JPH0237398B2 - FUKUGOKOKEINENRYONOSEIZOHOHO - Google Patents
FUKUGOKOKEINENRYONOSEIZOHOHOInfo
- Publication number
- JPH0237398B2 JPH0237398B2 JP3621582A JP3621582A JPH0237398B2 JP H0237398 B2 JPH0237398 B2 JP H0237398B2 JP 3621582 A JP3621582 A JP 3621582A JP 3621582 A JP3621582 A JP 3621582A JP H0237398 B2 JPH0237398 B2 JP H0237398B2
- Authority
- JP
- Japan
- Prior art keywords
- thermoplastic synthetic
- paper
- waste
- synthetic resin
- citrus processing
- 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.)
- Expired - Lifetime
Links
- 239000002699 waste material Substances 0.000 claims description 18
- 241000207199 Citrus Species 0.000 claims description 15
- 235000020971 citrus fruits Nutrition 0.000 claims description 15
- 229920003002 synthetic resin Polymers 0.000 claims description 15
- 239000000057 synthetic resin Substances 0.000 claims description 15
- 229920001169 thermoplastic Polymers 0.000 claims description 14
- 239000004416 thermosoftening plastic Substances 0.000 claims description 14
- 238000010411 cooking Methods 0.000 claims description 12
- 239000004449 solid propellant Substances 0.000 claims description 11
- 239000001913 cellulose Substances 0.000 claims description 5
- 229920002678 cellulose Polymers 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 239000010893 paper waste Substances 0.000 claims description 5
- 239000002131 composite material Substances 0.000 claims description 4
- 239000008187 granular material Substances 0.000 claims description 3
- 238000000465 moulding Methods 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 claims 1
- 238000004898 kneading Methods 0.000 claims 1
- 238000002485 combustion reaction Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- -1 polyethylene Polymers 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 2
- 238000000748 compression moulding Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000001247 metal acetylides Chemical class 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 230000002459 sustained effect Effects 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
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
Landscapes
- Solid Fuels And Fuel-Associated Substances (AREA)
Description
製紙工業においては、回収古紙を蒸解、解砕
し、セルロースを過して再び紙の原料として利
用している。前記の回収古紙にはポリエチレンフ
イルム等の熱可塑性合成樹脂がかなり含まれてい
るが、これらは過器で捕集され、廃棄されるべ
き蒸解残渣中でかなりの部分(通常ドライベース
で50〜60%程度)を占めて排出されてくる。これ
らの廃棄物は直接埋立てに使用したり、燃焼させ
て熱エネルギとして利用した後処分されている。
一方、かんきつ類の加工業界では、果皮やしぼ
り粕等(本明細書中でかんきつ類加工廃棄物と称
する)が多量に副生してくるが、これらのかんき
つ類加工廃棄物は一部は肥料あるいは飼料の一部
として利用されているものの、大部分は無用なも
のとして放置されている。最近、こられ廃棄物を
脱水乾燥して、そのままあるいは造粒して燃料と
して利用することも試みられているが、発熱量が
3880kcal/Kg程度でエネルギ源としては著しく低
品位なため、その利用価値はほとんどない。
この発明は、上述した製紙工業の古紙蒸解工程
において排出される熱可塑性合成樹脂含有の残渣
とかんきつ類加工廃棄物とを利用して高品質の複
合固形燃料を得ることを目的として提案されたも
のである。
製紙工業において回収古紙よりセルロースを分
離した際に発生する蒸解残渣には、ポリエチレ
ン、ポリプロピレンその他のポリオレフイン系合
成樹脂がドライベースで50〜60%程度含まれてい
ることが多く、本発明では、燃焼させても毒性ガ
スの発生しない蒸解残渣中の熱可塑性合成樹脂分
を有効に利用するものである。また、第2の原料
としてはかんきつ類の加工業界で排出される果皮
やしぼり粕等(かもきつ類加工廃棄物)が用いら
れる。
本発明においては、前記の蒸解残渣及びかんき
つ類加工廃棄物を必要に応じて含有水分が20%以
下となるように脱水又は乾燥させた後、粒子径が
数mm以下となるように粉砕し、後述する製品固形
燃料中の熱可塑性合成樹脂の含有率がドライベー
スで20〜70重量%となるように混合する。そして
更にその混合物を100〜300℃で加熱半溶融化して
混練した後、混入熱可塑性合成樹脂の粘着性を利
して押出式圧縮成形機、双輪式圧縮成形機その他
の成形装置により圧縮力50Kg/cm2程度以上の加圧
力で大きさ5mm以上100mm以下の粒状体ないし塊
状体に成形し製品の固形燃料を得る。熱可塑性合
成樹脂含有の蒸解残渣とかんきつ類加工廃棄物と
の混合比は、サンプリングにより予備的試験を行
い、製品固形燃料中の熱可塑性合成樹脂の含有率
がドライベースで20〜70重量%の範囲に納まるよ
うに決定するものである。
上記した複合固形燃料の製造方法において、か
んきつ類加工廃棄物の一部を他の可燃性物質で置
き換えることもできる。その可燃性物質として
は、木片、バーク、稲わら等別の繊維質廃棄物、
それらの炭化物あるいは鉱物質炭素粉等が挙げら
れる。
次に、本願の発明者等が行つた試験結果を示
す。第1表は、熱可塑性合成樹脂含有の蒸解残渣
とかんきつ類加工廃棄物との配合比を変えて固形
燃料とした場合の実験結果であり、第2表は、蒸
解残渣、かんきつ類加工廃棄物及び繊維質廃棄物
の配合比を変えて固形燃料とした場合の実験結果
である(但し、かんきつ類加工廃棄物と繊維質廃
棄物とは同量とした)。
