JPH10110176A - Production of solid fuel from waste material - Google Patents
Production of solid fuel from waste materialInfo
- Publication number
- JPH10110176A JPH10110176A JP26409096A JP26409096A JPH10110176A JP H10110176 A JPH10110176 A JP H10110176A JP 26409096 A JP26409096 A JP 26409096A JP 26409096 A JP26409096 A JP 26409096A JP H10110176 A JPH10110176 A JP H10110176A
- Authority
- JP
- Japan
- Prior art keywords
- waste
- raw material
- cement
- process product
- combustible waste
- 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.)
- Withdrawn
Links
- 239000002699 waste material Substances 0.000 title claims description 28
- 238000004519 manufacturing process Methods 0.000 title claims description 12
- 239000004449 solid propellant Substances 0.000 title abstract 3
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims abstract description 50
- 239000000292 calcium oxide Substances 0.000 claims abstract description 25
- 235000012255 calcium oxide Nutrition 0.000 claims abstract description 25
- 239000004568 cement Substances 0.000 claims abstract description 24
- 238000000034 method Methods 0.000 claims abstract description 21
- 239000002994 raw material Substances 0.000 claims abstract description 21
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 11
- 239000000725 suspension Substances 0.000 claims abstract description 10
- 238000011282 treatment Methods 0.000 claims abstract description 9
- 238000010438 heat treatment Methods 0.000 claims abstract description 6
- 239000000446 fuel Substances 0.000 claims description 21
- 238000010304 firing Methods 0.000 claims description 7
- 238000000465 moulding Methods 0.000 claims description 4
- 239000010849 combustible waste Substances 0.000 abstract description 19
- 230000018044 dehydration Effects 0.000 abstract description 3
- 238000006297 dehydration reaction Methods 0.000 abstract description 3
- 230000001954 sterilising effect Effects 0.000 abstract description 3
- 238000004659 sterilization and disinfection Methods 0.000 abstract description 3
- 238000004332 deodorization Methods 0.000 abstract description 2
- 239000000463 material Substances 0.000 abstract 3
- 239000011369 resultant mixture Substances 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 229910052799 carbon Inorganic materials 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 3
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 3
- 239000000920 calcium hydroxide Substances 0.000 description 3
- 235000011116 calcium hydroxide Nutrition 0.000 description 3
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 235000019738 Limestone Nutrition 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 238000000748 compression moulding Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000006028 limestone Substances 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 2
- XURIQWBLYMJSLS-UHFFFAOYSA-N 1,4,7,10-tetrazacyclododecan-2-one Chemical compound O=C1CNCCNCCNCCN1 XURIQWBLYMJSLS-UHFFFAOYSA-N 0.000 description 1
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- -1 and the like Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000010850 non-combustible waste Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
Description
【０００１】[0001]
【発明の属する技術分野】本発明は、家庭ゴミ、一般ゴ
ミ等の廃棄物を、生石灰を含む処理剤により処理して、
固形化燃料を製造する廃棄物からの固形化燃料の製造方
法に関する。The present invention relates to a method for treating waste such as household waste and general waste with a treatment agent containing quicklime.
The present invention relates to a method for producing solidified fuel from waste for producing solidified fuel.
【０００２】[0002]
【従来の技術】従来の廃棄物から固形化燃料を製造する
方法は、 （１）廃棄物を破砕する （２）破砕された廃棄物中の可燃物と不燃物とを選別す
る （３）選別された可燃性廃棄物に処理剤として生石灰を
混合して処理する （４）処理された可燃性廃棄物を圧縮・成形・乾燥して
固形化燃料とする 等の工程からなっており、特開平６−１０８０７５号公
報等に開示されている。2. Description of the Related Art Conventional methods for producing solidified fuel from waste include: (1) crushing waste; (2) sorting combustibles and non-combustibles in crushed waste; and (3) sorting. Mixing the treated combustible waste with quick lime as a treating agent and treating it. (4) Compression, molding and drying of the treated combustible waste to obtain a solidified fuel. It is disclosed in, for example, JP-A-6-108075.
