JPS6356598A - Production of specialty fuel utilizing waste - Google Patents
Production of specialty fuel utilizing wasteInfo
- Publication number
- JPS6356598A JPS6356598A JP19950186A JP19950186A JPS6356598A JP S6356598 A JPS6356598 A JP S6356598A JP 19950186 A JP19950186 A JP 19950186A JP 19950186 A JP19950186 A JP 19950186A JP S6356598 A JPS6356598 A JP S6356598A
- Authority
- JP
- Japan
- Prior art keywords
- waste
- crushed
- chlorine
- crushing
- crusher
- 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.)
- Pending
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 27
- 239000000446 fuel Substances 0.000 title claims abstract description 11
- 238000004519 manufacturing process Methods 0.000 title claims description 4
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims abstract description 13
- 229910052801 chlorine Inorganic materials 0.000 claims abstract description 12
- 239000000460 chlorine Substances 0.000 claims abstract description 12
- 239000000463 material Substances 0.000 claims abstract description 12
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 claims abstract description 9
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 7
- 239000008188 pellet Substances 0.000 claims description 19
- 238000006386 neutralization reaction Methods 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 7
- 239000000126 substance Substances 0.000 abstract description 7
- 239000011521 glass Substances 0.000 abstract description 4
- 229910052742 iron Inorganic materials 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 3
- 230000003472 neutralizing effect Effects 0.000 abstract description 2
- 239000004576 sand Substances 0.000 abstract description 2
- 239000004449 solid propellant Substances 0.000 abstract description 2
- 238000005453 pelletization Methods 0.000 abstract 3
- 238000010298 pulverizing process Methods 0.000 abstract 2
- 238000005549 size reduction Methods 0.000 abstract 2
- 238000007906 compression Methods 0.000 abstract 1
- 230000006835 compression Effects 0.000 abstract 1
- 238000004898 kneading Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 11
- 239000002994 raw material Substances 0.000 description 9
- 238000001125 extrusion Methods 0.000 description 8
- 239000002023 wood Substances 0.000 description 4
- 239000010849 combustible waste Substances 0.000 description 2
- 239000010791 domestic waste Substances 0.000 description 2
- 239000002440 industrial waste Substances 0.000 description 2
- 238000010169 landfilling Methods 0.000 description 2
- 239000000696 magnetic material Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 1
- 241000270666 Testudines Species 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 210000004907 gland Anatomy 0.000 description 1
- -1 gravel Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000010893 paper waste Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 231100000167 toxic agent Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B15/00—Details of, or accessories for, presses; Auxiliary measures in connection with pressing
- B30B15/0005—Details of, or accessories for, presses; Auxiliary measures in connection with pressing for briquetting presses
-
- 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
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野、〕
この発明は、廃棄物を処理して燃料を製造せんとするも
のであり、特に塩素を除去してペレット化すための廃棄
物を利用した特殊燃料の製造法に関するものである、
〔従来の技術及び発明が解決しようと干る問題点〕従来
、廃棄物を処理する方法として、暁却炉によって焼却す
る方法、或は破砕した後焼却したり、埋立てられたりす
る方法その他１種々の方法が存在する。然し乍ら、之等
の廃棄物の中には金属＠−鉄屑類等を除き、多くの燃焼
可能物質が包含さ引ており、従って、この燃焼可能物質
を取出し、−定の処理を施して燃料にするためにＭ決さ
れるべき問題点が生じてくるのである。[Detailed Description of the Invention] [Industrial Application Field] This invention aims to produce fuel by treating waste, and in particular, it aims to process waste to produce fuel, and in particular, to remove chlorine and use waste to pelletize it. [Problems that conventional technology and inventions are trying to solve] Concerning the manufacturing method of special fuels. Conventionally, as a method for treating waste, there have been methods of incinerating it in an incinerator or crushing it and then incinerating it. There are various methods such as landfilling, landfilling, etc. However, these wastes contain many combustible substances other than metal scraps, etc. Therefore, these combustible substances are extracted and processed in a certain way to produce fuel. In order to do so, there are issues that need to be resolved.
