rainfall, and the amount of water spray It depends on various conditions such as.
【0014】請求項5に記載の発明は、上記塩素除去工
程は、都市ごみ焼却灰を水洗することにより、および、
酸性溶液を用いて酸洗することにより行われる請求項1
〜請求項4のうちのいずれか1項に記載の都市ごみ焼却
灰のセメント原料化方法である。都市ごみ焼却灰中に
は、水に溶ける塩素分と、溶けない塩素分とがある。こ
の後者の塩素分は、通常、酸性の溶液に溶出するので、
水洗だけでなく酸洗を行えば、この焼却灰中に含有する
ほとんどの塩素分を除去することができることになる。
酸洗用の酸としては、硝酸、硫酸、炭酸などが挙げられ
る。According to a fifth aspect of the present invention, in the chlorine removing step, municipal solid waste incineration ash is washed with water;
2. The method according to claim 1, wherein the washing is performed by pickling using an acidic solution.
A method for converting municipal solid waste incineration ash into a cement raw material according to any one of claims 4 to 4. Municipal solid waste incineration ash contains chlorine that is soluble in water and chlorine that is insoluble. This latter chlorine content usually elutes in acidic solutions,
By performing not only water washing but also acid washing, most of the chlorine contained in the incinerated ash can be removed.
Examples of the acid for pickling include nitric acid, sulfuric acid, and carbonic acid.
【0015】発明者の実験によれば、脱塩処理としての
水洗前、全塩素濃度4100ppmだったものが、所定
の水洗を行うことで約2600ppmまで低下した。こ
のとき、全塩素濃度に対して、水洗で溶出しない不溶性
塩素分の濃度は、洗浄前と同じ約1000ppmであっ
た。したがって、この水洗が十分に行われ、水溶性塩素
濃度が0に近くなると、この全塩素濃度は約1000p
pmまで低下させることができることとなる。しかも、
この残りの不溶性塩素分は、例えば硝酸などを用いて酸
洗することで除去することができる。これにより、全塩
素濃度を0に近づけることができる。According to the experiment of the inventor, the total chlorine concentration was 4100 ppm before the water washing as the desalting treatment, but it was lowered to about 2600 ppm by performing the predetermined water washing. At this time, the concentration of insoluble chlorine which was not eluted by washing with water was about 1000 ppm, which was the same as before the washing, relative to the total chlorine concentration. Therefore, when the water washing is sufficiently performed and the water-soluble chlorine concentration becomes close to 0, the total chlorine concentration becomes about 1000 p.
pm. Moreover,
The remaining insoluble chlorine can be removed by pickling with, for example, nitric acid. Thereby, the total chlorine concentration can be brought close to zero.
【0016】請求項6に記載の発明は、都市ごみ焼却灰
中から異物を除去し、しかもこの都市ごみ焼却灰中に含
まれる塩素分を除去した都市ごみ焼却灰から得られたセ
メント原料である。都市ごみ焼却灰から得られた5mm
以下のセメント原料の成分は、ポルトランドセメント用
のセメント原料の粘土原料、または、使用している鉄原
料の品位が低い工場における低品位の鉄原料に類似した
ものとなる。すなわち、例えば水分(11.4重量
%)、ig.loss(5.45重量%)、SiO
2(39.62重量%)、Al2O3(14.71重量
%)、Fe2O3(13.20重量%)、CaO(1
6.84重量%)、MgO(2.42重量%)、SO3
(0.68重量%)、Na2O(2.35重量%)、K
2O(1.41重量%)、TiO 2(1.40重量
%)、MnO(0.13重量%)、P2O5(1.50
重量%)、ZnO(0.26重量%)、Cr2O
3(0.04重量%)、CuO(0.20重量%)であ
る。このときの全塩素濃度は、例えば2600ppm程
度である。According to a sixth aspect of the present invention, there is provided municipal waste incineration ash.
Foreign matter is removed from the inside, and also included in this municipal solid waste incineration ash.
From municipal solid waste incineration ash from which chlorine
It is a raw material. 5mm obtained from municipal solid waste incineration ash
The following components of cement raw materials are used for Portland cement
Clay raw material of cement raw material or iron field used
Similar to low-grade iron raw materials in factories with low-grade materials
It will be. That is, for example, moisture (11.4 weight
%), Ig. loss (5.45% by weight), SiO
2(39.62% by weight), Al2O3(14.71 weight
%), Fe2O3(13.20% by weight), CaO (1
6.84% by weight), MgO (2.42% by weight), SO3
(0.68% by weight), Na2O (2.35% by weight), K
2O (1.41% by weight), TiO 2(1.40 weight
%), MnO (0.13% by weight), P2O5(1.50
Wt%), ZnO (0.26 wt%), Cr2O
3(0.04% by weight) and CuO (0.20% by weight).
You. At this time, the total chlorine concentration is, for example, about 2600 ppm.
Degrees.