In the paper industry, recovered waste paper is digested and crushed to remove cellulose and used again as a raw material for paper. The recovered waste paper mentioned above contains a considerable amount of thermoplastic synthetic resin such as polyethylene film, and these are collected in a filtration unit and a considerable portion (usually 50 to 60% on a dry basis) of the cooking residue to be disposed of. %) is emitted. These wastes are either used directly in landfills or burned for thermal energy and then disposed of. On the other hand, in the citrus processing industry, a large amount of pericarp, pomace, etc. (herein referred to as citrus processing waste) is produced as a by-product, and some of these citrus processing wastes are used as fertilizer or feed. Although some of it is used, most of it is left unused. Recently, attempts have been made to dehydrate and dry this waste and use it as fuel as it is or after granulating it, but the calorific value is low.
As it is extremely low-grade as an energy source at around 3880kcal/Kg, it has almost no value in use. This invention was proposed for the purpose of obtaining a high-quality composite solid fuel by using the thermoplastic synthetic resin-containing residue and citrus processing waste discharged in the waste paper digestion process of the paper industry mentioned above. be. The cooking residue generated when cellulose is separated from recovered paper in the paper manufacturing industry often contains about 50 to 60% polyethylene, polypropylene, and other polyolefin synthetic resins on a dry basis. This makes effective use of the thermoplastic synthetic resin content in the cooking residue, which does not generate toxic gas even if the cooking residue is heated. Further, as the second raw material, pericarp, squeezed lees, etc. (citrus processing waste) discharged in the citrus processing industry are used. In the present invention, the above-mentioned cooking residue and citrus processing waste are dehydrated or dried as necessary so that the water content is 20% or less, and then pulverized to a particle size of several mm or less. The content of thermoplastic synthetic resin in the product solid fuel is 20 to 70% by weight on a dry basis. Then, the mixture is heated at 100 to 300°C to semi-melt it and kneaded, and then compressed with a compression force of 50 kg using an extrusion compression molding machine, a twin-wheel compression molding machine, or other molding equipment, taking advantage of the tackiness of the mixed thermoplastic synthetic resin. A solid fuel product is obtained by molding into granules or lumps with a size of 5 mm or more and 100 mm or less using a pressure of about /cm 2 or more. The mixing ratio of cooking residue containing thermoplastic synthetic resin and citrus processing waste was determined through preliminary testing through sampling, and the content of thermoplastic synthetic resin in the product solid fuel was in the range of 20 to 70% by weight on a dry basis. It is determined so that it fits within the following. In the method for producing the composite solid fuel described above, a part of the citrus processing waste can also be replaced with other combustible substances. The combustible materials include wood chips, bark, other fibrous waste such as rice straw,
Examples include carbides thereof and mineral carbon powder. Next, the results of tests conducted by the inventors of the present application will be shown. Table 1 shows the experimental results when solid fuel was produced by changing the mixing ratio of cooking residue containing thermoplastic synthetic resin and citrus processing waste, and Table 2 shows the results of experiments using cooking residue, citrus processing waste, and fibers. These are the results of an experiment in which solid fuel was produced by changing the blending ratio of quality waste (however, the amounts of citrus processing waste and fibrous waste were the same).
