JPS60123594A - Solid fuel, its manufacture and manufacturing unit for the same - Google Patents
Solid fuel, its manufacture and manufacturing unit for the sameInfo
- Publication number
- JPS60123594A JPS60123594A JP23192483A JP23192483A JPS60123594A JP S60123594 A JPS60123594 A JP S60123594A JP 23192483 A JP23192483 A JP 23192483A JP 23192483 A JP23192483 A JP 23192483A JP S60123594 A JPS60123594 A JP S60123594A
- Authority
- JP
- Japan
- Prior art keywords
- powder
- solid fuel
- waste
- combustion pot
- combustion
- 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
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
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、廃タイヤや廃棄プラスチックを原料とした固
形燃料に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to solid fuel made from waste tires and waste plastics.
ボイラー燃料には液体、固形又は粉状の３種類があり、
固形の場合は主に石炭が使われている。There are three types of boiler fuel: liquid, solid, or powder.
In solid form, coal is mainly used.
最近、液体燃料の価格］二υＶにより、廃タイヤ又は廃
棄プラスチック、廃油、木屑なとを燃料とする省エネル
ギークイブのボイラーか多くなり、各社各様の方式が提
案されているか、カロリーや硫黄含有率、粒径の面で５
！Ｉｆ点かあり、普及にはまだまだ障壁かある。Recently, due to the price of liquid fuel [2υV], energy-saving Quib boilers that use waste tires, waste plastic, waste oil, and wood chips as fuel have become more common, and various companies are proposing various methods, or they contain calories and sulfur. 5 in terms of rate and particle size.
! There are some If points, and there are still barriers to widespread use.
本発明は、このような従来の問題点を解消してカロリー
をある範囲で任意に選定でき、有害な硫黄分を抑え、ま
た形状の揃った固形燃料及びその製造方法、並びにその
製造装置を提供することを目的とするものである。The present invention solves these conventional problems and provides a solid fuel that allows the calorie to be arbitrarily selected within a certain range, suppresses harmful sulfur content, and has a uniform shape, a method for producing the same, and an apparatus for producing the same. The purpose is to
■）本発明に係る固形燃料は、
木質系粉粒４０〜５０重量部、廃タイ４・粉粒２５〜３
５重量部、合成樹脂廃祠粉粒２０〜３０重量部を）も４
脂系結合剤及び樹脂系硬化剤で固化したものであり、■
）本発明に係る固形燃料の製造方法は、木質系有機物粉
粒及び廃タイヤ、廃棄合成樹脂粉粒を第１燃焼釜に投入
し、同第１燃焼釜内において前記粉粒を攪拌した後、２
気圧程度の加圧雰囲気中で２１５〜２５０°Ｃに加熱し
、材料が褐色になったときに祠料を第２燃焼釜に移動し
、同第２燃焼釜内で１４０〜１８０”Ｃの加熱下で攪拌
しながら樹脂系結合相及び樹脂系硬化剤を投入し、攪拌
機から取り出して所定の形状に成形するものであり、Ｉ
ｔ ）本発明に係る固形燃料の製造装置は、原料を粉砕
して粉粒にする粉砕装置と、同粉粒を加熱加圧及び攪拌
する第１燃焼釜と、第１燃焼釜から取り出した材料を加
熱攪拌する第２燃焼釜と、同第２燃焼釜から取り出した
材料を成形する成形機とを備えたものである。■) The solid fuel according to the present invention includes 40 to 50 parts by weight of wood powder, 4 parts by weight of waste tie, and 25 to 3 parts by weight of powder.
5 parts by weight, 20 to 30 parts by weight of synthetic resin waste abrasive powder) also 4
It is solidified with a fat-based binder and resin-based curing agent, and ■
) The method for producing solid fuel according to the present invention includes adding wood-based organic powder, waste tires, and waste synthetic resin powder to a first combustion pot, stirring the powder in the first combustion pot, and then 2
Heat to 215-250°C in a pressurized atmosphere of about atmospheric pressure, and when the material turns brown, move the abrasive material to the second combustion pot, and heat it to 140-180"C in the second combustion pot. The resin binder phase and resin curing agent are added while stirring under the stirrer, and then taken out from the stirrer and molded into a predetermined shape.
t) The solid fuel production apparatus according to the present invention includes a pulverizer that crushes raw materials into powder, a first combustion pot that heats, pressurizes, and stirs the powder, and a material taken out from the first combustion pot. It is equipped with a second combustion pot that heats and stirs the material, and a molding machine that molds the material taken out from the second combustion pot.