【0017】ちなみに、セメント原料中の粘土原料の成
分は、通常、水分(10〜15重量%)、ig.los
s(4〜7重量%)、SiO2(65〜70重量%)、
Al 2O3(13〜15重量%)、Fe2O3(4〜6
重量%)、CaO(1〜3重量%)である。また、セメ
ント原料中の鉄原料の成分は、通常、水分(2〜8重量
%)、ig.loss(4〜5重量%)、SiO2(3
〜35重量%)、Al2O3(3〜8重量%)、Fe2
O3(20〜67重量%)、CaO(3〜30重量%)
である。異物が除去された都市ごみ焼却灰の大きさは、
前述したように粒径5mm以下が好ましい。[0017] Incidentally, the composition of the clay raw material in the cement raw material
Minutes are usually water (10-15% by weight), ig. los
s (4-7% by weight), SiO2(65-70% by weight),
Al 2O3(13 to 15% by weight), Fe2O3(4-6
% By weight) and CaO (1 to 3% by weight). In addition,
The component of the iron raw material in the cement raw material is usually water (2 to 8 weight
%), Ig. loss (4-5% by weight), SiO2(3
~ 35% by weight), Al2O3(3 to 8% by weight), Fe2
O3(20-67% by weight), CaO (3-30% by weight)
It is. The size of municipal solid waste incineration ash from which foreign matter has been removed
As described above, the particle size is preferably 5 mm or less.
【0018】[0018]
【作用】この発明の請求項1〜5に記載の都市ごみ焼却
灰のセメント原料化方法および請求項6に記載のセメン
ト原料によれば、都市ごみ焼却灰中からセメント原料と
して不要な異物や塩素分を除去する。これにより、セメ
ント原料中の低品位の粘土原料(または低品位の鉄原
料)と成分が類似した代替え用の原料が得られる。な
お、異物が除去されているので、セメント原料の焼成工
程やセメントクリンカの仕上げ工程において、通常のセ
メント原料と一体的に処理されても、なんら問題はな
い。また、塩素分が除去されているので、例えば通常の
セメント原料と混合し、焼成し、さらに石灰石を加えて
粉砕して製造されたセメントは、汎用のセメントと同様
に、多方面の用途に利用することができる。例えば、塩
素によって浸食されやすい鉄筋が埋め込まれた鉄筋コン
クリート用のセメントとしても利用することができる。According to the method for converting municipal solid waste incineration ash into a cement raw material according to the first to fifth aspects of the present invention and the cement raw material according to the sixth aspect, foreign matter or chlorine unnecessary as a cement raw material from the municipal waste incinerated ash. Remove the minute. As a result, a substitute raw material having components similar to the low-grade clay raw material (or the low-grade iron raw material) in the cement raw material can be obtained. In addition, since the foreign matter has been removed, there is no problem even if it is integrally treated with a normal cement raw material in the step of firing the cement raw material or the step of finishing the cement clinker. In addition, since the chlorine content has been removed, for example, cement manufactured by mixing with ordinary cement raw materials, firing, and adding limestone to pulverize, like general-purpose cement, can be used for various purposes can do. For example, it can be used as a cement for reinforced concrete in which a reinforcing bar which is easily eroded by chlorine is embedded.
【0019】特に、請求項2に記載の発明によれば、都
市ごみ焼却灰を分級して異物を除去し、かつこの焼却灰
中の塩素分を水洗により除去するので、この焼却灰中か
ら異物や塩素分を比較的容易かつ確実に除去することが
できる。In particular, according to the second aspect of the present invention, the incineration ash from municipal waste is classified to remove foreign matter, and the chlorine in the incineration ash is removed by washing with water. And chlorine can be relatively easily and reliably removed.
【0020】また、請求項3に記載の発明によれば、塩
素分の除去に先がけて都市ごみ焼却灰中から異物を除去
するので、都市ごみ焼却灰中からの塩素分の除去が効果
的に行え、比較的時間を要する塩素分の除去工程が、わ
りあい短時間で行える。According to the third aspect of the present invention, foreign matter is removed from the incineration ash of municipal waste prior to the removal of the chlorine content. A relatively time-consuming and relatively time-consuming step of removing chlorine can be performed in a relatively short time.
【0021】さらに、請求項4に記載の発明によれば、
都市ごみ焼却灰を管理型処分場の土中に埋設し、その
後、この埋められた灰の表面上に覆土をかぶせて、雨水
にさらすとともに、またスプリンクラー、散水車または
その他の散水設備を用いて、この覆土の上から強制的に
散水を行うので、比較的少ない設備コストで、かつ比較
的短期間に、この焼却灰中の塩素濃度を低減することが
できる。この結果、得られた代替え用の原料を、セメン
ト原料の一部として比較的多量に利用することができ
る。Further, according to the invention described in claim 4,
The municipal solid waste incineration ash is buried in the soil of a managed landfill and then covered with soil over the surface of the buried ash, exposed to rainwater, and also by using a sprinkler, water sprinkler or other watering equipment. Since the water is forcibly sprayed on the soil cover, the chlorine concentration in the incinerated ash can be reduced with a relatively small facility cost and in a relatively short time. As a result, the obtained substitute raw material can be used in a relatively large amount as a part of the cement raw material.
