JPS6241640B2 - - Google Patents
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- Publication number
- JPS6241640B2 JPS6241640B2 JP16585181A JP16585181A JPS6241640B2 JP S6241640 B2 JPS6241640 B2 JP S6241640B2 JP 16585181 A JP16585181 A JP 16585181A JP 16585181 A JP16585181 A JP 16585181A JP S6241640 B2 JPS6241640 B2 JP S6241640B2
- Authority
- JP
- Japan
- Prior art keywords
- fuel
- viscosity
- biomass
- mixture
- weight
- 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
Links
- 239000000446 fuel Substances 0.000 claims description 42
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 32
- 239000012530 fluid Substances 0.000 claims description 22
- 239000003610 charcoal Substances 0.000 claims description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 239000000203 mixture Substances 0.000 claims description 14
- 239000003921 oil Substances 0.000 claims description 11
- 239000002131 composite material Substances 0.000 claims description 9
- 239000004094 surface-active agent Substances 0.000 claims description 8
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 claims description 7
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 claims description 7
- KHPCPRHQVVSZAH-UHFFFAOYSA-N trans-cinnamyl beta-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OCC=CC1=CC=CC=C1 KHPCPRHQVVSZAH-UHFFFAOYSA-N 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 230000007935 neutral effect Effects 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 4
- 239000003349 gelling agent Substances 0.000 claims description 3
- 235000013311 vegetables Nutrition 0.000 claims description 3
- 239000012752 auxiliary agent Substances 0.000 claims description 2
- 239000002028 Biomass Substances 0.000 description 28
- 235000019441 ethanol Nutrition 0.000 description 22
- 239000002023 wood Substances 0.000 description 13
- 239000003350 kerosene Substances 0.000 description 7
- 239000007864 aqueous solution Substances 0.000 description 6
- 239000006185 dispersion Substances 0.000 description 6
- 150000001450 anions Chemical class 0.000 description 5
- 239000000295 fuel oil Substances 0.000 description 5
- 238000002360 preparation method Methods 0.000 description 5
- 239000003381 stabilizer Substances 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 241000047703 Nonion Species 0.000 description 4
- 239000003245 coal Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 229920001223 polyethylene glycol Polymers 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 235000008331 Pinus X rigitaeda Nutrition 0.000 description 3
- 235000011613 Pinus brutia Nutrition 0.000 description 3
- 241000018646 Pinus brutia Species 0.000 description 3
- 229920002472 Starch Polymers 0.000 description 3
- 238000010000 carbonizing Methods 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 3
- 229920005610 lignin Polymers 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 239000004570 mortar (masonry) Substances 0.000 description 3
- 239000010893 paper waste Substances 0.000 description 3
- 239000011297 pine tar Substances 0.000 description 3
- 229940068124 pine tar Drugs 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 235000019698 starch Nutrition 0.000 description 3
- 239000008107 starch Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- IXPNQXFRVYWDDI-UHFFFAOYSA-N 1-methyl-2,4-dioxo-1,3-diazinane-5-carboximidamide Chemical compound CN1CC(C(N)=N)C(=O)NC1=O IXPNQXFRVYWDDI-UHFFFAOYSA-N 0.000 description 2
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- 229920002488 Hemicellulose Polymers 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- 239000004372 Polyvinyl alcohol Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000003763 carbonization Methods 0.000 description 2
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 2
- 235000014113 dietary fatty acids Nutrition 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 239000000194 fatty acid Substances 0.000 description 2
- 229930195729 fatty acid Natural products 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- 239000002803 fossil fuel Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- 238000009775 high-speed stirring Methods 0.000 description 2
- 239000010903 husk Substances 0.000 description 2
