JPS5956496A - Preparation of solid fuel from wastes - Google Patents

Preparation of solid fuel from wastes

Info

Publication number
JPS5956496A
JPS5956496A JP16812882A JP16812882A JPS5956496A JP S5956496 A JPS5956496 A JP S5956496A JP 16812882 A JP16812882 A JP 16812882A JP 16812882 A JP16812882 A JP 16812882A JP S5956496 A JPS5956496 A JP S5956496A
Authority
JP
Japan
Prior art keywords
hopper
waste
solid fuel
wastes
combustible
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
Application number
JP16812882A
Other languages
Japanese (ja)
Inventor
Shinichi Asada
浅田 信市
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP16812882A priority Critical patent/JPS5956496A/en
Publication of JPS5956496A publication Critical patent/JPS5956496A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

PURPOSE:To dispose of industrial wastes and urban refuses effectively and prepare solid fuel with a high calorific value, by picking up combustible wastes and blending them in proper amounts for solidification. CONSTITUTION:Industrial wastes and urban refuses are classified in a selector A. Combustible plastic material picked up from combustible wastes is fed into a hopper 11 in proper amounts through a hopper 1, a crusher 2, a burner and blower 3, a drier 4, a hopper 5, a hopper 7 and a mixer 9. Proper amounts of heat-fusible rubbers, heat-infusible rubbers <e.g. used tyre>, combustible woody substances and city refuses are fed into the hopper 11 through the same channel. The mixture is burned in a rotary kiln 13, passed through a forming machine 14 and a roller 15 and is cut in lengths in a cutter 16 to produce a solid fuel.

Description

【発明の詳細な説明】 この発明は、産業廃棄物、都市ゴミ等現在地方自治体な
どに於て、焼却又は埋立地に埋没するなど、何等経済性
の伴なわない処理が行なわれている可燃性廃棄物を主原
料となし、これら有機物を分離選別の前処理を行ない、
適応した比率に配合固型化し、燃料として再生する、廃
棄物固型燃料の製造法に関するものである。
[Detailed Description of the Invention] This invention deals with the treatment of combustible waste, such as industrial waste and municipal waste, which are currently being disposed of by local governments without any economic efficiency, such as incineration or burying in landfills. Using waste as the main raw material, these organic substances are pretreated for separation and sorting,
This relates to a method for producing waste solid fuel, which is blended in an appropriate ratio, solidified, and recycled as fuel.

従来の固型燃料又は、最近開発中の固型燃料について、
併せて自治体運営の隘路となっている、ゴミ処理の問題
については、次に掲げる様な欠点と立ち遅れが指摘され
る。
Regarding conventional solid fuels or solid fuels currently under development,
At the same time, the following shortcomings and delays have been pointed out regarding the problem of garbage disposal, which has become a bottleneck for local government management.

現在各自溶体とも廃棄物の資源化については、強い要望
を示し、特に廃プラスチックの処理については、幾多の
企業に於ても、あらゆる実証試験が試みられてはいるが
、いまだ経済的に成立つ処理方法の見出せないのが現状
である。
Currently, there is a strong demand for the recycling of waste from all types of self-dissolved materials, and although many companies have attempted various demonstration tests, especially regarding the treatment of waste plastics, it is still not economically viable. At present, no treatment method has been found.

この発明は、かかる問題の解消を図る強い要望を満たす
ために開発したものである。
This invention was developed to meet the strong demand for solving this problem.

周知の如く、従来のオガライトは、オガクズを高圧成型
したものに過ぎず、湿気に弱いため着火が容易でなく、
雨水に濡れた場合型くずれして使用不能となり、比較的
発熱量も低く、又原料となるオガクズが不足して入手困
難等の欠点がある。
As is well known, conventional sawlight is nothing more than high-pressure molded sawdust, and it is difficult to ignite because it is sensitive to moisture.
If it gets wet with rainwater, it loses its shape and becomes unusable, has a relatively low calorific value, and has disadvantages such as the lack of raw material sawdust, which is difficult to obtain.