【0022】そして、請求項5に記載の発明によれば、
都市ごみ焼却灰中から塩素分を除去する際、都市ごみ焼
却灰を水洗するだけでなく、酸性溶液を用いる酸洗も行
う。これにより、この塩素分の一部を構成する水溶性の
塩素分だけでなく、残りの成分である不溶性の塩素分も
除去することができる。この結果、得られたセメント原
料の塩素分をさらに低減することができる。よって、こ
の都市ごみ焼却灰から得られた原料を、より大きい割合
で、通常のセメント原料の一部に置き換えることができ
る。According to the invention described in claim 5,
When removing chlorine from municipal solid waste incineration ash, not only municipal solid waste incineration ash is washed with water, but also acid pickling using an acidic solution is performed. This makes it possible to remove not only the water-soluble chlorine constituting a part of the chlorine but also the insoluble chlorine which is the remaining component. As a result, the chlorine content of the obtained cement raw material can be further reduced. Therefore, the raw material obtained from the municipal solid waste incineration ash can be replaced with a larger proportion of the normal cement raw material.
【0023】[0023]
【発明の実施の形態】以下、この発明の実施例を説明す
る。図1は、この発明の一実施例に係る都市ごみ焼却灰
のセメント原料化方法が適用された都市ごみ焼却灰のセ
メント原料化設備の全体構成図である。図2は、都市ご
み焼却灰の水洗による塩素除去工程を示す構成図であ
る。この発明の一実施例に係る都市ごみ焼却灰から得ら
れたセメント原料(代替えセメント原料)は、以下のよ
うにして製造された。すなわち、図1に示す都市ごみ焼
却灰のセメント原料化設備(以下、単にセメント原料化
設備という)10において、まず都市ごみ焼却灰11を
分級した後、この都市ごみ焼却灰11中の塩素分を水洗
により除去する。まず、都市ごみ焼却灰11の分級工程
を説明する。Embodiments of the present invention will be described below. FIG. 1 is an overall configuration diagram of a municipal solid waste incineration ash cement raw material applying apparatus to which a municipal solid waste incinerated ash method according to an embodiment of the present invention is applied. FIG. 2 is a configuration diagram showing a chlorine removal step by washing municipal waste incineration ash with water. A cement raw material (alternative cement raw material) obtained from municipal solid waste incineration ash according to one embodiment of the present invention was produced as follows. That is, in the municipal solid waste incineration ash 11 shown in FIG. 1, the municipal solid waste incineration ash 11 is first classified, and then the chlorine content in the municipal solid waste incineration ash 11 is classified. Remove by washing with water. First, the classification process of the municipal waste incineration ash 11 will be described.
【0024】すなわち、図1に示すように、自治体のご
み処理工場から運搬されてきた都市ごみ焼却灰11を、
網目サイズが65mmのふるい網12aが張られた粗分
級用の分級機12に供給する。網上に空き缶,鉄くず,
未燃の電話帳などが残り、網下から65mm以下の都市
ごみ焼却灰11が得られる。この65mm以下まで分級
された都市ごみ焼却灰11は、やや粗い網目サイズが2
0mmのふるい網13aを有する分級機13へ送られ
る。ここでは、分級することで、網上に空き缶,ガラ
ス,陶器片,大型のフォークなどが残り、網下から20
mm以下の都市ごみ焼却灰11が得られる。その後、こ
の20mm以下の都市ごみ焼却灰11を、網目サイズが
5mmのふるい網14aを有する分級機14へ投入す
る。網上には釘,ボルト・ナット類,小型フォークなど
が残る一方、網下からは5mm以下の都市ごみ焼却灰1
1が得られる。次に、この得られた5mm以下の都市ご
み焼却灰11の塩素除去工程を説明する。That is, as shown in FIG. 1, municipal solid waste incineration ash 11 transported from a municipal waste treatment plant is
The sieve is supplied to a classifier 12 for coarse classification, which has a sieve mesh 12a having a mesh size of 65 mm. Empty cans, scrap iron,
Unburned telephone directories and the like remain, and municipal waste incineration ash 11 of 65 mm or less is obtained from under the net. The municipal waste incineration ash 11 classified to 65 mm or less has a slightly coarse mesh size of 2.
It is sent to a classifier 13 having a sieve screen 13a of 0 mm. Here, by classification, empty cans, glass, pottery pieces, large forks, etc., remain on the net, and 20
The municipal solid waste incineration ash 11 mm or less is obtained. Thereafter, the municipal waste incineration ash 11 having a size of 20 mm or less is put into a classifier 14 having a sieve 14a having a mesh size of 5 mm. While nails, bolts and nuts, small forks, etc. remain on the net, municipal waste incineration ash 1 mm or less from below the net
1 is obtained. Next, the chlorine removal process of the obtained incinerated ash 11 of 5 mm or less in municipal waste will be described.