この発明は、前記問題点に鑑み之を解決せんと、して提
案せられたものであり、廃棄物を一次破砕機により所定
の犬ぎさに破砕し、之を選別機によって燃焼不可能の物
質を除去し一燃等可能な物質を選別して二次破砕機に送
り込み、之を再度破砕、混線、圧ａ−縮少し、そして之
をペレットマシーンにて更に破砕、圧潰、粉砕し、而も
−このペレットマシーンにおける処理中に生じる高熱に
よりて発生子る塩素ガスをＮａ ｏＨ！％を使用した中
和装置中を通過させろととてより該塩素を除去すると共
に、該ペレットマシーンの前面よりペレット状に形成し
て取出すようにしたことを特徴とする廃棄物を利用した
特殊燃料の製造法を提供せんとするものである。This invention was proposed in order to solve the above-mentioned problems, and involves crushing waste into predetermined sizes using a primary crusher, and separating the waste into non-combustible materials using a sorter. The materials that can be combusted are removed, and the materials that can be combusted are sent to the secondary crusher, which is then crushed again, cross-wired, compressed, and further crushed, crushed, and pulverized using a pellet machine. - The chlorine gas generated by the high heat generated during processing in this pellet machine is replaced with Na oH! A special fuel made from waste, characterized in that the chlorine is removed by passing it through a neutralization device using % chlorine, and the chlorine is formed into pellets and taken out from the front of the pellet machine. The purpose of this study is to provide a method for producing .
この発明の方法によって、一般家庭用の廃棄物或は産業
廃棄物を問わず、凡そ燃焼可能である物質が大別されて
一次破砕機によって破砕され、更に一選別機によって鉄
分、砂利、硝子類が取除かれ１次の工程でブロアーによ
って非磁気性物質が選別され、之を二次破砕機によって
破砕すると同時に投入口より投入される木屑等と混練さ
れ、圧縮、縮少され１次にペレットマシーンに投入すれ
。According to the method of this invention, combustible substances, whether general household waste or industrial waste, are roughly separated and crushed by a primary crusher, and iron, gravel, and glass are further separated by a first sorter. is removed, non-magnetic substances are sorted out by a blower in the first step, and are crushed by a secondary crusher and at the same time mixed with wood chips etc. that are input from the input port, compressed and reduced, and become pellets in the first step. Throw it into the machine.
このペレットマシーンの処理胴の中を通過するとぎ、更
に細かく粉砕され、この処理胴前面よりペレット状に形
成されて取出される。このとき、当該処理胴の中を約２
００″Ｃ位に温度を上昇せしめ、この温度上昇によって
被処理物より塩素が分離して塩素ｒスが発生する。そこ
で、前記処理胴の前方部上面を解放し、この開放部より
ダクト等で前記被処理物中の前記塩素ガスを取出し、そ
の途中でＮａｏＨ等のシャワー中を通過させて前記塩素
を中和させ、被処理物の中より塩素を除去し、全く無害
なペレット状の燃料を生産できるようになったのである
。As it passes through the processing barrel of this pellet machine, it is further finely ground and is formed into pellets and taken out from the front surface of this processing barrel. At this time, about 2
The temperature is raised to about 00"C, and due to this temperature rise, chlorine is separated from the object to be treated and chlorine gas is generated.Then, the upper surface of the front part of the processing cylinder is opened, and a duct etc. is used from this open part. The chlorine gas in the object to be treated is taken out, passed through a shower of NaoH or the like during the process to neutralize the chlorine, remove chlorine from the object to be treated, and produce completely harmless pellet-shaped fuel. It became possible to produce it.
以下、この発明の一実施例を別紙添附図面に従って詳述
する。本発明の原材料は廃棄物である。Hereinafter, one embodiment of the present invention will be described in detail with reference to the accompanying drawings. The raw material of the present invention is waste.
