JPS60112892A - Process for producing solid fuel from industrial waste - Google Patents

Process for producing solid fuel from industrial waste

Info

Publication number
JPS60112892A
JPS60112892A JP22005683A JP22005683A JPS60112892A JP S60112892 A JPS60112892 A JP S60112892A JP 22005683 A JP22005683 A JP 22005683A JP 22005683 A JP22005683 A JP 22005683A JP S60112892 A JPS60112892 A JP S60112892A
Authority
JP
Japan
Prior art keywords
waste
raw material
sludge
solid fuel
main raw
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
JP22005683A
Other languages
Japanese (ja)
Inventor
Yukio Miyagi
宮城 幸男
Hiroshi Okita
沖田 浩
Koichi Nishikawa
幸一 西川
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.)
KANSAI SANGYO KK
Original Assignee
KANSAI SANGYO KK
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 KANSAI SANGYO KK filed Critical KANSAI SANGYO KK
Priority to JP22005683A priority Critical patent/JPS60112892A/en
Publication of JPS60112892A publication Critical patent/JPS60112892A/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 obtain a solid fuel for e.g. boiler, etc. from an industrial waste, by dehydrating a main raw material such as pulp sludge, and mixing and kneading the product with the subsidiary material such as kneaded and crushed waste of petroleum refining process having relatively high calorific value. CONSTITUTION:A main raw material composed of the sludge of pulp and paper industry containing organic components such as cellulose, lignin, etc. and optionally mixed with other sludge or sewage sludge such as municipal waste containing other organic components, is preliminarily dehydrated, and subjected to the main dehydration optionally in the presence of a dehydration assistant. Separately, the subsidiary raw material composed of the waste of petroleum refining process, combustible municipal waste, waste oil, waste organic solvent, vehicle, etc. is kneaded and crushed, and the product is mixed and kneaded with the above main raw material to obtain the objective solid fuel.

Description

【発明の詳細な説明】 この発明は産業廃棄物から固形燃料を製造する方法に係
り、その目的は産業廃棄物(可燃性固形分)を利用し、
その産業廃棄物を再生して燃焼炉等の燃料として再生で
きることからなる産業廃棄物から固形燃料を製造する方
法の提供にある。
[Detailed Description of the Invention] This invention relates to a method for producing solid fuel from industrial waste, and its purpose is to utilize industrial waste (flammable solid content),
The object of the present invention is to provide a method for producing solid fuel from industrial waste, which can be recycled as fuel for combustion furnaces and the like.

一般に、パルプ、製紙工場からの排出汚泥にはセルロー
ス、リグニン等の可燃性固形質が含まれるが含水率が高
い為にこれを焼却することはむづかしいという事情があ
った。
Generally, sludge discharged from pulp and paper mills contains flammable solids such as cellulose and lignin, but it is difficult to incinerate this because of its high moisture content.

この発明は上記事情にてらしてなされたもので、セルロ
ース5 リグニン等の有機質を含むパルプ、製紙汚泥や
他の有機質を含む都市ゴミなどの汚泥、或いは原尿汚泥
更には有機溶剤を含む産業廃棄物等をその排出場所に於
て処理し、且つそれを燃料として再生利用することによ
って、埋立や焼却及び海洋投棄等の廃棄処理をなくし延
いてはエネルギー源の確保の一助となるように発明され
たもので即ち産業廃棄物から固形燃料を製造する方法に
関する。
This invention was made in view of the above-mentioned circumstances, and is applicable to pulp containing organic matter such as cellulose 5 lignin, sludge such as paper manufacturing sludge and municipal waste containing other organic matter, raw urine sludge, and even industrial waste containing organic solvents. It was invented to eliminate waste disposal such as landfilling, incineration, and ocean dumping by treating waste at the place where it is discharged and reusing it as fuel, thereby helping to secure energy sources. The present invention relates to a method for producing solid fuel from industrial waste.

この発明を以下図面に基づき詳述する。This invention will be explained in detail below based on the drawings.