【0025】すなわち、図1に示すように、まずショベ
ルカーなどにより、管理型処分場に大きなごみ焼却灰投
入穴15を掘削する。それから、このごみ焼却灰投入穴
15に5mm以下の都市ごみ焼却灰11を投入し、その
表面を覆土16によりおおう。これは、強風などで都市
ごみ焼却灰11の表層部が飛散しないようにするためで
ある。この状態で、3.5ヵ月間、雨水にさらす(この
間の総降雨量は471mm)。次に、散水車17または
スプリンクラー18により、この覆土16上から強制的
に散水する(全散水量116t)。こうして、都市ごみ
焼却灰11中に含まれる塩素分を水洗・除去する。な
お、強制散水を併用するので、このごみ焼却灰投入穴1
5に埋設された都市ごみ焼却灰11は、18ヵ月間、雨
水にさらされた状態と同じになる(年間降雨量を160
0mmとして換算)。こうすることで、塩素分が260
0ppm以下まで除去された5mm以下の代替えセメン
ト原料aが得られる。That is, as shown in FIG. 1, a large refuse incineration ash charging hole 15 is firstly excavated in a managed landfill using a shovel car or the like. Then, the municipal solid waste incineration ash 11 having a size of 5 mm or less is put into the refuse incineration ash charging hole 15, and the surface thereof is covered with the soil cover 16. This is to prevent the surface layer portion of the municipal waste incineration ash 11 from scattering due to a strong wind or the like. In this state, it is exposed to rainwater for 3.5 months (total rainfall during this period is 471 mm). Next, water is forcibly sprayed from above the covering soil 16 by the watering truck 17 or the sprinkler 18 (total watering amount 116t). Thus, chlorine contained in the municipal waste incineration ash 11 is washed and removed with water. Since forced watering is also used, this waste incineration ash injection hole 1
The municipal solid waste incineration ash 11 buried in 5 will be the same as that exposed to rainwater for 18 months (with an annual rainfall of 160
0 mm). By doing so, chlorine content is 260
An alternative cement material a of 5 mm or less removed to 0 ppm or less is obtained.
【0026】代替えセメント原料aに含まれる各成分量
は、粉末X線回析法により分析したところ、上記「課題
を解決するための手段」(段落番号「0015」)に記
載したものとほぼ同じであった。なお、水洗後の都市ご
み焼却灰11を、例えば硝酸により酸性すれば、この都
市ごみ焼却灰11中から水溶性の塩素だけでなく水に溶
けない不溶性塩素をも除去することができ、セメント原
料として有害な塩素分をさらに低減することができ、よ
り大きな割合で、この灰11中から得られた代替えセメ
ント原料aを、既存の通常セメント原料bの一部として
利用することができる。The amounts of the respective components contained in the alternative cement raw material a were analyzed by a powder X-ray diffraction method and found to be substantially the same as those described in the above “Means for Solving the Problems” (paragraph number “0015”). Met. If the municipal solid waste incineration ash 11 after washing with water is acidified with, for example, nitric acid, not only water-soluble chlorine but also insoluble chlorine that is insoluble in water can be removed from the municipal waste incineration ash 11, and cement raw material can be removed. The harmful chlorine content can be further reduced, and the replacement cement raw material a obtained from the ash 11 can be used as a part of the existing normal cement raw material b in a larger ratio.
【0027】所定の雨ざらし(散水を含む)期間を終え
た代替えセメント原料aは、その後、ごみ焼却灰投入穴
15から掘り出される。それから、図外のセメント原料
貯蔵サイロよりパイプ移送された通常セメント原料bと
ともに、プレヒータ19へ投入される。なお、このとき
の混合比は、代替えセメント原料a:通常セメント原料
b=1:4000である。セメント原料a,bは、プレ
ヒータ19の通過中、1000℃近くまで仮焼される。
その後、乾式セメントキルン20へと投入される。ここ
で焼成されて、セメントクリンカ21が中間製造され
る。得られたセメントクリンカ21は、図外のクリンカ
クーラにより冷やされ、それから石膏を添加して仕上げ
ミル内で粉砕される。そして、袋詰めされてから出荷さ
れる。なお、前述したように都市ごみ焼却灰11は、分
級工程で5mm以下に分級されているので、代替えセメ
ント原料a中から小型フォークなどの金属片がほぼ完全
に除去されている。これにより、仕上げミルで粉砕した
後は、このミルの内部に異物が残らず、セメント原料
a,bを良好に粉砕することができる。The alternative cement raw material a after a predetermined rain exposure (including watering) period is excavated from the refuse incineration ash charging hole 15. Then, it is put into the preheater 19 together with the normal cement raw material b transferred from a cement raw material storage silo (not shown). The mixing ratio at this time is: substitute cement raw material a: normal cement raw material b = 1: 4000. The cement raw materials a and b are calcined to near 1000 ° C. while passing through the preheater 19.