- 235000013379 molasses Nutrition 0.000 description 2
- 125000004430 oxygen atom Chemical group O* 0.000 description 2
- 229920002451 polyvinyl alcohol Polymers 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- 239000000661 sodium alginate Substances 0.000 description 2
- 235000010413 sodium alginate Nutrition 0.000 description 2
- 229940005550 sodium alginate Drugs 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000004711 α-olefin Substances 0.000 description 2
- 244000215068 Acacia senegal Species 0.000 description 1
- 241001474374 Blennius Species 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 229920002907 Guar gum Polymers 0.000 description 1
- 229920000084 Gum arabic Polymers 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 240000000111 Saccharum officinarum Species 0.000 description 1
- 235000007201 Saccharum officinarum Nutrition 0.000 description 1
- 239000000205 acacia gum Substances 0.000 description 1
- 235000010489 acacia gum Nutrition 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000002154 agricultural waste Substances 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000004996 alkyl benzenes Chemical class 0.000 description 1
- 230000004071 biological effect Effects 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 239000005539 carbonized material Substances 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 229920006184 cellulose methylcellulose Polymers 0.000 description 1
- 238000001246 colloidal dispersion Methods 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000000665 guar gum Substances 0.000 description 1
- 235000010417 guar gum Nutrition 0.000 description 1
- 229960002154 guar gum Drugs 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000012552 review Methods 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 229920001059 synthetic polymer Polymers 0.000 description 1
Landscapes
- Liquid Carbonaceous Fuels (AREA)
Description
本発明は、木質バイオマス、草本バイオマスよ
り得られた炭化物と油類と松やにを10%前後含ん
だアルコールとから成る複合流体燃料及びその製
造方法に関するものである。
現在近代化された生活において、家庭用燃料に
はほとんど6500kcal/Kg以上のガス化燃料又は液
体燃料が用いられ、又各種産業用ボイラー燃料或
いは農業用燃料も、使用しやすい高発熱量である
液体燃料(重油や灯油)が使用されている。しか
るに最近化石燃料特に油が不足し、その高騰から
脱石油が強く叫ばれている。
バイオマスから直接燃料ということで、薪、或
いは加工されたオガライト、ウデツクス等が生産
され使用されている。元来、木質を中心とした草
本バイオマスはそのままの状態では不定形な固相
で多量の水分を含んでおり、見掛のかさ比重も小
さく、構成成分には酸素原子を多く含んでいるの
でその絶対発熱量が低く、このままでは燃料とし
ての用途の範囲はせまい。
また輸送上の問題となる見掛比重は石油で
0.8、石炭では0.7、程度の値に対して、木質バイ
オマス、草本バイオマスでは0.1と極端に小さく
なることや、燃焼熱が低いこと、輸送コストの面
で不利であることなど、他の燃料と比較してマイ
ナスの点が多い。そこでそれらの欠点、問題点を
解決し国民の生活様式に合せた普遍性のある複合
流体燃料の開発が従来より熱望されていた。
本発明は上記の現況に鑑み、木質系バイオマ
ス、草木系バイオマスより得られた炭化物の流体
複合燃料化により、これらの要求に適合した燃料
およびその製造方法を提供することを第1の目的
とする。
最近バイオマスという言葉がよく使用されるが
バイオマスを定義すれば、量的規模で集積され、
エネルギー、食料、工業原料の資源となる生物体
もしくは生物活動に付随して生成される物体とい
うことになる。バイオマスは陸域バイオマスと水
域バイオマスに大別される。陸域バイオマスとし
ては、澱粉質バイオマス、糖質バイオマス、
木質バイオマス、草本系バイオマス、炭化
水素系バイオマス、廃棄物系バイオマスに分け
ることができる。雑誌「木材工業」1981(S.56
年)5月号P.10〜16には、このうち,を原料
とした複合流体燃料の総説が掲載されている。
本発明は木質系バイオマスと草本系バイオ
マスの炭化物を原料とし、使用しやすい流体燃料
を提供することを第2の目的としたものである。
木質エネルギーの消費は昭和30年代までは総エ
ネルギー消費量の8%を占め、どこの家庭にも木
炭の1俵や2俵はころがつていたものである。経
済成長による庶民の生活変化により家庭エネルギ
ーは電気、ガス、石油に変化し、薪炭は庶民家庭
から消え去つてしまつた。過疎地帯の山村農家ま
で電力、化石燃料に変つてしまつたが、石油危機
の叫ばれるこのごろ、再び木質エネルギー見直し
論まで現れても不思議ではない。しかし、木質エ
ネルギーが庶民家庭に復活するためにはその利用
について新らたな進歩が必要である。
そこで発明者は使用し易い流体燃料化の研究を
行つた結果、粉状炭化物と油類とアルコールの三
者が安定なコロイダル状を呈する流体燃料とその
製造方法を見出したものである。木質及び草本系
バイオマスの炭化は燃焼につぐ、容易な木質エネ
ルギー化の方法で、古来より広く一般に行われて
きた。木炭は薪よりも発熱量が大きい。乾燥した
薪は4500kcal/Kgだが木炭は平均7000kcal/Kgで
薪と異なり無焔性である。木材は加熱すると分解
してガス状の物質と木炭になる。この現象を木材
の熱分解という。
木炭はリグニン炭とホロセルロース炭と両者の
性質をもつている。木材を加熱すると水分が蒸発
し、ヘミセルロースとリグニンの一部が分解をは
じめる。この温度は140℃くらいである。次にヘ
ミセルロースがはげしく分解をはじめ、298℃に
なるとセルロースがはげしく分解して発熱する。
最後にリグニンの残りが分解して木炭が残るが、
この温度は約450℃である。
本発明は前述したごとく、木炭は薪の如く分子
構造中に酸素原子を含んでいないのでその発熱量
が高いことと、その微粉化が木質に比較して容易
であることを考慮し、前記種々の目的を達成する
ためこの粉末木炭に油類と松やにを10%添加した
アルコールを添加し、乳鉢の中で混合混練して木
炭を均一な微粉とし、これを安定なコロイダル状
流体燃料とするために水溶性界面活性剤を0.5〜
1.5%、添加剤として植物性ゲル化剤又は合成高
分子水溶液を全重量に対して0.06〜0.5%それぞ
れ添加し、粘度の調整と分散安定化保持のために
燃料全重量に対して水分量を10〜25%に調整し粘
度を250〜5000cpとするように構成したものであ
る。
本発明に使用する炭化物は木質バイオマス炭化
物、草本バイオマス炭化物(例えばモミガラ炭化
物、サトウキビ炭化物等を指す)、故紙等の炭化
物である。
アルコールは、エチルアルコール、メチルアル
コール何れでもよいがこのアルコールに松やにを
10%添加すると松やにはアルコール中によく溶解
する。
界面活性剤としては中性、水溶液型のものを使
用する。一般に使用できるものは
α―オレフイン系(陰イオン)、高級アルコール
系(陰イオン)脂肪酸系(非イオン)、高級アル
コール系(非イオン)の混合されたものから、そ