［発明の詳細な説明〕 以下、本発明を実施例に基いて説明する。[Detailed description of the invention] The present invention will be explained below based on examples.
第１図は本発明に係る固形燃料の製造方法のフローチャ
ートであり、固形燃料は以Ｆの手順て製造する。FIG. 1 is a flowchart of the method for producing solid fuel according to the present invention, and the solid fuel is produced according to the following procedure.
Ｉ原料粉砕
（ａｌポリエチレン、ポリスチロールなとのプラスチッ
ク廃材
（ｂｌ Ｉ、ａタイ−１・などのコム系皮相ｆｃｌおが
くずなどの植物性来月
これらを粉砕機によって所定の粒径以下に粉砕する。Pulverization of raw materials (plastic waste materials such as polyethylene and polystyrene (BL I, A-1, etc.), vegetable materials such as FCL sawdust, etc. are crushed to a predetermined particle size or less using a crusher.
ＩＩ加圧加熱攪拌（乾溜）
＋８＋前記の粉粒を第１加熱釜に投入し、釜内を２気圧
程度に保ぢ、２】５〜２５０″Ｃに加熱し、ミキサーで
攪拌する。この温度でタイヤは軟化し、乾性油が分離さ
れる。II Pressure heating stirring (dry distillation) +8+Put the above powder into the first heating pot, maintain the inside of the pot at about 2 atmospheres, heat to 2]5~250''C, and stir with a mixer.This temperature The tire is softened and the drying oil is separated.
■攪拌
乾性油を分離した材料を第２加熱釜に投入し、ミキサー
によって攪拌する。温度は１４０〜１８０°Ｃに加熱し
、植物系結合剤、硬化剤を投入する。■ Stirring The material from which the drying oil has been separated is put into the second heating pot and stirred by a mixer. The temperature is heated to 140-180°C, and a vegetable binder and a hardening agent are added.
例えば、エポキシ樹脂、クール、アスファルトなどを使
用することができる。For example, epoxy resin, cool, asphalt, etc. can be used.
ＩＶ加圧成型
第２加熱釜から祠料を搬出し、まだ冷却しないうちに加
圧成型する。IV pressure molding The abrasive material is carried out from the second heating pot and is pressure molded before it has cooled down yet.
〔実施１例〕 実際に試作した製品についてその結果を下に示す。[Example 1] The results of the prototype products are shown below.
なお、燃焼火力または設ω１ｒにより燃焼時間及び釜内
の温度は異なる。また、配合の量又Ｃ；ｔ：燃焼の時間
によりカロリー又は灰分、揮発分、固定炭素。Incidentally, the combustion time and the temperature inside the pot differ depending on the combustion thermal power or the setting ω1r. In addition, the amount of compounding or C; t: Calorie, ash content, volatile content, fixed carbon depending on the combustion time.
硫黄分の割合が調整できる。The sulfur content ratio can be adjusted.
固形燃料の大きさ及び形状は、成型の型により自由に設
定できる。The size and shape of the solid fuel can be freely set depending on the mold.
植物性の有機物と廃ブラ（プラス千ツク廃４わを加熱し
て炭化させ、結合剤、硬化剤を混入し、強度に圧力を加
えることにより、崩壊のない固形燃料を製作することか
できる。By heating and carbonizing vegetable organic matter and waste plastic waste, mixing binders and hardening agents, and applying intense pressure, it is possible to produce solid fuel that does not disintegrate.
製品祠料は、皮相が多く有り、また生産するにしても安
易であるため、今後の合成エネルギーとして最も有効で
ある。Product abrasive materials have many superficial layers and are easy to produce, making them the most effective synthetic energy source in the future.
製造過程で乾性油を抽出するため、排気は水蒸気が少量
用る程度である。Since drying oil is extracted during the manufacturing process, only a small amount of water vapor is used for exhaust.