現在、高知系工業試験場で開発されている、パークライ
トは、杉、桧の樹皮に廃ポリを混入し、固型燃料として
開発されたものである。
Parklite, which is currently being developed at the Kochi Industrial Research Institute, is a solid fuel made by mixing waste polyethylene into the bark of cedar and cypress trees.

又、愛媛県青果連に於ても、ミカンの搾りかすを固型燃
料として開発されており、現在燃焼実験が行なわれてい
る。
Additionally, the Ehime Prefecture Fruit and Vegetables Association has developed mandarin orange pomace as a solid fuel, and combustion experiments are currently underway.

次に、北海道旭川型旭川総合鉄工団地に於ては、竹内勝
義社長が樹皮を原料として木質中に含まれたリグニンの
働きによって固める固型燃料を開発されるなど、何れも
優秀な燃料であると思われ賞賛すべきであるが、これら
は、何れも林業及び、ミカンの生産地であるが故に、開
発されたものであり、他の消費糸、消費都市に於ては、
オガライトの原料となるオガクズの入手さえ困難な現状
である。
Next, at the Asahikawa General Iron Works Complex in Asahikawa, Hokkaido, president Katsuyoshi Takeuchi developed a solid fuel that uses tree bark as a raw material and solidifies it with the action of lignin contained in wood, all of which are excellent fuels. This should be praised, but these were developed because they are forestry and mandarin orange production areas, and in other consumption yarns and consumption cities,
At present, it is difficult to even obtain sawdust, which is the raw material for Ogarite.

然るに、特定の原料を主体とする固型燃料は、必然的に
生産地域の制約があり、従って、生産量にも限界がある
など、巾広い資源の再生利用とか廃棄物の処理対策など
としては、当然不可能であるなどの欠点に鑑み。
However, solid fuels that are mainly made from specific raw materials are inevitably limited by the region in which they can be produced, and therefore there are limits to the amount of production, making them difficult to use as a means of wide-ranging resource recycling or waste treatment. , in view of the drawbacks such as the fact that it is of course impossible.

この発明は、従来のものがもつ以上の様な欠点と問題を
除去し、廃棄物の資源化を求める強い要望を満たすため
に、固型燃料として有効に再生利用し、かつ廉価に提供
する事が目的である。
This invention eliminates the drawbacks and problems of conventional products, and satisfies the strong demand for recycling waste by effectively recycling it as a solid fuel and providing it at a low price. is the purpose.

以下その詳細を系統図面にもとすいて説明すると、収集
された廃棄物をプラスチック系、古タイヤ類、ゴム類、
木質系物質、都市ゴミ等に発熱量と燃焼度合を考慮して
、第1図に示す、選別機(4)に於て、分離選別の前処
理を行なう。
The details will be explained below based on the system diagram. The collected waste will be recycled into plastics, old tires, rubber, etc.
Taking into consideration the calorific value and degree of combustion of wood-based materials, municipal waste, etc., pretreatment for separation and sorting is performed in the sorter (4) shown in FIG. 1.

前処理の行なわれた原料は、次の様な工程に順じて製造
を行ない固型燃料として完成する。
The pretreated raw material is manufactured into a solid fuel according to the following steps.

第1図に示す、ホッパー(1)に投入された、プラスチ
ック系の原料は、破砕機(2)に於て5mm乃至10m
m程度に破砕されて、乾燥機(4)に送られる、ここで
は、バーナーと送風機(8)より吹込む熱風によって乾
燥すると同時に異物の除去作業も行ない、これをホッパ
ー(5)に貯留する。
As shown in Fig. 1, the plastic raw materials put into the hopper (1) are crushed into 5mm to 10m by the crusher (2).
It is crushed into pieces of about 1.5 m and sent to a dryer (4), where it is dried by hot air blown from a burner and a blower (8) and at the same time removes foreign substances, and is stored in a hopper (5).

