JPS5947296A - Preparation of solid fuel from organic sludge - Google Patents

Preparation of solid fuel from organic sludge

Info

Publication number
JPS5947296A
JPS5947296A JP15659482A JP15659482A JPS5947296A JP S5947296 A JPS5947296 A JP S5947296A JP 15659482 A JP15659482 A JP 15659482A JP 15659482 A JP15659482 A JP 15659482A JP S5947296 A JPS5947296 A JP S5947296A
Authority
JP
Japan
Prior art keywords
organic sludge
solid fuel
dried
raw material
dehydrated
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
JP15659482A
Other languages
Japanese (ja)
Inventor
Hidekazu Fujimori
藤森 英一
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.)
Japan Steel Works Ltd
Original Assignee
Japan Steel Works Ltd
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 Japan Steel Works Ltd filed Critical Japan Steel Works Ltd
Priority to JP15659482A priority Critical patent/JPS5947296A/en
Publication of JPS5947296A publication Critical patent/JPS5947296A/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 prepare solid fuel without the need of any binder and without generation of harmful gas, by granulating dehydrated organic sludge, molding the dried granules by extrusion molding at a temperature and under a pressure which cause plasticization and then drying cut pieces by forced draft. CONSTITUTION:Organic sludge (e.g. those produced in pulp and fermentation industries) is dehydrated and crushed into small granules. The granules are dried to a water content of 5-25wt%. The dried granules are molded by extrusion molding. The formed product is cut and the cut pieces are cooled by forced draft into pellets of solid fuel. It has been a general practice to mix dehydrated and dried organic sludge with a binder (e.g. coal, tar, pitch or waste oil) for molding, but the method has a demerit in that it requires a large amount of binder which generates harmful gas in combustion. This invention eliminates such disadvantages.

Description

【発明の詳細な説明】 本発明は、有機質汚泥からの固形燃料製造方法に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing solid fuel from organic sludge.

パルプ工業、醸造業等の分野においては有機質を主成分
とする汚泥が多量に発生する。これらの有機質汚泥の大
部分は焼却、海洋投棄、埋立等によって処分されている
が、このような処分方法は多大な費用を必要とするだけ
でなく、環境破壊をひき起こす原因ともなっていた。有
機質汚泥を嫌気性消化、堆肥化、熱分解等によって資源
として回収することも一部実用化されているが、効率、
費用等に制約されて大量には行なわれていない。
In fields such as the pulp industry and the brewing industry, a large amount of sludge mainly composed of organic matter is generated. Most of these organic sludges are disposed of by incineration, ocean dumping, landfilling, etc., but these disposal methods not only require a large amount of cost but also cause environmental destruction. Recovery of organic sludge as a resource through anaerobic digestion, composting, thermal decomposition, etc. has been partially put into practical use, but efficiency and
It is not carried out on a large scale due to cost constraints.

有機質汚泥を固形燃料化して再利用することも行なわれ
ている。有機質汚泥を固形化するために、従来は、有機
質汚泥を脱水し乾燥した後、粘結剤(石炭、タール、ピ
ッチ、重質油、廃油等)と4昆練して成形していた。し
かし、このような従来の有機質汚泥からの固形燃料製造
方法には、大量の粘結剤が必要であるという欠点、及び
燃焼時に粘結剤が有害ガスを発生するため固形化燃料の
利用面で制約されるという欠点があった。
Organic sludge is also converted into solid fuel and reused. Conventionally, in order to solidify organic sludge, the organic sludge was dehydrated and dried, and then kneaded with a binder (coal, tar, pitch, heavy oil, waste oil, etc.) and molded. However, this conventional method for producing solid fuel from organic sludge has the disadvantage of requiring a large amount of binder, and the binder generates harmful gases during combustion, making it difficult to use solidified fuel. It had the disadvantage of being restricted.

本発明は、従来の有機質汚泥からの固形燃料製造方法に
おける上記ような問題点に着目してなされたものであり
、原料である脱水した有機質汚泥を解砕して小粒子状と
し、この小粒子状の原料を乾燥させて水分が5〜25(
重量)%の乾燥原料とし、乾燥原料が可塑化する温度及
び圧力下においてこれを押出し成形し、押出された成形
品を切断し、切断された成形品を強制通風冷却して固形
燃料ペレッI・とすることにより、上記問題点を解消す
ることを目的としている。
The present invention was made by focusing on the above-mentioned problems in the conventional method for producing solid fuel from organic sludge. Dry the raw material to reduce the moisture content to 5 to 25 (
% by weight as a dry raw material, extrusion molded at a temperature and pressure that plasticizes the dry raw material, cut the extruded molded product, and cooled the cut molded product with forced ventilation to form solid fuel pellets I. The purpose of this is to solve the above problems.