第２図は本発明に係る固形燃料の製造設備の系統図であ
り、図中（１）はポリエチレン等のプラスチック系原料
タンク、（２）ばおがり−３゛等の木質系原料タンク、
（３）は廃クイ４・系原料タンク、（４）は搬送コンヘ
ア、（５）は結合相投入シュー１〜、（６）は燃焼加圧
釜、（７）は攪拌羽根、（８）は第１燃焼室、（９）は
ブロアー、００）は第２燃焼室、（１１）はバーナー、
（１２）はブ１コアー、（■３）は燃焼加圧釜（６）内
の原料を排出するコンヘア、（１４）はその開閉ダンパ
ー、（１５）は攪拌室、（１６）はその攪拌羽根、（１
７）は乾溜浦採油装置、（１８）は乾溜油タンク、（１
９）は冷却水パイプ、り２０）は水溜、（２１）は集塵
機、（２２）は灰出し容器である。FIG. 2 is a system diagram of the solid fuel manufacturing equipment according to the present invention, in which (1) is a plastic raw material tank such as polyethylene, (2) a wood raw material tank such as Baogari-3゛, etc.
(3) is the waste picket 4/system raw material tank, (4) is the conveyor container, (5) is the binder phase input shoe 1~, (6) is the combustion pressure cooker, (7) is the stirring blade, (8) is the 1 combustion chamber, (9) is the blower, 00) is the second combustion chamber, (11) is the burner,
(12) is the bu 1 core, (■3) is the container that discharges the raw material in the combustion pressurized pot (6), (14) is its opening/closing damper, (15) is the stirring chamber, (16) is its stirring blade, (1
7) is dry distillation oil extraction equipment, (18) is dry distillation oil tank, (1
9) is a cooling water pipe, 20) is a water reservoir, (21) is a dust collector, and (22) is an ash removal container.
また前記攪拌室（１５）によって攪拌された原料はコン
ヘア（３０）上に排出され、同コンベア」二に設置され
た低圧ローラ（３１） 、加圧ローラ（３２）、カッタ
ー（３３）によって一定寸法の固形燃料が製造され、製
品へケソ） （３４）内に排出される。低圧ローラ（３
１）は１′］１密度の排出原料を予め所定の密度まで圧
縮して次の加圧ローラ（３２）による加圧製品の密度の
安定化を図るものである。低圧ローラ（３１）及び加圧
１コーラ（３２）の下側には、それぞれハックアップロ
ーラ（３５） 、（３６）を設置して、加圧時にコンヘ
ア（３０）に無理な力が加わらないようにする。また、
カッター（３３）の下側にも受けローラ（３７）を設り
てりＪ断時のコンヘア」二の材料がカッター刃によって
正６′１Ｆに切断されるようにする。The raw material stirred by the stirring chamber (15) is discharged onto the conveyor (30), and is moved to a certain size by a low pressure roller (31), a pressure roller (32), and a cutter (33) installed on the same conveyor. of solid fuel is produced and discharged into the product (34). Low pressure roller (3
1) is intended to stabilize the density of the pressurized product by compressing the discharged raw material having a density of 1']1 to a predetermined density in advance by the pressurizing roller (32). Hack-up rollers (35) and (36) are installed under the low pressure roller (31) and pressure 1 cola (32), respectively, to prevent excessive force from being applied to the con hair (30) during pressurization. Make it. Also,
A receiving roller (37) is also provided on the lower side of the cutter (33) so that the cutter blade cuts the material in the shape of 6'1F when J is cut.
第３図はコンベア（３０）部の平面図であり、（３８）
及び（３９）はコンヘア駆動用モータ、（４０）は低圧
ローラ駆動用モータ、（４１）は加圧ローラ（３２）と
カッター（３３）とを同期的に駆動するモータ、 （４
２）は操作盤である。FIG. 3 is a plan view of the conveyor (30) section, and (38)
and (39) is a motor for driving the conhair, (40) is a motor for driving a low-pressure roller, and (41) is a motor for synchronously driving the pressure roller (32) and cutter (33).
2) is the operation panel.
第４図及び第５図はそれぞれ第３図の１−１線及びｕ−
ｎ線より見た加圧ローラ（３２）部の拡大図であり、こ
れらの図に示されているように、コンヘア（３０）は一
定ピンチのセグメン１−よりなり、その断面（第５図参
照）は成形品の幅に等しい幅の溝か形成され、加圧ロー
ラ（３２）もその溝に嵌入する幅のローラ径を有したも
のが溝の数と等しく一定間隔で配置されている。なお、
第４図における（４３）は、加工製品Ａが加圧しＪ−ラ
（３２）に付着した場合に同ローラより剥離する押え板
である。Figures 4 and 5 are the 1-1 line and u- line of Figure 3, respectively.