【０００３】[0003]
【発明が解決しようとする課題】上述の廃棄物に生石灰
を混合して処理する工程においては、生石灰と廃棄物中
の水分とが以下のように反応し、廃棄物中の水分が、こ
の水和反応に消費され、又は反応熱により蒸発すること
によって、廃棄物が脱水される。また、これにより発生
した消石灰によって、ｐＨが強アルカリ性となるため、
廃棄物中の微生物は殺菌され、有機物の腐敗が抑制され
る。 ＣａＯ＋Ｈ2 Ｏ→Ｃａ（ＯＨ）2 In the above-mentioned process of mixing quicklime with waste and treating it, quicklime and water in the waste react as follows, and the water in the waste is converted into water. The waste is dehydrated by being consumed in the summation reaction or being evaporated by the heat of reaction. In addition, since the pH becomes strongly alkaline due to slaked lime generated by this,
Microorganisms in waste are sterilized, and spoilage of organic matter is suppressed. CaO + H 2 O → Ca (OH) 2
【０００４】しかし、処理剤として生石灰を使用する場
合は、生石灰が高価でありコスト的に問題があり、ま
た、生石灰は一般的に粒状のものが使用されるため、廃
棄物との混合が十分でなく、上記反応が不均一になる等
の問題があった。[0004] However, when quicklime is used as a treating agent, quicklime is expensive and there is a problem in terms of cost. In addition, since quicklime is generally used in a granular form, it cannot be sufficiently mixed with waste. However, there is a problem that the above reaction becomes non-uniform.
【０００５】本発明は、このような従来の問題に鑑み、
廃棄物から固形化燃料を経済的かつ効率的に製造するこ
とができる廃棄物からの固形化燃料の製造方法の提供を
目的としたものである。The present invention has been made in view of such a conventional problem,
It is an object of the present invention to provide a method for producing solidified fuel from waste, which can economically and efficiently produce solidified fuel from waste.
【０００６】[0006]
【課題を解決するための手段】上述の如き従来の問題を
解決し、所期の目的を達成するための本発明の特徴は、
破砕された廃棄物に生石灰を含む処理剤を混合して処理
した後に成形して固形化燃料を製造する廃棄物からの固
形化燃料の製造方法において、前記処理剤は、セメント
焼成系のサスペンションプレヒーターから分取され、セ
メント原料を加熱して得られる生石灰を含む中間工程品
であることにある。SUMMARY OF THE INVENTION The features of the present invention for solving the conventional problems as described above and achieving the intended purpose are as follows.
In a method for producing a solidified fuel from waste, which comprises mixing and treating a crushed waste with a treatment agent containing quick lime, and then molding to produce a solidified fuel, the treatment agent comprises a cement firing suspension suspension. It is an intermediate process product containing quicklime that is separated from a heater and obtained by heating a cement raw material.
【０００７】[0007]
【発明の実施の形態】次に本発明の実施の形態を図面に
ついて説明する。Embodiments of the present invention will now be described with reference to the drawings.
【０００８】セメント工場においては、図１に示すよう
に、セメント原料Ｌが、原料貯蔵場１から、原料乾燥機
２、原料粉砕機３、原料タンク４を介して、セメント焼
成系のサスペンションプレヒーターに供給されるように
なっている。なお、セメント原料Ｌは石灰石、粘土、珪
石、鉄原料等からなり、これを加熱して得られる中間工
程品Ｑ（後述）は生石灰に比して一般的に安価である。In a cement factory, as shown in FIG. 1, a cement raw material L is supplied from a raw material storage site 1 through a raw material dryer 2, a raw material crusher 3, and a raw material tank 4 to a cement pre-heating suspension preheater. It is supplied to. Note that the cement raw material L is made of limestone, clay, silica stone, iron raw material, and the like, and an intermediate process product Q (described later) obtained by heating the raw material is generally less expensive than quick lime.
【０００９】セメント焼成系のサスペンションプレヒー
ターは、複数段のサイクロン５、６、７、８、仮焼炉９
をもって構成されており、ロータリーキルン１０の排ガ
スが、仮焼炉９、サイクロン８、７、６、５へ順に供給
されるようになっている。そして、最上段のサイクロン
５にセメント原料Ｌが投入され、このセメント原料Ｌが
最下段のサイクロン８に達するまでに８５０°Ｃ〜９０
０°Ｃに加熱されて、セメント原料Ｌ中の石灰石の脱炭
酸化により以下のように生石灰が生成される。 ＣａＣＯ3 →ＣａＯ＋ＣＯ2 [0009] The suspension preheater of the cement firing system comprises a plurality of stages of cyclones 5, 6, 7, 8 and a calciner 9
The exhaust gas of the rotary kiln 10 is sequentially supplied to the calciner 9 and the cyclones 8, 7, 6, and 5. Then, the cement raw material L is supplied to the cyclone 5 at the uppermost stage, and the cement raw material L reaches 850 ° C. to 90 ° C. until the cement raw material L reaches the cyclone 8 at the lowermost stage.