この廃棄物は産業廃棄物、一般家庭の廃棄物等があるが
、之等の廃棄物の中には燃焼不可能な物質も多く含まれ
ている。例えば金４類−鉄屑、廃油。This waste includes industrial waste, general household waste, etc., and these wastes include many substances that cannot be combusted. For example, metal type 4 - iron scrap, waste oil.
廃酸−廃アルカリ、多くの建築材、硝子、砂利類等であ
るが、之等は予め大別して除去し、燃焼可能な廃棄物を
選別しておく。即ち、燃焼可能な廃棄物は、廃プラスチ
ツク類、木屑１紙屑−繊維屑。Waste acids, waste alkalis, many building materials, glass, gravel, etc. are roughly separated and removed in advance, and combustible wastes are sorted out. That is, the combustible wastes include waste plastics, wood chips, paper waste, and fiber waste.
動植物残渣等℃ある。そして、予め大別された之等の燃
焼可能な物質は、投入コンベア（１）を経て一次破砕機
（２）に投入さ七る。この−次破砕機（２）によって細
かく破砕された廃棄物は、肖該−次破砕機（２）より取
出さ引でコンベアＣ３１ｒ３）を経て、マグネットロー
ラー（４）によって鉄分（Ｆ＋＞ｆ５）・・・が除去さ
れる。There are animal and plant residues, etc. The combustible substances, which have been roughly classified in advance, are then fed into the primary crusher (2) via the feeding conveyor (1). The waste finely crushed by this secondary crusher (2) is taken out from the secondary crusher (2) and passed through a conveyor C31r3) by a magnetic roller (4) to remove iron (F+>f5). ... is removed.
次に、トロンメル（６）の中を通過させ、このトロンメ
ル（６）の回転によって当該メツシュより砂、硝子屑（
７１（７１・・・等が除去される。次に、ブロアー（８
）によって比較的重量物である磁気性物質（９）（９）
・・・を除去し、非磁気性物質［株］（＋１・・・を選
別し、之をコンベアーを経て二次破砕機（１３に投入す
る。この二次破砕機ａｚに於ては木屑が同時に投入され
る。而して、この二次破砕機（１３と次の工程のペレッ
トマシーン０３とは、その＋７３部構造が殆ど一致して
いる構成が多い。唯、相違する点は二次破砕機ｆｉ３に
於ては。Next, the sand and glass chips (
71 (71...etc.) are removed. Next, the blower (8
) is a relatively heavy magnetic material (9) (9)
... is removed, the non-magnetic material [stock] (+1... The secondary crusher (13) and the pellet machine 03 used in the next process often have the same +73 structure.The only difference is that the secondary crusher (13) In machine fi3.
ペレット生成の為の装置及び被処理中の塩素ガスを発生
させないようにし、従ってこの塩素ガスの中和装置を有
しない点が相違するのである。即ち。The difference is that the method does not have a device for producing pellets or a device for neutralizing the chlorine gas, so as not to generate chlorine gas during treatment. That is.
この二次破砕機０２の中に木屑と同時に投入された被処
理物は、この二次破砕機ａ２によって更に細かく破砕さ
れ、前記木屑と混練され圧縮、縮少され乍ら該二次破砕
機αりの前方より取出されるのである。斯くして一取出
さ引た被処理物Ｇ′ｉ最後の工程のペレットマシーン０
りに投入さ引、て処理さレル。The material to be treated, which is fed into the secondary crusher 02 at the same time as the wood chips, is further crushed by the secondary crusher a2, kneaded with the wood chips, compressed and reduced, and then processed by the secondary crusher α2. It is taken out from the front of the car. In this way, the pellet machine 0 of the last process of the processed object G′i is taken out.
It is then put into the tank and processed.
ソコテ、このペレットマシーン０騰を第２図に従って詳
述する。The details of this pellet machine will be explained according to Fig. 2.