This is an enlarged view of the pressure roller (32) section seen from the n-line.As shown in these figures, the con hair (30) is made up of segment 1- with a constant pinch, and its cross section (see Figure 5). ) are formed with grooves having a width equal to the width of the molded product, and pressure rollers (32) having a roller diameter wide enough to fit into the grooves are arranged at constant intervals equal to the number of grooves. In addition,
(43) in FIG. 4 is a presser plate that is peeled off from the J-ra (32) when the processed product A is pressurized and adheres to the J-ra (32).
加圧ローラ（３２）によって一定幅に加圧された原料は
、次のカッター（３３） ４こよる切断により、一定寸
法の製品となる。The raw material, which has been pressed to a certain width by the pressure roller (32), is then cut by four cutters (33) into products of a certain size.
上述したように、本発明によれば、廃棄物として大量に
存在しかつ次々と発生する材料を再生して、取り扱い易
い一定寸法の燃料を製造でき、省資源及び無公害のエネ
ルギー源として活用できるという効果を奏するものであ
る。As described above, according to the present invention, materials that exist in large quantities and are generated one after another as waste can be recycled to produce fuel of a certain size that is easy to handle, and can be used as a resource-saving and pollution-free energy source. This effect is achieved.
第１図は本発明に係る固定燃料の製造方法のフ１コーチ
ヤード、第２図はその製造設備の構成を示す系統図、第
３図は固形燃料を定形に成形する設備の平面図、第４図
及び第５図はそれぞれ第３図のＩ−Ｉ線及びＩＩ −Ｉ
Ｉ線にお１ノる拡大矢視図である。
（１）ニブラスチック系原料タンク
（２）：木質系原料タンク
（３）：廃タイヤ系原料タンク
（４）：搬送コンヘア
（５）：結合相投入シュー１−
（６）：燃焼加圧釜
＋７１ ： ｌ’＆拌羽根
（８）：第１燃焼室
（９）：フロアー
００）：第２燃焼室
（］ｌ） ：バーナー
（１２） ニブロアー
（１３） ：コンヘア
（１４） ：開閉クンパー
（１５） ：攪拌室
（１６） ：攪（１ぜ羽根
（１７） ：乾溜浦採油装置
（１８） ：乾溜曲タンク
（１９） ：冷却水パイプ
（２０） ：水溜
（２］、） ：集塵機
（２２） ：灰出し容器
（３０） ：コンヘア
（３１） ：低圧ローラ
（３２） ：加圧ローラ
（３３） ：カソター
（３４） ：製品へケソ１〜
（３５） 、（３６） ：ハソクアソプローラ（３７）
：受すローラ
（３日）〜（旧）：駆動モータ
（４２） ：操作盤
（４３） ：押え板
特許出願人 春 永 験 朗
代理人 手掘 益（はが２名）Fig. 1 is a front yard of the fixed fuel production method according to the present invention, Fig. 2 is a system diagram showing the configuration of the production equipment, Fig. 3 is a plan view of the equipment for forming solid fuel into a regular shape, Figures 4 and 5 are line I-I and II-I in Figure 3, respectively.