After that, it is put into the dry cement kiln 20. Here, it is fired, and the cement clinker 21 is intermediately manufactured. The obtained cement clinker 21 is cooled by a clinker cooler (not shown), and then added with gypsum and pulverized in a finishing mill. Then, they are packed and then shipped. As described above, since the municipal waste incineration ash 11 is classified to 5 mm or less in the classification step, metal pieces such as small forks are almost completely removed from the substitute cement raw material a. Thereby, after crushing by the finishing mill, no foreign matter remains in the inside of the mill, and the cement raw materials a and b can be crushed well.
【0028】このように、都市ごみ焼却灰11中からセ
メント原料として不適な異物や塩素分を取り除くように
したので、都市ごみ焼却灰11から得られた代替えセメ
ント原料aを、汎用性のある既存の通常セメント原料b
の一部として利用することができる。また、この都市ご
み焼却灰11中に含まれる異物を、それぞれ網目サイズ
が異なるふるい網12a(65mm分級)、13a(2
0mm分級)、14a(5mm分級)を有する分級機1
2〜14により分級することで除去するようにし、しか
もこの都市ごみ焼却灰11中の塩素分を水洗により除去
するようにしたので、都市ごみ焼却灰11中からの異物
および塩素分の除去を比較的容易で、しかも確実に行う
ことができる。As described above, the foreign matter and chlorine which are not suitable as the cement raw material are removed from the municipal waste incineration ash 11. Therefore, the alternative cement raw material a obtained from the municipal waste incineration ash 11 can be used as a general-purpose existing ash. Normal cement raw material b
Can be used as part of In addition, foreign substances contained in the municipal solid waste incineration ash 11 are separated into sieve nets 12a (classified by 65 mm) and 13a (2
Classifier 1 having 0 mm classification) and 14a (5 mm classification)
Since the chlorine in the municipal waste incineration ash 11 was removed by washing with water, the foreign matter and chlorine in the municipal waste incineration ash 11 were compared. It is easy and reliable.
【0029】さらに、この異物の除去と、塩素分の除去
とは、まず異物を除去後に塩素分を除去するようにした
ので、この都市ごみ焼却灰11中からの塩素分の除去を
効果的に行うことができる。さらにまた、この塩素分の
除去を、管理型処分場での雨ざらし法により行い、しか
も散水車17やスプリンクラー18を用いて強制散水も
行うようにしたので、比較的少ない設備コストで、かつ
比較的短期間に、この灰11中の塩素濃度を低減するこ
とができる。そして、この実施例では、都市ごみ焼却灰
11中の塩素分を2600ppm以下まで下げるように
したので、通常セメント原料bの一部として比較的多量
にこの代替えセメント原料aを利用することができる。
なお、都市ごみ焼却灰11が埋設されたのは、管理型処
分場であるので、洗浄後の塩素分を含む水は、この処分
場に通常配備された処理設備により無害化される。Further, the removal of the foreign matter and the removal of the chlorine content mean that the chlorine content is first removed and then the chlorine content is removed. Therefore, the removal of the chlorine content from the municipal waste incineration ash 11 can be effectively performed. It can be carried out. Furthermore, since the chlorine content is removed by the rain method in a controlled disposal site, and forced watering is also performed by using a watering truck 17 and a sprinkler 18, the facility cost is relatively low and the cost is relatively low. In a short period of time, the chlorine concentration in the ash 11 can be reduced. In this embodiment, the chlorine content in the municipal waste incineration ash 11 is reduced to 2600 ppm or less, so that a relatively large amount of the substitute cement raw material a can be used as a part of the cement raw material b.
Since the municipal solid waste incineration ash 11 is buried in the management-type disposal site, the water containing chlorine after cleaning is rendered harmless by the processing equipment normally provided in this disposal site.