０４１は円筒状に形成せらｈた処理胴であり、この内面
にはその殆ど全長にわたってスクリュ状の回転刃（１５
１が回転自在に枢支せら刺ている。そして、この回転刃
０Ｓのねじ刃（１５ａ）間の１１−１ｊは、送り側末端
に近づくに従って短かくなるように形成されている。又
、この回転刃（１５１の軸（′ｌＦ＋１は、前端部を処
理胴ａ４の送り側前端部に取付けた端板１１７）ｋ軸支
しており、更に、その他端部は、処理胴α荀の出口側に
取付けられた押出板１Ｉ８１の中心部に嵌蕾したベアリ
ング（１９ｂ）に軸支しである。更に一前記押出板０８
１には多数の開穿孔（１８ａ）（１８ａ）・・・が設げ
ら引ている。041 is a processing cylinder formed into a cylindrical shape, and a screw-shaped rotary blade (15
1 is rotatably supported. The length 11-1j between the threaded blades (15a) of the rotary blade 0S is formed to become shorter as it approaches the feed end. In addition, this rotary blade (151) is supported by the axis ('lF+1 is the end plate 117 whose front end is attached to the feeding side front end of the processing cylinder a4), and the other end is supported by the processing cylinder α It is pivotally supported by a bearing (19b) fitted into the center of the extrusion plate 1I81 attached to the outlet side of the extrusion plate 08.
1 has a large number of open holes (18a) (18a)...
又、この押出板−は中央部を開口（１９ａ）Ｌ、たグラ
ンドナツトα９にて前記処理胴（１荀の出口に取付けら
れている。又、前記処理胴囲の送り側出口に於て。This extrusion plate has an opening (19a) L at the center and is attached to the outlet of the processing cylinder (1) with a gland nut α9.Also, at the outlet on the feed side of the processing cylinder.
処理胴α荀によって生成されろ製品を一定の長さに切断
するために回転切断刃（２Ｇを前記回転刃α９の軸鰻に
固着しであるが、前記製品をペースト状に生成干る場合
は、この回転切断刃■を使用しないこともある。又、該
処理胴ａ４の始端部の上方は開放され、原料投入口３１
）が形成さ幻ており、原料は樋りより該原料投入口２１
１Ｆに投入せられるのである。A rotary cutting blade (2G) is fixed to the shaft of the rotary blade α9 to cut the product produced by the processing body α9 into a certain length, but when the product is produced into a paste and dried , this rotary cutting blade (2) may not be used.Also, the upper part of the starting end of the processing cylinder a4 is open, and the raw material input port 31
) is formed, and the raw material is transferred from the gutter to the raw material input port 21.
It is thrown into the 1st floor.
尚−前記処理胴（１４）の内側面の所々に刃体（図示せ
ず）を設けてもよい。前記回転刃０５１の軸＋ＩＦ１１
の一端部は前述せるように、端板鼎によって枢支される
と共に七〇余端部は軸接手のを介してモーターの如き原
動機Ｃ２４１に連結している。原料が前記投入口Ｃυに
投入せられたとき、処理胴０４内の回転刃ｑ５１の回転
によって当該原料は切断され、出口側に行くに従ってね
じ刃（１５ａ）間のリードが短かくなっているので、前
記切断された原料は更に短かく切断さｆｌ−且つ、破砕
、圧潰−揉捻される。そして、該原料は処理胴（１４Ｊ
内の熱処理を経てペースト状となり、押出板（１８１の
開穿孔（１８ａＸ１８ａ）・・・よりしぼり出されるの
である。このとき−この押出板（１８の内側面に接する
ように取付けである回転切断刃■によって一定の長さに
切断され、ペレット状に形成されて開口（１〜）より放
出さ刺るのである。このよ５に原料が処理胴へ・０内に
於て処理される際−その処理中に当該処理胴ａ４の内部
は摩擦熱が上昇し１％に肉厚の押出板側にあってし１そ
の出口附近の温度が２００”Ｃ程度に昇温するので、高
圧のもとで煮ら幻たように碓めて軟かいペースト状とな
り、而も、この昇温によって材料内の塩素が塩素ガスと
なって処理胴０４）の前方上方部の開口部（１４ａ）よ
り一ヒのダクト□□□を介して一途中に設げら幻たＮａ
ｏＨのシャワー（Ａ１を有する中和装置【、ざ９内の前
記のシャワー（Ａｔを通過者るとぎ、前記塩素ガスは中
和され「塩」となる。従って、処理胴Ｉ内を通過して処
理されつＮある材料より有害物質の塩素は完全に除去さ
幻る。斯くして、処理胴α４を通過するとき全体が一体
的にペースト状となり一押出板Ｑ８）の開穿孔（１亀）
（１８ａ）・・・よりしぼり出されるのである。このと
き。Incidentally, blade bodies (not shown) may be provided at various locations on the inner surface of the processing cylinder (14). Axis of the rotary blade 051 + IF11