Heated to 0 ° C., limestone in the cement raw material L is decarboxylated to produce quicklime as follows. CaCO 3 → CaO + CO 2
【００１０】なお、最下段のサイクロン８までの中間工
程品Ｑの主な成分は、一例として、ＳｉＯ2 １９．０
％、Ａｌ2 Ｏ3 ４．３％、Ｆｅ2 Ｏ3 ２．７％、Ｃ
ａＯ ６０．５％、ＭｇＯ １．５％となっており、生
石灰を十分に含有している。また、中間工程品Ｑは、微
粉末状になっており、約０．５％の未燃カーボンが含有
されている。The main component of the intermediate process product Q up to the lowermost cyclone 8 is, for example, SiO 2 19.0.
%, Al 2 O 3 4.3%, Fe 2 O 3 2.7%, C
It is 60.5% of aO and 1.5% of MgO, and contains sufficient quicklime. The intermediate process product Q is in the form of fine powder, and contains about 0.5% of unburned carbon.
【００１１】そして、最下段のサイクロン８からロータ
リーキルン１０へ、生石灰を含有した中間工程品Ｑが供
給されるが、最下段のサイクロン８の下部出口には分取
ダンパ２０が設けられており、分取ダンパ２０を介して
所定量の中間工程品Ｑが分取されるようになっている。
そして、分取された中間工程品Ｑは、水冷式冷却器２
１、輸送機２２、出荷タンク２４を介して、搬送車２５
により固形化燃料製造工場へ搬送される。なお、図１に
おいて、２３はエアロックフィーダであり、また、出荷
タンク２４には集塵機が装備されている。Then, the intermediate process product Q containing quicklime is supplied from the lowermost cyclone 8 to the rotary kiln 10, and a lowering outlet of the lowermost cyclone 8 is provided with a separation damper 20. A predetermined amount of the intermediate process product Q is collected via the take-off damper 20.
Then, the separated intermediate process product Q is supplied to the water-cooled cooler 2.
1. Transport vehicle 25 via transport device 22 and shipping tank 24
Is transported to the solidified fuel manufacturing plant. In FIG. 1, reference numeral 23 denotes an air lock feeder, and the shipping tank 24 is equipped with a dust collector.
【００１２】一方、固形化燃料製造工場においては、図
２に示すように、廃棄物Ｇが、廃棄物置場３１から搬送
されて、破砕機３２により適度な大きさに破砕され、更
に、分離選別機３３により、比重差を利用して、生ゴミ
等の可燃性廃棄物と金属、ガラス片等の不燃性廃棄物と
に分別され、分別された可燃性廃棄物が混合反応機３４
に投入されるようになっている。なお、生ゴミ等の可燃
性廃棄物は、約２５〜４０％の水分を含有している。ま
た、生石灰を含有したセメント中間工程品Ｑは、搬送車
２５から、受入タンク２６を介して、処理剤として混合
反応機３４に投入される。On the other hand, in the solidified fuel manufacturing plant, as shown in FIG. 2, waste G is transported from a waste storage site 31 and crushed to an appropriate size by a crusher 32, and further separated and sorted. The combustible waste is separated into combustible waste such as garbage and non-combustible waste such as metal and glass pieces by utilizing the difference in specific gravity.
It is to be thrown into. Combustible waste such as garbage contains about 25 to 40% of water. In addition, the cement intermediate process product Q containing quicklime is fed from the transport vehicle 25 to the mixing reactor 34 as a processing agent via the receiving tank 26.