の一部を除いたものが使用できる。例えば簡単な
界面活性剤としては直鎖アルキルベンゼン系と高
級アルコール系(陰イオン)混合物を分散剤とし
て使用することができる。
中性界面活性剤の添加量は全重量に対して最低
1.5%を要する。なお上限は1.5%でそれ以上は効
果として同一である。
助剤としては植物性高粘稠物質例えばアルギン
酸ソーダ、CMC、澱粉のり、糖蜜、グアーガ
ム、アラビヤゴム、海藻をすりつぶした粘稠液等
の水溶液がよい。これら植物性高粘稠物にPEG
(ポリエチレングリコール)とはPVA(ポリビニ
ールアルコール)等を50%添加した混合物で、こ
れ等は全重量に対して0.06〜0.5%で、250〜
5000cpの範囲に調整するものである。
又、水分の含有量を5〜20%とする。前述の通
りコロイダル状に分散させるためと、粘度の調整
のためであり、又この範囲において流体燃料の燃
焼性が良好であることよるものである。
本発明のコロイダル状混合物を得る撹拌は、高
速撹拌機か、または乳鉢状すりつぶし方式がよ
い。いずれも粉炭は爆発するおそれがあるので温
式法によるものである。
第1〜3表は代表的な実験例の結果を示し、第
1表は木炭、松やに10%含有エチルアルコール、
灯油複合燃料の熱量測定結果である。また第2表
は木炭、松やに10%添加エチルアルコール
(EA)の重量組成別にそれぞれ灯油を添加したと
きの熱量測定結果である。さらに第3表は木炭、
松やに10%添加エチルアルコール、灯油・水系複
合燃料の含水量(MC)変化に対する発熱量の測
定結果である。
The present invention relates to a composite fluid fuel comprising charcoal obtained from woody biomass and herbaceous biomass, oils, and alcohol containing about 10% pine resin, and a method for producing the same. In today's modernized lifestyle, most household fuels use gasified fuels or liquid fuels with a value of 6,500 kcal/Kg or more, and various industrial boiler fuels and agricultural fuels are also easily used liquid fuels with a high calorific value. Fuel (heavy oil or kerosene) is used. However, recently there has been a shortage of fossil fuels, especially oil, and the soaring prices have led to strong calls for a move away from oil. Fuels such as firewood, processed ogalite, and wood are produced and used directly from biomass. Originally, herbaceous biomass, mainly wood, is an amorphous solid phase that contains a large amount of water in its original state, has a small apparent bulk specific gravity, and contains many oxygen atoms in its constituent components. Its absolute calorific value is low, so its range of uses as a fuel is limited. Also, the apparent specific gravity, which is a problem in transportation, is
Compared to other fuels, woody biomass and herbaceous biomass have an extremely small value of 0.8, 0.7 for coal, and 0.1 for woody biomass, low heat of combustion, and disadvantages in terms of transportation costs. There are many negative points. Therefore, there has been a desire for the development of a universal composite fluid fuel that solves these drawbacks and problems and is compatible with people's lifestyles. In view of the above-mentioned current situation, the first object of the present invention is to provide a fuel that meets these requirements and a method for producing the same by converting charcoal obtained from woody biomass and plant biomass into a fluid composite fuel. . The word biomass is often used these days, but if we define biomass, it means that it is accumulated on a quantitative scale,
It refers to living organisms that serve as resources for energy, food, and industrial raw materials, or objects that are generated as a result of biological activities. Biomass is broadly divided into terrestrial biomass and aquatic biomass. Terrestrial biomass includes starchy biomass, carbohydrate biomass,
It can be divided into wood biomass, herbaceous biomass, hydrocarbon biomass, and waste biomass. Magazine "Wood Industry" 1981 (S.56
A review of composite fluid fuels made from these materials is published on pages 10 to 16 of the May issue. A second object of the present invention is to provide an easy-to-use fluid fuel that uses charred materials of woody biomass and herbaceous biomass as raw materials. Until the 1950s, wood energy consumption accounted for 8% of total energy consumption, and every household had a bale or two of charcoal lying around. As the lives of ordinary people changed due to economic growth, household energy sources changed to electricity, gas, and oil, and firewood and charcoal disappeared from ordinary households. Even farmers in mountain villages in depopulated areas have turned to electricity and fossil fuels, but with the oil crisis in the air, it would not be surprising to see people reconsidering wood energy. However, new advances in the use of wood energy are needed before it can be brought back into the homes of ordinary people. Therefore, the inventor conducted research on creating a fluid fuel that is easy to use, and as a result, discovered a fluid fuel in which powdered carbide, oil, and alcohol exhibit