【0030】ここで、図2を参照しながら、都市ごみ焼
却灰11の水洗工程を試験した結果を説明する。なお、
ここでは、都市ごみ焼却灰11として、分級前のものを
採用している。図2に示すように、まずショベルカーな
どにより埋立て場(管理型処分場)に底面5×7m、上
面7×9m、深さ1.3mのごみ焼却灰投入穴15を掘
削した。その後、この穴15内に深さ1.2mまで分級
前の都市ごみ焼却灰11を投入した。なお、この都市ご
み焼却灰11は、所定自治体のごみ処理工場から持ち込
まれた、一般ごみを焼却したものである。その後、この
都市ごみ焼却灰11の表面に、100〜200mmの覆
土16をかぶせ、一年間程度、屋外で雨ざらしにするこ
とを想定し、散水車17やスプリンクラー18を用い
て、強制的な散水を実施した。試験期間は、約3ヵ月半
である。この間、この地域に実際に降った累積雨量は4
71mmである。そして、強制的に散水した散水量は、
116t(降雨換算で1800mm)であった。その結
果、ここのごみ処理場の年平均降雨量は、1600mm
程度であり、年平均降雨量換算で、この水量は約1年半
分となった。Here, referring to FIG. 2, the result of testing the washing process of the municipal waste incineration ash 11 will be described. In addition,
Here, the municipal solid waste incineration ash 11 is the one before classification. As shown in FIG. 2, first, a waste incineration ash input hole 15 having a bottom surface of 5 × 7 m, an upper surface of 7 × 9 m, and a depth of 1.3 m was excavated in a landfill (managed disposal site) using a shovel truck or the like. Thereafter, the municipal solid waste incineration ash 11 before classification was put into the hole 15 to a depth of 1.2 m. The municipal solid waste incineration ash 11 is obtained by incinerating general refuse brought from a municipal waste treatment plant. Then, cover the surface of the municipal incineration ash 11 with a covering soil 16 of 100 to 200 mm, and suppose that it will be raining outdoors for about one year, and use a watering truck 17 or a sprinkler 18 to forcibly spray water. Carried out. The test period is about three and a half months. During this period, the cumulative rainfall that actually fell in this area was 4
71 mm. And the amount of water sprayed forcibly is
It was 116 t (1800 mm in terms of rainfall). As a result, the annual average rainfall at the landfill here is 1600 mm
This amount is about one and a half years in terms of annual average rainfall.
【0031】試料のサンプリングは次の方法で行った。
なお、各試料はJIS網ふるいで分級した30mm以下
のものとし、しかも予め目視により鉄くずなどの異物を
除去しておいた。水洗処理前の試料には、埋設された都
市ごみ焼却灰11の任意の3箇所からサンプリングし、
それらを混合した試料を使用した。水洗処理後の試料に
は、図2に示したように水平方向に3点の位置(ごみ焼
却灰投入穴15の同図左右両端から各1.8mの位置
(1),(3)および中央位置(2))をとり、各
(1)〜(3)の位置において、深さ方向へ200m
m,500mm,1000mmでサンプリングした試料
と、これら全部を混合した試料とを使用した。また、塩
素濃度分析方法としては、JIS(R5202)の塩素
濃度定量方法に準じ、比色法により分析した。ただし、
水溶性塩素濃度は、試料2gに対して水100mlを加
え、その後、30分間攪拌して、それを濾過し、水洗し
た濾液を分析した。以下、その分析結果を示す。The sample was sampled by the following method.
Each sample had a size of 30 mm or less classified by a JIS screen sieve, and foreign matters such as iron chips had been visually removed in advance. For the sample before the washing process, sample from any three places of the buried municipal waste incineration ash 11,
The sample which mixed them was used. As shown in FIG. 2, the sample after the water washing treatment had three positions in the horizontal direction (the positions (1), (3) at 1.8 m each from the left and right ends of the refuse incineration ash charging hole 15 and the center). Position (2)), and at each of the positions (1) to (3), 200 m in the depth direction
Samples sampled at m, 500 mm, and 1000 mm and a sample obtained by mixing all of them were used. The chlorine concentration was analyzed by a colorimetric method according to the chlorine concentration determination method of JIS (R5202). However,
The water-soluble chlorine concentration was determined by adding 100 ml of water to 2 g of the sample, stirring the mixture for 30 minutes, filtering it, and analyzing the filtrate washed with water. Hereinafter, the analysis results are shown.
【0032】水洗処理前の塩素濃度は、試料中に含まれ
るすべての塩素濃度である全塩素濃度では、水洗前41
00ppmであった。これが、今回実施した程度の水洗
処理でも1000ppm近くまで全塩素濃度が低下する
ことが確認できた。次に、表1を用いて、水洗処理後の
位置別の塩素濃度を説明する。The chlorine concentration before the water rinsing treatment is the same as the total chlorine concentration which is the concentration of all chlorine contained in the sample.
It was 00 ppm. It was confirmed that the total chlorine concentration was reduced to nearly 1000 ppm even with the water washing treatment performed this time. Next, the chlorine concentration at each position after the water washing process will be described with reference to Table 1.
【0033】[0033]
【表1】 [Table 1]
【0034】各数値は、図2に示した(1)〜(3)の
位置でサンプリングした試料に基づいて調べた結果であ
る。表1から次のことが明らかになった。すなわち、不
溶性塩素濃度は、各試料とも、約1000ppm前後で
一定している。このような試験からも、都市ごみ焼却灰
11を水洗することが、この都市ごみ焼却灰11中から
塩素分を除去することに有効であることが判明した。Each numerical value is a result obtained by examining a sample sampled at the positions (1) to (3) shown in FIG. The following has become clear from Table 1. That is, the concentration of insoluble chlorine is constant at about 1000 ppm for each sample. From such a test, it was found that washing the municipal waste incineration ash 11 with water was effective in removing chlorine from the municipal waste incineration ash 11.