以下、本発明を添付図面に基づいて説明する。Hereinafter, the present invention will be explained based on the accompanying drawings.

図面に本発明方法の工程を示す。The drawings show the steps of the method of the invention.

まず、有機物を主成分とする汚泥を脱水機により脱水し
て、有機質汚泥のかたまりを作る。現在実用化されてい
る高性能の脱水機を使用すれば含水率45〜55(重量
)%程度まで脱水することができる。
First, sludge whose main component is organic matter is dehydrated using a dehydrator to form a mass of organic sludge. If a high-performance dehydrator that is currently in practical use is used, it is possible to dehydrate to a water content of about 45 to 55% (by weight).

次に、脱水した有機質汚泥のかたまりを解砕機によって
直径10mm以下の小粒子に解砕し、これを乾燥機(例
えば、回転ドラム式乾燥機)によって乾燥する。この乾
燥によって小粒子状原料の水分を5〜25(重量)%と
する。なお、乾燥原料の水分が5%より少ないと、後述
のダイス内において可塑化されず粉末状となって成形す
ることができない。また乾燥原料の水分が25%以上の
場合にはダイス内において所定の圧力に達しないため成
形が困難であり、また成形することができたとしてもペ
レッ)・は軟弱で圧密性に欠けたものとなる。乾燥機の
熱源としては、本工程によって得られる乾燥原料の一部
を使用する。
Next, the dehydrated organic sludge mass is crushed into small particles with a diameter of 10 mm or less using a crusher, and these are dried using a dryer (for example, a rotating drum dryer). This drying brings the moisture content of the small particulate raw material to 5 to 25% (by weight). It should be noted that if the moisture content of the dry raw material is less than 5%, it will not be plasticized in the die described below and will become powder-like and cannot be molded. Furthermore, if the moisture content of the dry raw material is 25% or more, it will be difficult to mold it because the specified pressure will not be reached in the die, and even if it can be molded, the pellets will be soft and lack compactness. becomes. A part of the dry raw material obtained by this process is used as a heat source for the dryer.

乾燥原料はコンベアによって原料貯留槽に送っていった
ん貯留する。原料貯留槽内の乾燥原料は定量供給機によ
ってミキサーに送られ、ミキサー内でかくはんされた後
、連続圧縮成形機に定量供給される。ミキサーは連続圧
縮成形機に供給される乾燥原料の粒度及び性状を均一化
する機能を有し、これによって連続圧縮成形機の負荷が
均一化されると共に成形品の品質が安定する。
Dry raw materials are sent to a raw material storage tank by a conveyor and stored there. The dry raw material in the raw material storage tank is sent to a mixer by a quantitative feeder, stirred in the mixer, and then quantitatively fed to a continuous compression molding machine. The mixer has the function of uniformizing the particle size and properties of the dry raw material supplied to the continuous compression molding machine, thereby equalizing the load on the continuous compression molding machine and stabilizing the quality of the molded product.

連続圧縮成形機は、モータによって回転駆動される円筒
状のダイスと、ダイスの内径部に接するように配置した
複数のロールと、乾燥原料をダイス内径部と各ロールと
の間のすきまに均等に分配するスプレッダとを有してい
る。ダイスは、内径部から外周面に通じる半径方向ダイ
ス穴を有している。ダイス穴の直径は5〜7mmである
。ダイス内径部に定量供給された乾燥原料はダイス内周
面とロール外周面との間にかみ込まれ、ダイス穴から連
続的に押し出される。ダイスとロールとの間にかみ込ま
れた乾燥原料は圧縮され、ダイス穴を通過するときには
、100〜150℃の温度及び400〜8000 k 
g / c m 2の圧力に達する。この高温・高圧力
のために、乾燥原料は可塑化され、原料中の油脂、リグ
ニン等によって自己粘結性を有するようになり、また圧
密性も高くなる。また、原料がダイス穴を通過する際、
原料中の油脂性等が表面ににじみ出て、成形品の表面に
疎水性の膜が形成される。このため、成形品は耐水性を
有する。
A continuous compression molding machine consists of a cylindrical die that is rotationally driven by a motor, multiple rolls that are placed in contact with the inner diameter of the die, and a dry raw material that is evenly distributed between the inner diameter of the die and each roll. and a dispensing spreader. The die has a radial die hole extending from the inner diameter to the outer circumferential surface. The diameter of the die hole is 5-7 mm. The dry raw material supplied in a fixed amount to the inner diameter portion of the die is caught between the inner circumferential surface of the die and the outer circumferential surface of the roll, and is continuously extruded from the die hole. The dry raw material caught between the die and the roll is compressed, and when it passes through the die hole, it is heated at a temperature of 100 to 150°C and 400 to 8000 k.
A pressure of g / cm 2 is reached. Due to this high temperature and high pressure, the dried raw material is plasticized and becomes self-caking due to the oils, fats, lignin, etc. in the raw material, and also has high compactability. Also, when the raw material passes through the die holes,
Oil and fat in the raw materials ooze out to the surface, forming a hydrophobic film on the surface of the molded product. Therefore, the molded product has water resistance.