ホッパー(5)(5A)(5B)(50)(5E)の下
端部には総てに、第2図に示す、スクリューフィーダー
(6E)と同じ、スクリューフィーダー(6)(6A)
 (6B) (60)が装着されている故、第1図に示
す、ホッパー(5)に貯留された原料は、スクリューフ
ィーダー(6)の作動によって、配合比率の適量をホッ
パー(7)に送る。
The lower ends of the hoppers (5) (5A) (5B) (50) (5E) are all equipped with screw feeders (6) (6A), which are the same as the screw feeders (6E) shown in Figure 2.
(6B) Since (60) is installed, the raw material stored in the hopper (5) shown in Fig. 1 is sent to the hopper (7) at an appropriate mixing ratio by the operation of the screw feeder (6). .

第1図に示す、ホッパー(IA)に投入された加熱溶解
の可能なゴム類は、破砕機(2人)に於て、5mm乃至
IQrom程度に破砕されて、乾燥機(4A)に送られ
る、ここでは、バーナーと送風機(8A)より吹込む熱
風によって乾燥すると同時に異物の除去作業も行ない乍
らホッパー(5A)に貯留する。
Rubber that can be heated and melted is put into the hopper (IA) shown in Figure 1, and is crushed in a crusher (2 people) into pieces of about 5mm to IQrom, and then sent to the dryer (4A). Here, the material is dried by hot air blown from a burner and a blower (8A), and is stored in a hopper (5A) while simultaneously removing foreign substances.

ホッパ−(5A)に貯留された原料は、スクリューフィ
ーダー(6A)の作動によって、配合比率の適量がホッ
パー(7)に送られる。
The raw materials stored in the hopper (5A) are sent to the hopper (7) at an appropriate mixing ratio by the operation of the screw feeder (6A).

第1図に示す、ホッパー(IB)に投入された、加熱溶
解の不可能なる古タイヤ類に於ては、粉砕機(2B)で
粉砕を行ない、乾燥機(4B)に送られる、ここでもバ
ーナーと送風機(8B)より吹込む熱風によって乾燥し
乍ら異物の除去作業も同時に行ない、ホッパー(5B)
に貯留する。
As shown in Figure 1, old tires that cannot be heated and melted are placed in the hopper (IB) and are crushed in the crusher (2B) and sent to the dryer (4B). While drying with hot air blown from the burner and blower (8B), foreign matter is also removed at the same time, and the hopper (5B)
to be stored.

ホッパー(5B)に貯留された原料は、スクリューフィ
ーダー(6B)の作動によって、配合比率の適量がホッ
パー(7)に送られる。
The raw materials stored in the hopper (5B) are sent to the hopper (7) at an appropriate mixing ratio by the operation of the screw feeder (6B).

第1図に示す、ホッパー(IC)に投入された木質系原
料に於ては、粉砕機(2C)で粉砕を行ない、乾燥機(
4C)に送られる、ここでもバーナーと送風機(8C)
より吹込む熱風によって乾燥し乍ら異物の除去作業も同
時に行ない、ホッパー(5C)に貯留する。
As shown in Fig. 1, the wood-based raw materials put into the hopper (IC) are pulverized by the pulverizer (2C) and then pulverized by the dryer (2C).
4C), here also the burner and blower (8C)
While drying with hot air blowing in, foreign matter is removed at the same time and stored in a hopper (5C).

ホッパ−(50)に貯留された原料は、スクリューフィ
ーダー(6C)の作動によって、配合比率の適量がホッ
パー(7)#に送られる。
The raw materials stored in the hopper (50) are sent to the hopper (7) # in an appropriate amount by the operation of the screw feeder (6C).