【００１３】そして、混合反応機において、破砕された
可燃性廃棄物と微粉末状の中間工程品Ｑとが混合され、
中間工程品Ｑ中の生石灰分と可燃性廃棄物中の水分とが
以下のように反応し、可燃性廃棄物中の水分が、この水
和反応に消費され、又は反応熱により蒸発することによ
って、可燃性廃棄物が脱水される。また、この反応で発
生する消石灰によって、ｐＨが強アルカリ性となるた
め、可燃性廃棄物中の微生物は殺菌され、有機物の腐敗
が抑制される。 ＣａＯ＋Ｈ2 Ｏ→Ｃａ（ＯＨ）2 Then, in the mixing reactor, the crushed combustible waste and the finely powdered intermediate process product Q are mixed,
The quicklime component in the intermediate process product Q and the water in the combustible waste react as follows, and the water in the combustible waste is consumed in this hydration reaction or is evaporated by the heat of reaction. The combustible waste is dehydrated. In addition, slaked lime generated by this reaction makes the pH highly alkaline, so that microorganisms in the combustible waste are sterilized, and spoilage of organic matter is suppressed. CaO + H 2 O → Ca (OH) 2
【００１４】また、微粉末状で、少量の未燃カーボンを
含んでいる中間工程品Ｑに、可燃性廃棄物中の臭気成分
が吸着され、可燃性廃棄物が脱臭される。Further, the odor components in the combustible waste are adsorbed by the intermediate process product Q in the form of fine powder and containing a small amount of unburned carbon, and the combustible waste is deodorized.
【００１５】このようにして、破砕された可燃性廃棄物
に対して、脱水、殺菌、脱臭等の化学的処理が施される
が、処理剤としてセメント焼成系から分取した中間工程
品Ｑを使用したので、生石灰を使用する場合に比して、
可燃性廃棄物を経済的に処理することができると共に、
可燃性廃棄物と十分に混合し、適度な反応速度により好
適に処理することができる。The crushed combustible waste thus obtained is subjected to chemical treatment such as dehydration, sterilization, and deodorization. The intermediate process product Q separated from the cement firing system as a treatment agent is used. As I used it, compared to using quicklime,
Combustible waste can be economically treated,
It is sufficiently mixed with combustible waste and can be suitably treated with an appropriate reaction rate.
【００１６】そして、処理された可燃性廃棄物は、圧縮
成形機３５により所定の大きさ、形状に成形され、乾燥
機３６により熱風で乾燥されて、固形化燃料Ｆとなり、
固形化燃料置場３７に搬送される。The treated combustible waste is formed into a predetermined size and shape by a compression molding machine 35 and dried by hot air by a dryer 36 to become a solidified fuel F.
It is transported to the solidified fuel storage 37.
【００１７】なお、上述の実施の形態は、セメント焼成
系のサスペンションプレヒーターに仮焼炉が備えられて
いる場合について述べたが、仮焼炉は必ずしも備えなく
てもよい。また、上述の実施の形態は、セメント焼成系
のサスペンションプレヒーターの最下段のサイクロンか
ら中間工程品を分取する場合について述べたが、中段の
サイクロンから分取してもよい。In the above embodiment, the case where the calciner is provided in the suspension preheater of the cement firing system is described, but the calciner may not be necessarily provided. Further, in the above-described embodiment, the case where the intermediate process product is collected from the lowermost cyclone of the suspension preheater of the cement firing system is described, but the intermediate process product may be collected from the middle cyclone.
【００１８】[0018]
【発明の効果】上述のように、本発明に係る廃棄物から
の固形化燃料の製造方法は、セメント原料を加熱して得
られる生石灰を含む中間工程品を、セメント焼成系のサ
スペンションプレヒーターから分取し、破砕後成形前の
廃棄物に、処理剤として混合して処理することによっ
て、生石灰分の反応による脱水処理、生石灰分の反応で
発生する消石灰による殺菌処理、未燃カーボン及び微粉
末状による脱臭処理等を、効率的かつ経済的に行うこと
ができる。As described above, in the method for producing solidified fuel from waste according to the present invention, an intermediate process product containing quick lime obtained by heating a cement raw material is produced from a cement firing suspension preheater. Separation, crushing and pre-molding waste are mixed and treated as a treating agent, so that dehydration by the reaction of quick lime, sterilization by slaked lime generated by the reaction of quick lime, unburned carbon and fine powder Deodorizing treatment or the like depending on the condition can be performed efficiently and economically.
【図１】 本発明に係る廃棄物からの固形化燃料の製造
方法の実施の形態の一例であって、セメント工場におけ
る工程を示す概略図である。FIG. 1 is an example of an embodiment of a method for producing a solidified fuel from waste according to the present invention, and is a schematic view showing steps in a cement plant.