第1図はこの発明のの代表的実施例のフローシートを示
し、第2図は第1図の模式断面説明図である。
FIG. 1 shows a flow sheet of a typical embodiment of the present invention, and FIG. 2 is a schematic cross-sectional explanatory diagram of FIG. 1.

図面において、(1)は主原料たるセルロース、リグニ
ン等の有機質を含むパルプ、製紙汚泥で、場合によって
は他の有機質を含む都市ゴミなどの汚泥、或いは深床汚
泥であってもよい。
In the drawings, (1) is pulp or papermaking sludge containing organic substances such as cellulose and lignin as main raw materials, and may also be sludge such as municipal waste containing other organic substances, or deep bed sludge.

この主原料(1)は通富含水率が80%以上である。This main raw material (1) has a water content of 80% or more.

(2)は前処理としての脱水処理工程である。(2) is a dehydration treatment step as a pretreatment.

この脱水処理工程(2)では、少なくとも、主原料の含
水率が10%は低下する様に処理するが、粘度の低いバ
ルブ、製紙汚泥では含水率は30%程脱水助剤の添加工
程をしめす。
In this dehydration treatment step (2), the water content of the main raw material is treated to decrease by at least 10%, but for valves and papermaking sludge with low viscosity, the water content is about 30%, which indicates the addition process of a dehydration aid. .

(4)は主たる脱水処理工程で、この脱水処理工程では
、主原料(1)の種類を問わず確実に含水率を50%程
度まで落とす。
(4) is the main dehydration process, and in this dehydration process, the water content is reliably reduced to about 50% regardless of the type of main raw material (1).

(5)はこの脱水処理工程(4)から排出される排水の
処理をする排水処理工程である。
(5) is a wastewater treatment step for treating the wastewater discharged from this dehydration treatment step (4).

(6)は副原料で、この副原料(6)は石油精製カス、
可燃製都市ごみ、廃油、廃有機溶剤、更にはビヒクル等
からなる。
(6) is an auxiliary raw material, and this auxiliary raw material (6) is petroleum refinery residue,
It consists of combustible municipal waste, waste oil, waste organic solvents, and even vehicles.

(7)は副原料(6)の混練破砕工程で、この混練破砕
工程で前記石油精製カス、可燃製都市ごみ、廃油、廃有
機溶剤、更にはビヒクル等からなる副原料(6)を混合
する。
(7) is a kneading and crushing process for the auxiliary raw material (6), in which the auxiliary raw material (6) consisting of the petroleum refinery scum, combustible municipal waste, waste oil, waste organic solvent, and even a vehicle is mixed. .

(8)は少なくとも含水率を50%程度まで低下させた
主原料(1)と混合された前記副原料(6)を混練する
混練工程をしめず。
(8) does not include the kneading step of kneading the auxiliary raw material (6) mixed with the main raw material (1) whose water content has been reduced to at least about 50%.

このようにして混練工程(8)を経た押し出し物は、原
料自身にふくまれる水分がバインダーとしての機能を持
ち、更には必要に応して副原料(6)の混練破砕工程(
7)から供給されたビヒクルによって、造形された固形
燃料(9)となる。
In the extruded product that has undergone the kneading step (8) in this way, the water contained in the raw material itself has a function as a binder, and if necessary, the kneading and crushing step of the auxiliary raw material (6) (
The vehicle supplied from 7) becomes a shaped solid fuel (9).

この固形燃料(9)は少なくとも300(Mca I 
/ Kgをゆうする。
This solid fuel (9) has at least 300 (Mca I
/ Transfer Kg.

この様にして製造された固形燃料(9)は一時的に倉庫
00)に貯蔵されるか、直ちにボイラー等の燃焼装置て
11)に供給される。
The solid fuel (9) produced in this way is either temporarily stored in a warehouse 00) or immediately supplied to a combustion device 11) such as a boiler.