第1図に示す、ホッパー(IE)に投入された、都市ゴ
ミ類に於ては、粉砕機(2E)で粉砕を行ない、乾燥機
(4E)に送られ、バーナーと送風機(8E)より吹込
む熱風によって乾燥し乍ら異物を除去する作業も同時に
行い、ホッパー(5E)に貯留する。
As shown in Figure 1, the municipal waste put into the hopper (IE) is crushed by the crusher (2E), sent to the dryer (4E), and blown by the burner and blower (8E). While drying with hot air, foreign matter is removed at the same time and stored in the hopper (5E).

ホッパー(5E)に貯留された原料は、スクリューフィ
ーダー(6E)の作動によって、配合比率の適量がホッ
パー(7yに送られる。
The raw materials stored in the hopper (5E) are sent to the hopper (7y) at an appropriate mixing ratio by the operation of the screw feeder (6E).

第1図に示す、ポツパー(7)に於ては、ホッパー(5
)(5A) (5B ”)より送られる比率の異なる原
料を、スクリューコンベヤー(8)の適確な作動によっ
て、攪拌機(9)に送られる。
In the hopper (7) shown in Figure 1, the hopper (5
) (5A) (5B '') are sent to the agitator (9) by proper operation of the screw conveyor (8).

第1図に示す、ホッパー(7yに於ては、ホッパー(5
0)(5E)より送られる比率の異なる原料を、スクリ
ューコンベヤー(8)′の適確な作動によって、攪拌機
(9)に送られる。
In the hopper (7y) shown in Figure 1, the hopper (5y)
0) (5E) are sent to the agitator (9) by proper operation of the screw conveyor (8)'.

第1図に示す、攪拌機(9)に於ては、ホッパー(7)
及び(7)′の双方より同時に送り込まれる、異なる原
料を均等に攪拌を行ない、本機下端部に装着された、第
1図、第2図に示す、スクリューコンベヤー (10)
の作動によって、配合された原料がホッパー (11)
に貯留される。
In the agitator (9) shown in Figure 1, the hopper (7)
The screw conveyor (10) shown in Figures 1 and 2 is attached to the lower end of the machine to evenly stir the different raw materials that are fed simultaneously from both the and (7)'.
By the operation of the hopper, the blended raw materials are transferred to the hopper (11)
is stored in

第2図に示す、ホッパー(11)に貯留された原料はス
クリューフィーダー(12)の作動によって、ロータリ
ーキルン(18)の要求する量を常時送込む。
The raw material stored in the hopper (11) shown in FIG. 2 is constantly fed into the rotary kiln (18) in the amount required by the operation of the screw feeder (12).

ロータリーキルン(18)に於ては、ガスボンベ(17
)より、ガスパイプ(18)を通じて、ガスバーナー(
19)より発する外熱によって、ロータリーキルン(1
3)全体が加熱されるので、原料が攪拌され乍らロータ
リーキルン(1B)を通過する過程に於て、加熱溶解の
可能なる物質の溶解を行ない、成型機(14)の要求す
る量を送り込むのである。
In the rotary kiln (18), gas cylinders (17)
) from the gas pipe (18) to the gas burner (
19) The rotary kiln (1
3) Since the whole is heated, the raw materials are stirred and in the process of passing through the rotary kiln (1B), substances that can be heated and melted are melted, and the amount required by the molding machine (14) is fed. be.

第1図第2図に示す、成型機(14)に於ては、ロータ
リーキルン(18)より送られた原料を高圧成型して棒
状となって連続的に押出され、ローラー(15)上を流
れて、切断機(16)に於て任意の長さに切断され完成
品(20)に於て、製品として完成する。
In the molding machine (14) shown in Fig. 1 and Fig. 2, the raw material sent from the rotary kiln (18) is molded under high pressure and continuously extruded into a rod shape, which flows over rollers (15). Then, it is cut into a desired length by a cutting machine (16) to produce a finished product (20).

此の説明では棒状についてのみ説明したが、この外要求
に応じて熱量及び型状などは、需要及び燃焼器具などに
適応する成型が可能である。
In this explanation, only the rod shape has been described, but the heat amount and shape can be molded to suit the demand and combustion appliance according to external requirements.