It is an enlarged view taken along the I line. (1) Niblast raw material tank (2): Wood raw material tank (3): Waste tire raw material tank (4): Conveyor container (5): Binding phase input shoe 1- (6): Combustion pressure cooker +71: l'& stirring blade (8): 1st combustion chamber (9): Floor 00): 2nd combustion chamber (]l): Burner (12) Ni blower (13): Conhair (14): Opening/closing kumper (15): Stirring chamber (16) : Stirring (1 blade (17) : Dry distillation port oil extraction device (18) : Dry distillation bend tank (19) : Cooling water pipe (20) : Water reservoir (2) : Dust collector (22) : Ash Dispensing container (30): Conhair (31): Low pressure roller (32): Pressure roller (33): Cassotor (34): To the product 1~ (35), (36): Hasoku Asopro roller (37)
: Receiving roller (3 days) - (old) : Drive motor (42) : Operation panel (43) : Presser plate Patent applicant Kenro Harunaga Agent Masu Tegori (2 people)
Claims (1)
３５重量部、合成樹脂廃材粉粒２０〜３０重量部を含有
し、これらを樹脂系結合剤及び樹脂系硬化剤で固化して
なる固形燃料。 ２、木質系有機物粉粒及び廃タイヤ、廃棄合成樹脂粉粒
を第１燃焼釜に投入し、同第１燃焼釜内において前記粉
粒を攪拌した後、２気圧程度の加圧雰囲気中で２１５〜
２５０°Ｃに加熱し、材料が褐色になったときに材料を
第２燃焼釜に移動し、同第２燃焼釜内で１４０〜１８０
℃の加熱下で攪拌しながら樹脂系結合材及び樹脂系硬化
材を投入し、攪拌機から取り出して所定の形状に成形す
ることを特徴とする固形燃料の製造方法。 ３、原料を粉砕して粉粒にする粉砕装置と、同粉粒を加
熱加圧及びＩＷ拌する第１燃焼釜と、第１燃焼釜から取
り出した材料を加熱攪拌する第２燃焼釜と、同第２燃焼
釜から取り出した材料を成形する成形機とを備えた固形
燃料の製造装置。[Claims] 1. 40 to 50 parts by weight of wood powder, 25 to 50 parts by weight of waste tire powder
A solid fuel containing 35 parts by weight and 20 to 30 parts by weight of synthetic resin waste powder particles, which are solidified with a resin binder and a resin curing agent. 2. Put the wood-based organic powder, waste tires, and waste synthetic resin powder into the first combustion pot, stir the powder in the first combustion pot, and then heat the powder at 215 °C in a pressurized atmosphere of about 2 atmospheres. ~
Heat to 250°C, and when the material turns brown, move the material to the second combustion pot, and heat it to 140-180℃ in the second combustion pot.
A method for producing a solid fuel, which comprises adding a resin binder and a resin hardening material while stirring under heating at a temperature of 0.degree. 3. A pulverizer that crushes raw materials into powder, a first combustion pot that heats, pressurizes, and stirs the powder by IW; a second combustion pot that heats and stirs the material taken out from the first combustion pot; A solid fuel production device comprising a molding machine that molds the material taken out from the second combustion pot.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23192483A JPS60123594A (en) | 1983-12-07 | 1983-12-07 | Solid fuel, its manufacture and manufacturing unit for the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23192483A JPS60123594A (en) | 1983-12-07 | 1983-12-07 | Solid fuel, its manufacture and manufacturing unit for the same |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS60123594A true JPS60123594A (en) | 1985-07-02 |
Family
ID=16931193
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP23192483A Pending JPS60123594A (en) | 1983-12-07 | 1983-12-07 | Solid fuel, its manufacture and manufacturing unit for the same |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60123594A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2364325A (en) * | 2000-04-03 | 2002-01-23 | World Rubber Ltd | Calorific enhancer |
| RU2608733C1 (en) * | 2015-11-10 | 2017-01-23 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Кузбасский государственный технический университет имени Т.Ф. Горбачева" (КузГТУ) | Fuel briquette based on carbon residue of pyrolysis of tires |
| RU2664330C1 (en) * | 2018-04-05 | 2018-08-16 | федеральное государственное бюджетное образовательное учреждение высшего образования "Кузбасский государственный технический университет имени Т.Ф. Горбачева" (КузГТУ) | Composite fuel |
| CN113372974A (en) * | 2021-06-16 | 2021-09-10 | 扬州市职业大学(扬州市广播电视大学) | Green and environment-friendly new energy material and preparation method thereof |
| JP2023046445A (en) * | 2021-09-24 | 2023-04-05 | 株式会社トリウミ | Manufacturing method of waste tire-containing solid fuel |
-
1983
- 1983-12-07 JP JP23192483A patent/JPS60123594A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2364325A (en) * | 2000-04-03 | 2002-01-23 | World Rubber Ltd | Calorific enhancer |
| RU2608733C1 (en) * | 2015-11-10 | 2017-01-23 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Кузбасский государственный технический университет имени Т.Ф. Горбачева" (КузГТУ) | Fuel briquette based on carbon residue of pyrolysis of tires |
| RU2664330C1 (en) * | 2018-04-05 | 2018-08-16 | федеральное государственное бюджетное образовательное учреждение высшего образования "Кузбасский государственный технический университет имени Т.Ф. Горбачева" (КузГТУ) | Composite fuel |
| CN113372974A (en) * | 2021-06-16 | 2021-09-10 | 扬州市职业大学(扬州市广播电视大学) | Green and environment-friendly new energy material and preparation method thereof |
| 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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