このような構成からなるこのこう発明に係る産業廃棄物
から固形燃料を製造する方法を、第2図に基づいて更に
説明すると、製紙、バルブ工場(12)から排出された
主原料(11を脱水tJ、1l(13)(例えば、図で
はスクリュープレス)で脱水して水分を約35〜40%
(重量)以下の製紙汚泥ケーキ+11となし、これをサ
ービスホッパー(14)に投入する。
The method for producing solid fuel from industrial waste according to the present invention having such a configuration will be further explained based on FIG. tJ, 1l (13) (for example, screw press in the figure) to remove water to about 35-40%
A paper sludge cake of (weight) below +11 is prepared, and this is put into the service hopper (14).

一方、印刷工場から排出されるビヒクル、溶剤及び油等
を含む廃インクの蒸溜残渣(15)等を予めサービスホ
ッパー(16)に投入し、サービスホッパー(14)に
貯蔵された製紙汚泥ケーキ(1)と前記蒸溜残渣(15
)を排出重、量比的10:1〜5:1となるよう調整さ
れたスクリューフィーダー(1?)及び(18)により
排出してスクリューコンベア(19)で合流させる。
On the other hand, the distillation residue (15) of waste ink containing vehicle, solvent, oil, etc. discharged from the printing factory was previously put into the service hopper (16), and the paper manufacturing sludge cake (15) stored in the service hopper (14) ) and the distillation residue (15
) are discharged by screw feeders (1?) and (18) adjusted to have a discharge weight and quantity ratio of 10:1 to 5:1, and are combined on a screw conveyor (19).

この合流体は該スクリューコンヘア(19)の排出口(
20)より混練機(21)に投入され、混練機(21)
内で投入口(22)側から排出口(23)側に移送され
ながら上記汚泥ケーキ[11と蒸溜残渣(15)とは充
分混練される。
This confluence is the outlet of the screw conhair (19) (
20) into the kneading machine (21), and the kneading machine (21)
The sludge cake [11] and the distillation residue (15) are sufficiently kneaded while being transferred from the input port (22) side to the discharge port (23) side.

排出口(23)からフレーク状の固形燃料(9)かヘル
ドコンベア(24)に落下し該ベルトコンヘア(24)
により搬出され貯蔵容器(25)に貯えられる混練工程
に於いて、上記被混練物に刺i奥がある場合には、適当
な脱臭剤を混練と同時に連続的に投入するようにすれば
この臭いが緩和され作業もし易(なるのでのぞましい。
The flaky solid fuel (9) falls from the discharge port (23) onto the heald conveyor (24) and is conveyed to the belt conveyor (24).
During the kneading process, when the materials to be kneaded are transported out and stored in the storage container (25), if the materials to be kneaded have thorns, this odor can be removed by continuously adding a suitable deodorizing agent at the same time as the kneading. This is desirable because it eases the problem and makes the work easier.

上記製紙汚泥(1)は一般には水分約60%(重量)以
上含まれ、その発熱量は約1500Kcal/ kg以
下であるが、脱水後は発熱量的1800〜24、 OO
K c a 1 / kgである。
The above papermaking sludge (1) generally contains about 60% or more water (by weight) and has a calorific value of about 1,500 Kcal/kg or less, but after dehydration it has a calorific value of 1,800 to 24,000 Kcal/kg or less.
K ca 1/kg.

一方蒸溜残渣には、未揮発の各種有機溶剤約lO%(f
fiりが含まれ、その発熱量的6300〜7800Kc
 a 17kgであるが。
On the other hand, the distillation residue contains about 10% (f
The calorific value is 6300-7800Kc.
a It is 17 kg.

これは印刷工場で排出される廃インクから蒸溜により有
機溶剤を回収した残渣であって、従来焼却により処理さ
れていたものである。
This is a residue obtained by distilling organic solvents from waste ink discharged from printing factories, and has traditionally been disposed of by incineration.

この様にして得られた、固形燃料(9)の発熱量はほぼ
3500〜450’OKc a l 7kgであった。
The calorific value of the solid fuel (9) thus obtained was approximately 3500 to 450'OKcal 7 kg.