次に製造過程に於て留意すべき点など参考として附記す
ると、加熱温度及び溶解所要時間は、常時200℃乃至
280℃程度に加熱すれば、約70秒乃至90秒程度で
溶解可能であるが、ロータリーキルン(18)の構造及
び容量によっては、必然的に相違の生ずる事は避は難い
ことである。
Next, I would like to add some points to keep in mind during the manufacturing process for reference: The heating temperature and the time required for melting are: If you constantly heat the product to about 200°C to 280°C, it can be melted in about 70 to 90 seconds. It is inevitable that differences will inevitably occur depending on the structure and capacity of the rotary kiln (18).

プラスチック系物質は熱伝導率が小さいため、局部加熱
を避け、均等に攪拌し乍ら加熱する必要(7) があり、特に過熱による引火の恐れがあるので、加熱温
度の管理には十分注意を要する。
Plastic materials have low thermal conductivity, so it is necessary to avoid local heating and to heat while stirring evenly (7).There is a risk of ignition due to overheating, so please be careful in controlling the heating temperature. It takes.

配合比率の一例を次に説明する。An example of the blending ratio will be explained below.

都市ゴミ類40% 木質系10% 古タイヤ、ゴム類8
0% プラスチック系20% 但し、プラスチック系物質の配合比率は最高25%まで
とする。
Municipal garbage 40% Wood-based 10% Old tires and rubber 8
0% Plastic 20% However, the blending ratio of plastic materials shall be up to 25%.

以下燃焼実験の実施例について説明すると上水道の水を
使用して、一般家庭用風呂の例で見ると、夏季であれば
1000gの個体を一個燃焼する、ことによって、入湯
可能な温度にまで達し、冬季にても1500gの個体を
一個燃焼することによって、入湯可能な温度にまで達す
る事が実験の結果判明した。
An example of a combustion experiment will be explained below. Using water from the tap water, and looking at the example of a general household bath, in the summer, one 1000g solid is burned, thereby reaching a temperature that can be used for bathing. As a result of experiments, it was found that even in winter, by burning one 1500g piece, the temperature can be reached to the point where you can bathe in hot water.

燃焼時間については、1000gの個体−個で約40分
間程度の燃焼持続が確認された。
As for the combustion time, it was confirmed that the combustion continued for about 40 minutes for 1000 g of individual pieces.

以上の様な実験結果が確認されている。The above experimental results have been confirmed.

実験の例については、地理的温度差、燃焼器具の構造等
によって生ずる相違は止むを得ない。
Regarding experimental examples, differences caused by geographical temperature differences, the structure of combustion appliances, etc. are unavoidable.

当該固型燃料は、加熱溶解した物質が接着剤と(8) なるので、他の固型燃料の如く高圧成型の必要がなく、
従ってコスト軽減は明白である。
Since the solid fuel is made of heated and melted material that becomes an adhesive (8), there is no need for high-pressure molding like other solid fuels.
The cost savings are therefore obvious.

発熱量についても、オガライトの4ooo1ccaiに
比較して、例に示した配合率で計算した場合6050k
calであり、オガライトの約1.5倍と言う高カロリ
ーである。
The calorific value is also 6050k when calculated using the blending ratio shown in the example, compared to Ogalite's 4oooo1ccai.
cal, which is approximately 1.5 times higher in calories than Ogalite.

燃焼時には酸素量の要求が大であり、必要とする酸素供
給が十分であれば、完全燃焼が行なわれて残さ物がなく
、有毒ガスも発生せず、悪臭や黒煙も発生しないので、
家庭用、施設園芸用、工業用、各種事業所用など総てに
最適である。
During combustion, a large amount of oxygen is required, and if the required oxygen supply is sufficient, complete combustion will occur with no residue, no toxic gases, and no foul odor or black smoke.
It is ideal for home use, greenhouse horticulture, industrial use, and various business uses.