【図２】 本発明に係る廃棄物からの固形化燃料の製造
方法の実施の形態の一例であって、固形化燃料製造工場
における工程を示す概略図である。FIG. 2 is an example of an embodiment of a method for producing a solidified fuel from wastes according to the present invention, and is a schematic view showing steps in a solidified fuel production plant.
１ 原料貯蔵場 ２ 原料乾燥機 ３ 原料粉砕機 ４ 原料タンク ５、６、７、８ サイクロン（サスペンションプレヒー
ター） ９ 仮焼炉 １０ ロータリーキルン ２０ 分取ダンパ ２１ 冷却機 ２２ 輸送機 ２３ エアロックフィーダ ２４ 出荷タンク ２５ 搬送車 ２６ 受入タンク ３１ 廃棄物置場 ３２ 破砕機 ３３ 分離選別機 ３４ 混合反応機 ３５ 圧縮成形機 ３６ 乾燥機 ３７ 固形化燃料置場 Ｆ 固形化燃料 Ｇ 廃棄物 Ｌ セメント原料 Ｑ セメント中間工程品REFERENCE SIGNS LIST 1 raw material storage site 2 raw material dryer 3 raw material crusher 4 raw material tank 5, 6, 7, 8 cyclone (suspension preheater) 9 calciner 10 rotary kiln 20 preparatory damper 21 cooler 22 transporter 23 airlock feeder 24 shipping Tank 25 Carrier 26 Receiving tank 31 Waste storage area 32 Crusher 33 Separation and sorting machine 34 Mixing reactor 35 Compression molding machine 36 Dryer 37 Solidified fuel storage area F Solidified fuel G Waste L Cement raw material Q Cement intermediate process
Claims (1)
を混合して処理した後に成形して固形化燃料を製造する
廃棄物からの固形化燃料の製造方法において、 前記処理剤は、セメント焼成系のサスペンションプレヒ
ーターから分取され、セメント原料を加熱して得られる
生石灰を含む中間工程品であることを特徴としてなる廃
棄物からの固形化燃料の製造方法。1. A method for producing a solidified fuel from waste, which comprises mixing and treating a crushed waste with a treatment agent containing quick lime and then molding to produce a solidified fuel, wherein the treatment agent comprises cement. A method for producing a solidified fuel from waste, characterized in that it is an intermediate process product containing quicklime obtained by heating a cement raw material, which is fractionated from a firing system suspension preheater.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26409096A JPH10110176A (en) | 1996-10-04 | 1996-10-04 | Production of solid fuel from waste material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26409096A JPH10110176A (en) | 1996-10-04 | 1996-10-04 | Production of solid fuel from waste material |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH10110176A true JPH10110176A (en) | 1998-04-28 |
Family
ID=17398377
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP26409096A Withdrawn JPH10110176A (en) | 1996-10-04 | 1996-10-04 | Production of solid fuel from waste material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH10110176A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20010114025A (en) * | 2000-06-20 | 2001-12-29 | 강판수 | Method for manufacturing solid fuel from waste organic substance |
| GB2426004A (en) * | 2005-05-13 | 2006-11-15 | Design Build And Recycle Ltd | Process for treating waste |
| CN110557946A (en) * | 2018-04-04 | 2019-12-10 | 太平洋工程株式会社 | Organic sludge treatment device and treatment method |
| BE1030189B1 (en) * | 2022-01-14 | 2023-08-16 | Thyssenkrupp Ag | Plant and a method for operating a plant for the production of cement or lime |
-
1996
- 1996-10-04 JP JP26409096A patent/JPH10110176A/en not_active Withdrawn
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20010114025A (en) * | 2000-06-20 | 2001-12-29 | 강판수 | Method for manufacturing solid fuel from waste organic substance |
| GB2426004A (en) * | 2005-05-13 | 2006-11-15 | Design Build And Recycle Ltd | Process for treating waste |
| CN110557946A (en) * | 2018-04-04 | 2019-12-10 | 太平洋工程株式会社 | Organic sludge treatment device and treatment method |
| BE1030189B1 (en) * | 2022-01-14 | 2023-08-16 | Thyssenkrupp Ag | Plant and a method for operating a plant for the production of cement or lime |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A761 | Written withdrawal of application |
Effective date: 20041115 Free format text: JAPANESE INTERMEDIATE CODE: A761 |