As mentioned above, one end is pivotally supported by the end plate, and the 70-plus end is connected to a prime mover C241 such as a motor via a shaft joint. When the raw material is put into the input port Cυ, the raw material is cut by the rotation of the rotary blade q51 in the processing cylinder 04, and the lead between the screw blades (15a) becomes shorter as it goes toward the outlet side. Then, the cut raw material is further cut into short pieces, and then crushed, crushed and rolled. Then, the raw material is processed into a processing cylinder (14J
It becomes a paste after undergoing heat treatment inside, and is squeezed out through the open holes (18a x 18a) of the extrusion plate (181). The material is cut into a certain length by 5, formed into pellets, and released from the openings (1 to 1).In this way, when the raw material is processed in the processing cylinder and inside the During processing, frictional heat increases inside the processing cylinder A4, which is located on the side of the extrusion plate, which is 1% thicker, and the temperature near the outlet rises to about 200"C, so it is heated under high pressure. It melts into a soft paste as if boiling, and due to this temperature rise, the chlorine in the material turns into chlorine gas, which is then poured into the material through the opening (14a) in the upper front part of the processing barrel 04). Illustrated Na was installed halfway through the duct □□□
The chlorine gas is neutralized and becomes "salt". It appears that the toxic substance chlorine is completely removed from the treated material.In this way, when it passes through the processing cylinder α4, the whole becomes paste-like, and the perforation (1 turtle) of the extrusion plate Q8) is made.
(18a)... It is squeezed out more. At this time.
前記の通り押出板（１カの内（ｉ４１１１ｆｆｉに接す
るよ５に取付けである回転切断刃■によって一定の長さ
に切断され、ペレット状に形成されて抽出されるのであ
る。As mentioned above, it is cut into a certain length by the rotating cutting blade (2) attached to the extrusion plate (1) (5), which is in contact with the extrusion plate (1), and is formed into pellets and extracted.
このようにして生成したペレット状の生成物は、惨焼可
能な物質によって構成さ幻、而も圧縮、縮少した形状に
固形化さ引ているので、カロリーも充分な燃料となり一
且つ、塩素を除去しているので全く安心して使用するの
である。The pellet-like product produced in this way is made up of materials that can be burnt, and since it is compressed and solidified into a reduced shape, it has sufficient calories as a fuel, and also contains chlorine. Since it has been removed, it can be used with complete peace of mind.
この発明は叙述せろ実施例に於て詳述せる如く。 The present invention will be described in detail in the embodiments.
従来、焼却炉等に於て焼却するか、ｔｃは埋立等に利用
していた廃棄物を利用し、−次破砕処理から選別工程′
？：経て二欠破伜処理をし、最終工程のペレットマシー
ンにてペレット状の燃料を生成すると共に−このペレッ
ト状のｅ＠は一塩素の有毒分を除去しているので全く公
害の虞がなく、而も。Traditionally, waste is incinerated in an incinerator or used in landfills, etc., and the next step is crushing and sorting.
? : After that, it undergoes two-breakage treatment, and in the final process, a pellet machine produces pellet-shaped fuel. Since the toxic content of monochlorine has been removed from this pellet-shaped e@, there is no risk of pollution. , and also.