ダイス穴から押し出された円柱状の成形品は、ダイス外
周に近接して設けられたカッターナイフによって15〜
20mmの長さに切断される。こうして成形されたペレ
ットはペレット貯留容器に送られるが、その途中で強制
通風によって冷却される。この冷却によってペレットの
機械的強度が著しく向上する。従って、輸送の際等にペ
レットが破損することが防止され、燃料としての取扱い
が容易となる。また、冷却の際にはペレッ)・中の水分
の一部が蒸発し、水分が2〜3(重量)%減少するので
、燃料としてより好ましい状態となる。
The cylindrical molded product extruded from the die hole is cut by a cutter knife provided close to the outer periphery of the die.
Cut into 20mm lengths. The pellets formed in this way are sent to a pellet storage container, where they are cooled by forced ventilation. This cooling significantly improves the mechanical strength of the pellets. Therefore, the pellets are prevented from being damaged during transportation, and handling as fuel is facilitated. Also, during cooling, part of the water in the pellets evaporates, reducing the water content by 2 to 3% (by weight), making the pellets more desirable as fuel.

次に、上記方法を実施した具体例における物質収支につ
いて説明する。
Next, the material balance in a specific example in which the above method is implemented will be explained.

原料としては、故紙再生工程において発生する浮遊固形
物(紙繊維質を主成分とし、ポリエチレンを14(乾燥
重量)%含んでいる)を用いた。
As a raw material, suspended solids (mainly composed of paper fibers and containing 14% (dry weight) of polyethylene) generated in the waste paper recycling process were used.

なお、この浮遊固形物の発熱量は4960Kcal/k
g (乾燥重量)であった。上記浮遊固形物を含む廃水
を沈降分離後脱水し、水分を50(重量)%含むもの1
00kgを出発原料とした。この原料を解砕して乾燥す
ることにより39kgの水分を蒸発させたが、残る61
kgのうち11゜5kgは」二記乾燥のための燃料とし
て使用した。
The calorific value of this suspended solid is 4960Kcal/k
g (dry weight). Wastewater containing the above suspended solids is dehydrated after sedimentation separation and contains 50% (by weight) of water 1
00 kg was used as the starting material. By crushing and drying this raw material, 39 kg of water was evaporated, but the remaining 61 kg
Of the 11.5 kg, 11.5 kg was used as fuel for drying.

従って、乾燥原料として49.5kg(なお、水分を1
8(重量)%含む)が得られた。この乾燥原料を成形し
てベレット化し、強制通風により冷却・乾燥することに
より2kgの水分が失われ、最終的な製品ペレットとし
ては47.7kg(水分を15(重量)%含む)が得ら
れた。すなわち、100kgの出発原料から47.7k
gの製品ペレットを得ることができた。なお、出発原料
の乾燥のために使用された乾燥原料の自己消費率は(1
1,5/(11,5+49.5))X100=19%で
あり、またプランI・全体の電力消費縁は約180KW
H/l  (製品ペレット)であった。
Therefore, the dry raw material was 49.5 kg (in addition, the water content was reduced to 1
8% (by weight)) was obtained. This dried raw material was molded into pellets, cooled and dried by forced ventilation, resulting in a loss of 2 kg of water, resulting in a final product pellet weighing 47.7 kg (containing 15% (by weight) water). . That is, 47.7k from 100kg of starting material
g of product pellets could be obtained. In addition, the self-consumption rate of the dry raw material used for drying the starting raw material is (1
1,5/(11,5+49.5))X100=19%, and the total power consumption of Plan I is approximately 180KW.
H/l (product pellet).

以上説明してきたように、本発明によると、原料である
脱水した有機質汚泥を解砕して小粒子状とし、この小粒
子状の原料を乾燥させて水分が5〜25(重量)%の乾
燥原料とし、乾燥原料が可塑化する温度及び圧力下にお
いてこれを押出し成形し、押出された成形品を切断し、
切断された成形品を強制通風冷却して固形燃料ペレット
とするので、従来は処分に困っていた有機質汚泥を固形
燃料として利用することができるようになり、しかも成
形の際には原料の自己粘結性を利用するので粘結剤が不
必要であり、粘結剤の費用及び粘結剤からの悪性ガスの
発生という問題がなくなる。
As explained above, according to the present invention, dehydrated organic sludge, which is a raw material, is crushed into small particles, and this small particle-shaped raw material is dried to a moisture content of 5 to 25% (by weight). As a raw material, extrude it under the temperature and pressure that plasticizes the dry raw material, cut the extruded molded product,
Since the cut molded products are cooled with forced ventilation to form solid fuel pellets, it is now possible to use organic sludge, which was previously difficult to dispose of, as solid fuel. Since caking is utilized, no caking agent is required, and problems such as the cost of caking agent and the generation of malignant gas from the caking agent are eliminated.