尚、上記実施例では2種の産業廃棄物として製紙汚泥及
び廃インクを採用した例を示したが、これに限らず比較
的発熱量の低い廃棄物も、従来焼却処理されていた比較
的高い発熱量を有する廃棄物と混練することによってボ
イラー等の固形燃料として再生利用し得る。
In addition, in the above example, paper manufacturing sludge and waste ink were used as two types of industrial waste, but this is not limited to wastes with a relatively low calorific value. By mixing it with waste that has a calorific value, it can be recycled as solid fuel for boilers, etc.

以上詳述した如く、この発明に係る産業廃棄物から固形
燃料を製造する方法は2種の可燃性産業廃棄物を極めて
簡易に有用な固形燃料とすることが出来、従来埋立てた
り一部焼却されていていた製紙汚泥の如き廃棄物をその
発生場所で上記の如く固形燃料とし得るから、投棄の為
の場所を確保する必要もなくまたその輸送に用する労力
も要しなくなる上に新たなエネルギー源を製することに
なり、しかも従来焼却処理されていた比較的高発熱量の
廃棄物も上述の如く有効に利用される効果を奏する。
As explained in detail above, the method for producing solid fuel from industrial waste according to the present invention allows two types of combustible industrial waste to be made into useful solid fuel very easily, and it is possible to convert the two types of combustible industrial waste into useful solid fuel, and it Since waste such as paper sludge, which had previously been used as paper manufacturing sludge, can be turned into solid fuel at the place where it is generated, there is no need to secure a place for dumping it, and there is no need for labor to transport it. An energy source is produced, and wastes with a relatively high calorific value, which have conventionally been incinerated, can be effectively utilized as described above.

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

第1図はこの発明に係る産業廃棄物から固形燃料を製造
する方法のフローシート図、第2図は同説明図である。 +1)−主原料 (2)−脱水工程(前処理)(31−
脱水助剤添加工程 (41−生脱水工程 (61−副原料 (7)−混練破砕工程f8)−混練工程(9)−・−固
形燃料
FIG. 1 is a flow sheet diagram of a method for producing solid fuel from industrial waste according to the present invention, and FIG. 2 is an explanatory diagram thereof. +1) - Main raw material (2) - Dehydration process (pretreatment) (31-
Dehydration aid addition step (41-raw dehydration step (61-auxiliary raw material (7)-kneading crushing step f8)-kneading step (9)--solid fuel

Claims (1)

【特許請求の範囲】[Claims] (1)主原料と副原料の二種の産業廃棄物を使用し、こ
のセルロース、リグニン等の有機質を含むパルプ、製紙
汚泥で、場合によっては他の有機質を含む都市ゴミなど
の汚泥、或いは深床汚泥等からなる主原料をまず前処理
として脱水処理する工程と、必要に応じてこの主原料を
前処理として脱水処理する工程に追加する脱水助剤の添
加工程と、次いで行う主たる脱水処理工程と、これら一
連の主原料を処理する工程に平行し、石油精製カス、可
燃製都市ごみ、廃油、廃有機溶剤、更にはヒヒクル等か
らなる副原料を混練破砕する工程と、この混線破砕され
た副原料と前記脱水処理工程を経た主原料とを混合し且
つ混練する工程とからなる産業廃棄物から固形燃料を製
造する方法。
(1) Two types of industrial waste, the main raw material and the auxiliary raw material, are used, and pulp and paper sludge containing organic substances such as cellulose and lignin are used. In some cases, sludge such as municipal waste containing other organic substances, or deep A step in which the main raw material such as bed sludge is first dehydrated as a pre-treatment, a step in which a dehydration aid is added to the step in which the main raw material is dehydrated as a pre-treatment if necessary, and then the main dewatering step Parallel to the process of processing these main raw materials, there is a process of kneading and crushing auxiliary raw materials such as petroleum refinery scum, combustible municipal waste, waste oil, waste organic solvents, and even vehicles. A method for producing solid fuel from industrial waste, comprising a step of mixing and kneading an auxiliary raw material and a main raw material that has undergone the dehydration treatment process.
JP22005683A 1983-11-22 1983-11-22 Process for producing solid fuel from industrial waste Pending JPS60112892A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22005683A JPS60112892A (en) 1983-11-22 1983-11-22 Process for producing solid fuel from industrial waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22005683A JPS60112892A (en) 1983-11-22 1983-11-22 Process for producing solid fuel from industrial waste