【0035】[0035]
【発明の効果】以上説明してきたように、この発明に係
る都市ごみ焼却灰のセメント原料化方法およびこの方法
から得られたセメント原料によれば、都市ごみ焼却灰中
からセメント原料には不適な異物や塩素分を取り除くよ
うにしたので、都市ごみ焼却灰から得られたセメント原
料を、汎用性のある既存のセメント原料(ポルトランド
セメント用)の一部として利用することができる。As described above, according to the method for converting municipal solid waste incineration ash into a cement raw material and the cement raw material obtained by this method according to the present invention, unsuitable cement raw material from municipal solid waste incinerated ash is used. Since foreign substances and chlorine are removed, cement raw materials obtained from municipal waste incineration ash can be used as a part of general-purpose existing cement raw materials (for Portland cement).
【0036】特に、請求項2に記載の発明によれば、異
物を分級により除去し、かつ塩素分を水洗により除去す
るようにしたので、都市ごみ焼却灰中からの異物および
塩素分の除去を比較的容易で、しかも確実に行うことが
できる。In particular, according to the second aspect of the invention, the foreign matter is removed by classification and the chlorine content is removed by washing with water. Relatively easy and reliable.
【0037】さらに、請求項3に記載の発明によれば、
都市ごみ焼却灰中から異物と塩素分を除去するに際し
て、まず異物を除去した後、塩素分を除去するようにし
たので、この焼却灰中からの塩素分の除去を効果的に行
うことができる。Further, according to the third aspect of the present invention,
When removing foreign matter and chlorine from municipal solid waste incineration ash, the foreign matter is first removed and then the chlorine content is removed, so the chlorine content can be effectively removed from this incineration ash. .
【0038】さらにまた、請求項4に記載の発明によれ
ば、この塩素分の除去を、管理型処分場に都市ごみ焼却
灰を埋設して雨水にさらすとともに、しかも覆土の上か
らスプリンクラー、散水車またはその他の散水設備を用
いて強制散水するようにしたので、比較的少ない設備コ
ストで、かつ比較的短期間に、この焼却灰中の塩素濃度
を低減することができる。Further, according to the invention of claim 4, this chlorine content can be removed by burying municipal waste incineration ash in a controlled disposal site and exposing it to rainwater, and furthermore, sprinklers and water sprinkling from over the soil cover. Since the forced watering is performed by using a car or other watering equipment, the chlorine concentration in the incinerated ash can be reduced at a relatively low equipment cost and in a relatively short time.
【0039】そして、請求項5に記載の発明によれば、
この塩素除去工程を、水洗および酸洗により行うように
したので、この焼却灰中から水溶性の塩素分だけでなく
水に溶けない不溶性塩素分をも除去することができ、セ
メント原料として有害な塩素分をさらに低減し、より以
上の割合で、この焼却灰中から得られたセメント原料
を、既存セメントとして利用することができる。According to the fifth aspect of the present invention,
Since this chlorine removal step is performed by washing with water and pickling, not only water-soluble chlorine but also insoluble chlorine which is not soluble in water can be removed from the incinerated ash, which is harmful as a raw material for cement. The chlorine content is further reduced, and the cement raw material obtained from the incineration ash can be used as the existing cement at a higher ratio.
【図1】この発明の一実施例に係る都市ごみ焼却灰のセ
メント原料化方法が適用された都市ごみ焼却灰のセメン
ト原料化設備の全体構成図である。FIG. 1 is an overall configuration diagram of a facility for converting municipal waste incineration ash into a cement raw material to which a method for converting municipal waste incineration ash into a cement raw material according to an embodiment of the present invention is applied.
【図2】都市ごみ焼却灰の水洗による塩素除去工程を示
す構成図である。FIG. 2 is a configuration diagram showing a chlorine removal step by washing municipal waste incineration ash with water.
【符号の説明】 10 都市ごみ焼却灰のセメント原料化設備、 11 都市ごみ焼却灰、 15 ごみ焼却灰投入穴、 16 覆土、 17 散水車、 18 スプリンクラー、 a 代替えセメント原料、 b 通常セメント原料。[Description of Signs] 10 Municipal solid waste incineration ash as a cement raw material facility, 11 Municipal solid waste incineration ash, 15 Waste incineration ash input hole, 16 Cover soil, 17 Water sprinkler, 18 Sprinkler, a Alternative cement raw material, b Normal cement raw material.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI // B09B 1/00 ZAB B09B 5/00 N (72)発明者 山▲崎▼ 正康 福岡県北九州市八幡西区洞南町1番1号 三菱マテリアル株式会社セメント開発セン ター内 (72)発明者 橋本 光一 福岡県北九州市八幡西区洞南町1番1号 三菱マテリアル株式会社セメント開発セン ター内 (72)発明者 石▲崎▼ 倫朗 福岡県北九州市八幡西区洞南町1番1号 三菱マテリアル株式会社セメント開発セン ター内────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification symbol FI // B09B 1/00 ZAB B09B 5/00 N (72) Inventor Yama ▲ saki ▼ Masayasu No.1 Donanmachi, Yawatanishi-ku, Kitakyushu-shi, Fukuoka Prefecture No. 1 In the Cement Development Center of Mitsubishi Materials Corporation (72) Inventor Koichi Hashimoto No. 1-1 Donan-cho, Yawata-nishi-ku, Kitakyushu-shi, Fukuoka Prefecture In the Cement Development Center of Mitsubishi Materials Corporation (72) Inventor Toshiro Ishi ▲ Saki ▼ Fukuoka 1-1, Dongnan-cho, Yawatanishi-ku, Kitakyushu-shi, Japan Mitsubishi Materials Corporation Cement Development Center
Claims (6)
程と、 都市ごみ焼却灰中に含まれる塩素分を除去する工程とを
備えた都市ごみ焼却灰のセメント原料化方法。1. A method for converting municipal solid waste incineration ash into a cement raw material, comprising: a step of removing foreign matter from municipal waste incineration ash; and a step of removing chlorine contained in the municipal waste incineration ash.