【表】【table】
【表】
この発明の複合固形燃料の製造方法は、単独で
は燃料としては利用が困難な産業廃棄物すなわ
ち、回収古紙のセルロース過分離後の熱可塑性
合成樹脂含有蒸解残渣並びにかんきつ類加工廃棄
物を有効に利用するものであり、また、その方法
によつて製造された固形燃料は、一旦溶融させた
蒸解残渣中の熱可塑性合成樹脂で他の原料粒子の
表面を被覆し多数の粒子を強固に結合して成り、
第1表及び第2表に示すように、吸水率が低く、
強度的にも優れているので、屋外における長期保
存も可能であるなどの利点がある。更に、その固
形燃料は、燃焼過程において崩壊することが少な
く、適度の発熱量を持つ他、高い熱負荷特性を呈
しつつ持続した燃焼を可能にするので、各種の燃
焼装置に対し広範な利用が計れ、良質の燃料とし
て使用できるものである。[Table] The method for producing a composite solid fuel of the present invention effectively uses industrial waste that is difficult to use as fuel alone, such as cooking residue containing thermoplastic synthetic resin after cellulose over-separation of recovered waste paper and citrus processing waste. In addition, the solid fuel produced by this method coats the surface of other raw material particles with the thermoplastic synthetic resin in the melted cooking residue to firmly bond many particles. And so,
As shown in Tables 1 and 2, the water absorption rate is low;
Since it has excellent strength, it has the advantage of being able to be stored outdoors for a long time. Furthermore, the solid fuel is less likely to disintegrate during the combustion process, has an appropriate calorific value, and exhibits high heat load characteristics while enabling sustained combustion, making it widely applicable to various combustion devices. It can be measured and used as a high quality fuel.
Claims (1)
分離した際に発生する熱可塑性合成樹脂含有の蒸
解残渣にかんきつ類加工廃棄物を製品中の熱可塑
性合成樹脂の含有率が20〜70重量%となるように
混合し、それを100〜300℃で加熱半溶融化して混
練した後、大きさ5mm以上の粒状体ないし塊状体
に加圧成形したことを特徴とする複合固形燃料の
製造方法。 2 製紙工業において回収古紙よりセルロースを
分離した際に発生する熱可塑性合成樹脂含有の蒸
解残渣にかんきつ類加工廃棄物及びその他の可燃
性物質を製品中の熱可塑性合成樹脂の含有率が20
〜70重量%となるように混合し、それを100〜300
℃で加熱半溶融化して混練した後、大きさ5mm以
上の粒状体ないし塊状体に加圧成形したことを特
徴とする複合固形燃料の製造方法。[Claims] 1. Citrus processing waste is added to the cooking residue containing thermoplastic synthetic resin generated when cellulose is separated from recovered waste paper in the paper manufacturing industry.The content of thermoplastic synthetic resin in the product is 20 to 70% by weight. %, heated at 100 to 300°C to semi-melt, kneaded, and then pressure-molded into granules or lumps with a size of 5 mm or more. . 2. Citrus processing waste and other flammable substances are added to the cooking residue containing thermoplastic synthetic resins generated when cellulose is separated from recovered paper in the paper industry.The content of thermoplastic synthetic resins in the product is 20%.
Mix it so that it is ~70% by weight and then add it to 100~300
1. A method for producing a composite solid fuel, which comprises heating to semi-melt it at °C, kneading it, and then press-molding it into granules or lumps with a size of 5 mm or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3621582A JPH0237398B2 (en) | 1982-03-08 | 1982-03-08 | FUKUGOKOKEINENRYONOSEIZOHOHO |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3621582A JPH0237398B2 (en) | 1982-03-08 | 1982-03-08 | FUKUGOKOKEINENRYONOSEIZOHOHO |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58152094A JPS58152094A (en) | 1983-09-09 |
| JPH0237398B2 true JPH0237398B2 (en) | 1990-08-23 |
Family
ID=12463531
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3621582A Expired - Lifetime JPH0237398B2 (en) | 1982-03-08 | 1982-03-08 | FUKUGOKOKEINENRYONOSEIZOHOHO |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0237398B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4536744B2 (en) * | 2007-01-16 | 2010-09-01 | 株式会社御池鐵工所 | Solid fuel using organic waste and method for producing the same |
-
1982
- 1982-03-08 JP JP3621582A patent/JPH0237398B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58152094A (en) | 1983-09-09 |
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