Publications (1)

Publication Number Publication Date
JPS60112892A true JPS60112892A (en) 1985-06-19

Family

ID=16745238

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22005683A Pending JPS60112892A (en) 1983-11-22 1983-11-22 Process for producing solid fuel from industrial waste

Country Status (1)

Country Link
JP (1) JPS60112892A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03255192A (en) * 1990-03-05 1991-11-14 Norihiro Mitsunaga Fuel consisting mainly of organic sludge and preparation thereof
JPH101686A (en) * 1996-06-14 1998-01-06 Kawasaki Heavy Ind Ltd Production of compressed molding product of refuse
KR100908680B1 (en) 2009-01-22 2009-07-22 손민일 Solid fuel using waste paper sludge and waste oil, method for manufacturing the same
KR101033860B1 (en) * 2009-03-26 2011-05-16 손민일 Solid fuel of pellet form and method for preparing the same

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57139190A (en) * 1981-02-24 1982-08-27 Waeidou Kk Pelletized solid fuel

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57139190A (en) * 1981-02-24 1982-08-27 Waeidou Kk Pelletized solid fuel

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03255192A (en) * 1990-03-05 1991-11-14 Norihiro Mitsunaga Fuel consisting mainly of organic sludge and preparation thereof
JPH101686A (en) * 1996-06-14 1998-01-06 Kawasaki Heavy Ind Ltd Production of compressed molding product of refuse
KR100908680B1 (en) 2009-01-22 2009-07-22 손민일 Solid fuel using waste paper sludge and waste oil, method for manufacturing the same
KR101033860B1 (en) * 2009-03-26 2011-05-16 손민일 Solid fuel of pellet form and method for preparing the same

Similar Documents

Publication Publication Date Title
US4133273A (en) System for the disposal of sludge, hazardous and other wastes
US3342731A (en) Method for dewatering sludges
US3549010A (en) Methods and apparatus for disposing of waste materials
CA1085069A (en) Incineration of lime-conditioned sewage sludge with high sulfur fuel
US5433846A (en) Grease-trap wastewater treatment system
JP2007203213A (en) Method and apparatus for treating highly wet waste before hydration, and dehydration system equipped with this apparatus
US3549529A (en) Methods and apparatus for disposing of waste materials
US3652405A (en) Sewage and municipal refuse liquid phase coking process
JP4235091B2 (en) Method and apparatus for treating manure and organic sludge
JPS60112892A (en) Process for producing solid fuel from industrial waste
JP5039634B2 (en) Waste treatment facility and waste treatment method
KR20030014235A (en) Method and system for utilising waste
KR19990076618A (en) Separation method of waste mixture
JP2000239050A (en) Treatment of plant waste fluid
KR100663994B1 (en) Sewage cleaning device of resource process from food-wastes
US20220112109A1 (en) Organic waste treatment process
JPS60112893A (en) Apparatus for producing solid fuel from industrial waste
SU994442A1 (en) Process for treating precipitates of effluents from textile production
JPH07124599A (en) Sludge dehydration method
KR200426621Y1 (en) Regeneration fuel manufacturing apparatus using waste oil and organic sludge
KR20080002565U (en) Use apparatus of food garbage
CA1066857A (en) Biological sludge incineration in the recovery furnace of a cellulose processing facility
Ricci A method of manure disposal for a beef packing operation: first interim technical report
Hamm Environmental aspects
JPH06102791B2 (en) Used paper waste fuel