級により行われ、上記塩素除去工程が都市ごみ焼却灰の
水洗により行われる請求項1に記載の都市ごみ焼却灰の
セメント原料化方法。2. The method according to claim 1, wherein the foreign matter removing step is performed by classifying the municipal incineration ash, and the chlorine removing step is performed by washing the municipal incineration ash with water.
理は、上記異物除去工程を行った後、上記塩素除去工程
を行う請求項1または請求項2に記載の都市ごみ焼却灰
のセメント原料化方法。3. The municipal solid waste incinerated ash according to claim 1 or 2, wherein the municipal solid waste incinerated ash is subjected to the chlorine removing step after performing the foreign matter removing step. Method.
た状態で都市ごみ焼却灰を管理型処分場の土中に埋設
し、その後、雨水にさらす以外に、スプリンクラー、散
水車またはその他の散水設備によって強制散水する請求
項1〜請求項3のうちのいずれか1項に記載の都市ごみ
焼却灰のセメント原料化方法。4. The chlorine removing step comprises burying municipal waste incineration ash in the soil of a controlled disposal site with the surface covered with soil, and then exposing the ash to rainwater, or using a sprinkler, water sprinkler or other The method for converting municipal waste incineration ash into a cement material according to any one of claims 1 to 3, wherein water is forcibly sprayed by a water spraying facility.
を、水洗することにより、および、酸性溶液を用いて酸
洗することにより行われる請求項1〜請求項4のうちの
いずれか1項に記載の都市ごみ焼却灰のセメント原料化
方法。5. The chlorine removal step according to claim 1, wherein the municipal solid waste incineration ash is washed with water and pickled with an acidic solution. Method for converting municipal solid waste incineration ash into a cement raw material as described in 1 above.
かもこの都市ごみ焼却灰中に含まれる塩素分を除去した
都市ごみ焼却灰から得られたセメント原料。6. A cement raw material obtained from municipal waste incinerated ash from which foreign substances have been removed from the municipal waste incinerated ash and from which chlorine contained in the municipal waste incinerated ash has been removed.
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JP13718698A JP4067641B2 (en) | 1998-05-19 | 1998-05-19 | Method for converting municipal waste incineration ash to cement |
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Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13718698A JP4067641B2 (en) | 1998-05-19 | 1998-05-19 | Method for converting municipal waste incineration ash to cement |
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Publication Number | Publication Date |
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JPH11322381A true JPH11322381A (en) | 1999-11-24 |
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Family
ID=15192822
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JP13718698A Expired - Fee Related JP4067641B2 (en) | 1998-05-19 | 1998-05-19 | Method for converting municipal waste incineration ash to cement |
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JP2009233489A (en) * | 2008-03-25 | 2009-10-15 | Taiheiyo Cement Corp | Treatment method and treatment system for incinerated residue |
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Cited By (8)
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JP2003103232A (en) * | 2001-07-26 | 2003-04-08 | Tokuyama Corp | Method for treating incineration ash |
JP2008253881A (en) * | 2007-04-02 | 2008-10-23 | Taiheiyo Cement Corp | Incineration fly ash-treating method |
JP2009119407A (en) * | 2007-11-16 | 2009-06-04 | Kurita Water Ind Ltd | Desalinization accelerator of ash and desalinization method of the ash |
JP2009208990A (en) * | 2008-03-04 | 2009-09-17 | Ube Ind Ltd | Method and system for transporting moisture-containing powder |
JP2009227528A (en) * | 2008-03-25 | 2009-10-08 | Ube Ind Ltd | Method for transporting reclaimed ash |
JP2009233489A (en) * | 2008-03-25 | 2009-10-15 | Taiheiyo Cement Corp | Treatment method and treatment system for incinerated residue |
JP2022045008A (en) * | 2020-09-08 | 2022-03-18 | 太平洋セメント株式会社 | Producing method of cement or hardened cementitious material and producing system thereof |
CN114163150A (en) * | 2021-07-23 | 2022-03-11 | 深圳市能源环保有限公司 | Method for preparing cementing material by using water-washed waste incineration fly ash and application |
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