普通プラスチック系物質や古タイヤ類、ゴム類などを燃
焼する際には、非常な悪臭と黒煙、有毒ガスなどの発生
する事は周知の通りであるが、これに他の可燃物を適当
な比率に配合して燃焼することによって、勿論これらの
ものは一切発生しないのが、この燃料の特徴である。
It is well known that when plastic materials, old tires, rubber, etc. are burned, extremely foul odors, black smoke, and toxic gases are generated. A feature of this fuel is that, by blending it in the right proportions and burning it, none of these things are generated.

加熱溶解する物質の溶液が被膜を作り、他の物質に被着
するので湿気に強く、雨水に濡れても型くずれせず、濡
れた状態で容易に火がつく等は、燃料として最大の条件
を兼ね備えたものである。
A solution of a substance that dissolves when heated forms a film that adheres to other substances, making it resistant to moisture, retaining its shape even when wet with rainwater, and easily catching fire when wet. It has both.

原料の総てが廃棄物であるから、生産原価の軽減に伴な
い、廉価に提供する事は勿論、以上述べた如く、あらゆ
る面に於て、燃料としての効果が大である事は贅言を要
さない。
Since all of the raw materials are waste, it can be provided at a low price as production costs are reduced, and as mentioned above, it is no exaggeration to say that it is highly effective as a fuel in all aspects. Not needed.

この発明は、以上説明した如く、限りある資源をより効
果的に利用する事が、政府としても目下最大の急務であ
り、廃棄物を燃料とし、かつ有効的に活用する事が最大
の目的である。
As explained above, the most urgent task for the government is to use limited resources more effectively, and the most important purpose of this invention is to use waste as fuel and utilize it effectively. be.

毎年増加を続け、自治体運営に支障となっている、廃棄
物公害を軽減し、各自治体等の処理費をも軽減し、併せ
て資源をより効果的に利用する見地から、代替エネルギ
ーとして活用する事によって国家社会にも貢献する有益
な発明である。
To reduce waste pollution, which continues to increase every year and is a hindrance to local government operations, to reduce waste disposal costs for each local government, and to utilize it as an alternative energy from the standpoint of using resources more effectively. It is a useful invention that also contributes to the national society.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本発明の詳細な説明図である。 第2図は、本発明の詳細な説明図である。 (5)           選別機 (1)(IA)(IB)(1(3)(IE)    ホ
ッパー(2に2A)          破砕機(2B
) (2Cり (2E)      粉砕機(8)(8
A)(8BX8C)(8E)   バーナーと送風機(
4)(4A)(4B)(4C)(4E)   乾燥機(
5)(5A)(5B)(50)(5E)   ホッパー
(6)            スクリューフィーダー
(7)(7)′        ホッパー(8) (8
)’          スクリューコンベヤー(9)
          攪拌機 (10)          スクリューコンベヤー(
11)         ホッパー (12)          スクリューフィーダー(
18)           ロータリーキルン(14
)         成型機 (15)           ローラー(16)  
        切断機 (17)          ガスボンベ(18)  
       ガスパイプ(19)         
 バーナー(20)         完成品 特開昭59−51;49B (5) 1、事件の表示 3・補正をする者 4、代 理 人 5、補正命令の日付 昭和!8年Z月ノ 日 76補正の内容 別紙の通り
FIG. 1 is a detailed explanatory diagram of the present invention. FIG. 2 is a detailed explanatory diagram of the present invention. (5) Sorter (1) (IA) (IB) (1 (3) (IE) Hopper (2A to 2) Shredder (2B)
) (2C (2E) Pulverizer (8) (8
A) (8BX8C) (8E) Burner and blower (
4) (4A) (4B) (4C) (4E) Dryer (
5) (5A) (5B) (50) (5E) Hopper (6) Screw feeder (7) (7)' Hopper (8) (8
)' Screw conveyor (9)
Stirrer (10) Screw conveyor (
11) Hopper (12) Screw feeder (
18) Rotary kiln (14)
) Molding machine (15) Roller (16)
Cutting machine (17) Gas cylinder (18)
Gas pipe (19)
Burner (20) Completed product JP-A-59-51;49B (5) 1. Indication of the incident 3. Person making the amendment 4. Agent 5. Date of amendment order Showa! Contents of the amendment dated 76th day of month Z, 8th year as per the attached sheet.