また、ペレッI・は直径5〜7 m m、長さ15〜2
0mmの円柱状であり、燃焼装置への自動供給及び空気
輸送等を容易に行なうことができ、また従来の石炭ボイ
ラの燃料としてそのまま使用することができ、重油バー
ナ、ガスバーナ等にはバーナ部の一部改造によって使用
可能である。更に、本方法を実施するだめの設備は、脱
水機、解砕機、乾燥機、成形機、切断装置(カッタナイ
フ)及び冷却装置であり、プロセスは単純化されている
ため設備も安価である。
In addition, Pellet I. has a diameter of 5 to 7 mm and a length of 15 to 2 mm.
It has a cylindrical shape with a diameter of 0 mm, and can be easily supplied automatically to combustion equipment and transported by air, and can be used as fuel in conventional coal boilers. It can be used with some modification. Furthermore, the equipment for implementing this method is a dehydrator, a crusher, a dryer, a molding machine, a cutting device (cutter knife), and a cooling device, and since the process is simple, the equipment is inexpensive.

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

図面は本発明の工程を示す図である。 特許出願人 株式会社1」木製鋼所 代理人  弁理士 宮内利行 The drawings are diagrams showing the steps of the present invention. Patent applicant: 1 Co., Ltd. Wooden Steel Works Agent: Patent attorney: Toshiyuki Miyauchi

Claims (1)

【特許請求の範囲】[Claims] 脱水した有機質汚泥を解砕して小粒子状とし、この小粒
子状の原料を乾燥させて水分が5〜25(重量)%の乾
燥原料とし、乾燥原料が可塑化する温度及び圧力下にお
いてこれを押出し成形し、押出された成形品を切断し、
切断された成形品を強制通風冷却して固形燃料ペレット
とする有機質汚泥からの固形燃料製造方法。
The dehydrated organic sludge is crushed into small particles, this small particle material is dried to obtain a dry material with a water content of 5 to 25% (by weight), and this is heated at a temperature and pressure that plasticizes the dry material. extrusion molding, cutting the extruded molded product,
A method for producing solid fuel from organic sludge, in which cut molded products are cooled with forced ventilation to produce solid fuel pellets.
JP15659482A 1982-09-10 1982-09-10 Preparation of solid fuel from organic sludge Pending JPS5947296A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15659482A JPS5947296A (en) 1982-09-10 1982-09-10 Preparation of solid fuel from organic sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15659482A JPS5947296A (en) 1982-09-10 1982-09-10 Preparation of solid fuel from organic sludge

Publications (1)

Publication Number Publication Date
JPS5947296A true JPS5947296A (en) 1984-03-16

Family

ID=15631165

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15659482A Pending JPS5947296A (en) 1982-09-10 1982-09-10 Preparation of solid fuel from organic sludge

Country Status (1)

Country Link
JP (1) JPS5947296A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6116353U (en) * 1984-06-11 1986-01-30 荏原インフイルコ株式会社 Organic sludge solid fuel equipment
KR100387272B1 (en) * 2002-05-06 2003-06-18 Jungmin Construction Co Ltd Method for pressing and pelletizing organic sludge, and apparatus therefor
KR100459031B1 (en) * 1996-08-05 2005-04-06 주식회사 엘지화학 Manufacturing method of extruded molded body using wastewater sludge
CN108380363A (en) * 2018-03-19 2018-08-10 田东昊润新材料科技有限公司 A kind of high-purity montmorillonite new industrialization purification preparation technique
JP2020002323A (en) * 2018-07-02 2020-01-09 株式会社エム・アイ・エス Fuel production apparatus using organic sludge

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6116353U (en) * 1984-06-11 1986-01-30 荏原インフイルコ株式会社 Organic sludge solid fuel equipment
JPH0226920Y2 (en) * 1984-06-11 1990-07-20
KR100459031B1 (en) * 1996-08-05 2005-04-06 주식회사 엘지화학 Manufacturing method of extruded molded body using wastewater sludge
KR100387272B1 (en) * 2002-05-06 2003-06-18 Jungmin Construction Co Ltd Method for pressing and pelletizing organic sludge, and apparatus therefor
CN108380363A (en) * 2018-03-19 2018-08-10 田东昊润新材料科技有限公司 A kind of high-purity montmorillonite new industrialization purification preparation technique
JP2020002323A (en) * 2018-07-02 2020-01-09 株式会社エム・アイ・エス Fuel production apparatus using organic sludge

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