カロリーも充分な固形燃料を得ることができる等、正に
諸種の工業的著大なる価値ある発明である。It is truly an invention of great industrial value, such as being able to obtain solid fuel with sufficient calories.
図は本発明の一実施例を示し一第１図は全体の工程を示
すフローチャートであり、用２図はペレットマシーンの
Ｐａ ｌ￥ｆｒ ＜’Ａ１１面図である。
符号説明The drawings show an embodiment of the present invention. Fig. 1 is a flowchart showing the overall process, and Fig. 2 is a side view of the pellet machine. Code explanation
Claims (1)
選別機によって燃焼不可能の物質を除去し、燃焼可能な
物質を選別して二次破砕機に送り込み、之を再度破砕、
混練、圧縮、縮少し、そして之をペレットマシーンにて
更に破砕、圧潰、粉砕し、而も、このペレットマシーン
における処理中に生じる高熱によって発生する塩素ガス
をＮａＯＨ等を使用した中和装置中を通過させることに
より該塩素を除去すると共に、該ペレットマシーンの前
面よりペレット状に形成して取出すようにしたことを特
徴とする廃棄物を利用した特殊燃料の製造法。The waste is crushed into a predetermined size by a primary crusher, non-combustible materials are removed by a sorter, combustible materials are sorted and sent to a secondary crusher, and the waste is crushed again.
The mixture is kneaded, compressed, reduced, and further crushed, crushed, and pulverized in a pellet machine, and the chlorine gas generated due to the high heat generated during processing in the pellet machine is passed through a neutralization device using NaOH or the like. A method for producing a special fuel using waste, characterized in that the chlorine is removed by passing through the waste, and the waste is formed into pellets and taken out from the front of the pellet machine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19950186A JPS6356598A (en) | 1986-08-27 | 1986-08-27 | Production of specialty fuel utilizing waste |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19950186A JPS6356598A (en) | 1986-08-27 | 1986-08-27 | Production of specialty fuel utilizing waste |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6356598A true JPS6356598A (en) | 1988-03-11 |
Family
ID=16408874
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19950186A Pending JPS6356598A (en) | 1986-08-27 | 1986-08-27 | Production of specialty fuel utilizing waste |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6356598A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1998043805A1 (en) * | 1997-03-27 | 1998-10-08 | Fibrecycle Pty. Ltd. | Improvements in a process and apparatus for the production of paper products |
| AT407131B (en) * | 1999-04-12 | 2000-12-27 | Walter Stoiber | Process for obtaining wood chips or pellets from green cuttings |
| JP2002191587A (en) * | 2000-12-25 | 2002-07-09 | Canon Inc | Radiography equipment |
| JP2013501826A (en) * | 2009-08-13 | 2013-01-17 | 斌 牛 | Process and equipment for continuous dechlorination |
| CN103131500A (en) * | 2011-11-25 | 2013-06-05 | 仇峰 | Organic carbon and manufacturing method thereof |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59157187A (en) * | 1983-02-25 | 1984-09-06 | Toshiro Watanabe | Process for utilizing waste mixture of miscellaneous materials as solid fuel |
-
1986
- 1986-08-27 JP JP19950186A patent/JPS6356598A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59157187A (en) * | 1983-02-25 | 1984-09-06 | Toshiro Watanabe | Process for utilizing waste mixture of miscellaneous materials as solid fuel |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1998043805A1 (en) * | 1997-03-27 | 1998-10-08 | Fibrecycle Pty. Ltd. | Improvements in a process and apparatus for the production of paper products |
| AT407131B (en) * | 1999-04-12 | 2000-12-27 | Walter Stoiber | Process for obtaining wood chips or pellets from green cuttings |
| JP2002191587A (en) * | 2000-12-25 | 2002-07-09 | Canon Inc | Radiography equipment |
| JP2013501826A (en) * | 2009-08-13 | 2013-01-17 | 斌 牛 | Process and equipment for continuous dechlorination |
| CN103131500A (en) * | 2011-11-25 | 2013-06-05 | 仇峰 | Organic carbon and manufacturing method thereof |
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