Claims (1)

【特許請求の範囲】 (1)産業廃棄物、都市ゴミ中に混入する可燃性物質を
原料とした廃棄物固型燃料の製造法(2)産業廃棄物、
都市ゴミ中に混入する可燃性物質を原料とし、これら廃
棄物の分離選別を行ない、再度適当な比率に配合し加熱
成型してなる、特許請求の範囲第1項記載の廃棄物固型
燃料の製造法 (8)産業廃棄物、都市ゴミ中の可燃性物質を原料とし
、これら廃棄物中に混入するプラスチック系物質、古タ
イヤ類、ゴム類、木質系物質、都市ゴミ等の分離選別を
行ない、これらのものを再度適当なる比率に配合し、加
熱成型してなる特許請求の範囲第1項記載の廃棄物固型
燃料の製造法
[Claims] (1) A method for producing waste solid fuel using combustible substances mixed in industrial waste and municipal waste as raw materials (2) Industrial waste,
The waste solid fuel according to claim 1, which is made from combustible substances mixed in municipal garbage, is separated and sorted, and is blended again in an appropriate ratio and heat-molded. Manufacturing method (8) Uses combustible substances in industrial waste and municipal garbage as raw materials, and separates and sorts out plastic materials, old tires, rubber, wood materials, municipal garbage, etc. that are mixed in these wastes. , a method for producing solid waste fuel according to claim 1, wherein these materials are blended again in an appropriate ratio and heated and molded.
JP16812882A 1982-09-26 1982-09-26 Preparation of solid fuel from wastes Pending JPS5956496A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16812882A JPS5956496A (en) 1982-09-26 1982-09-26 Preparation of solid fuel from wastes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16812882A JPS5956496A (en) 1982-09-26 1982-09-26 Preparation of solid fuel from wastes

Publications (1)

Publication Number Publication Date
JPS5956496A true JPS5956496A (en) 1984-03-31

Family

ID=15862355

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16812882A Pending JPS5956496A (en) 1982-09-26 1982-09-26 Preparation of solid fuel from wastes

Country Status (1)

Country Link
JP (1) JPS5956496A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6140398A (en) * 1984-07-31 1986-02-26 Toshiro Watanabe Method for treatment utilizing waste as water-repellent solid fuel
JPS61247789A (en) * 1985-04-26 1986-11-05 Kawasaki Steel Corp Automatic temperature elevation drying for pulverized coal producing apparatus
CZ305274B6 (en) * 2008-07-07 2015-07-15 PolyComp, a. s. Alternative solid refuse derived fuel
JP2023046445A (en) * 2021-09-24 2023-04-05 株式会社トリウミ Manufacturing method of waste tire-containing solid fuel

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6140398A (en) * 1984-07-31 1986-02-26 Toshiro Watanabe Method for treatment utilizing waste as water-repellent solid fuel
JPS61247789A (en) * 1985-04-26 1986-11-05 Kawasaki Steel Corp Automatic temperature elevation drying for pulverized coal producing apparatus
JPH0576997B2 (en) * 1985-04-26 1993-10-25 Kawasaki Steel Co
CZ305274B6 (en) * 2008-07-07 2015-07-15 PolyComp, a. s. Alternative solid refuse derived fuel
JP2023046445A (en) * 2021-09-24 2023-04-05 株式会社トリウミ Manufacturing method of waste tire-containing solid fuel

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