a stable colloidal state, and a method for producing the fluid fuel. Carbonization of woody and herbaceous biomass is an easy method to convert wood into energy, second only to combustion, and has been widely used since ancient times. Charcoal has a higher calorific value than firewood. Dried firewood has 4500kcal/Kg, but charcoal has an average of 7000kcal/Kg, and unlike firewood, it is flameless. When wood is heated, it decomposes into gaseous substances and charcoal. This phenomenon is called wood pyrolysis. Charcoal has properties of both lignin charcoal and holocellulose charcoal. When wood is heated, water evaporates and some of the hemicellulose and lignin begin to decompose. This temperature is about 140℃. Next, hemicellulose begins to rapidly decompose, and when the temperature reaches 298°C, cellulose rapidly decomposes and generates heat.
Finally, the remaining lignin decomposes, leaving behind charcoal.
This temperature is approximately 450°C. As mentioned above, charcoal does not contain oxygen atoms in its molecular structure like firewood, so it has a high calorific value, and it is easier to pulverize it than wood, and the present invention is based on the above-mentioned various methods. In order to achieve this purpose, we added alcohol containing 10% oil and pine resin to this powdered charcoal, mixed and kneaded it in a mortar to make the charcoal into a uniform fine powder, and made this into a stable colloidal fluid fuel. Add water-soluble surfactant to
1.5%, a vegetable gelling agent or a synthetic polymer aqueous solution is added as an additive at 0.06 to 0.5% of the total weight, and the amount of water is adjusted to the total weight of the fuel to adjust the viscosity and maintain dispersion stability. The viscosity is adjusted to 10 to 25% and the viscosity is 250 to 5000 cp. The carbonized materials used in the present invention include carbonized wood biomass, carbonized herbaceous biomass (for example, carbonized rice husk, carbonized sugarcane, etc.), and waste paper. The alcohol can be either ethyl alcohol or methyl alcohol, but if you add pine tar to this alcohol,
When added at 10%, pine resin dissolves well in alcohol. As the surfactant, a neutral, aqueous type surfactant is used. Generally usable products are mixtures of α-olefin (anion), higher alcohol (anion), fatty acid (non-ion), and higher alcohol (non-ion), with some parts removed. Can be used. For example, as a simple surfactant, a mixture of a linear alkylbenzene and a higher alcohol (anion) can be used as a dispersant. Addition amount of neutral surfactant is minimum based on total weight
Requires 1.5%. The upper limit is 1.5%, and anything above that has the same effect. The auxiliary agent is preferably an aqueous solution of highly viscous vegetable substances such as sodium alginate, CMC, starch paste, molasses, guar gum, gum arabic, or a viscous liquid obtained by grinding seaweed. PEG is added to these plant-based high viscosity substances.
(Polyethylene glycol) is a mixture containing 50% of PVA (polyvinyl alcohol), etc. These are 0.06 to 0.5% of the total weight, and 250 to 250% of the total weight is added.
It is adjusted to a range of 5000 cp. Further, the water content is set to 5 to 20%. As mentioned above, this is for colloidal dispersion and for adjusting viscosity, and also because the combustibility of the fluid fuel is good within this range. Stirring to obtain the colloidal mixture of the present invention is preferably performed using a high-speed stirrer or a mortar-like grinding method. In both cases, a hot method is used since powdered coal may explode. Tables 1 to 3 show the results of typical experimental examples.
This is the calorific value measurement result of kerosene composite fuel. Furthermore, Table 2 shows the calorific value measurement results when kerosene was added to charcoal and 10% ethyl alcohol (EA) added to pine tar, depending on the weight composition. Furthermore, Table 3 shows charcoal,
These are the measurement results of the calorific value of 10% ethyl alcohol added to pine tar, and the change in water content (MC) of kerosene/water-based composite fuel.
【表】【table】
【表】【table】
【表】
次に本発明の実施例をさらに詳細に説明する。
実施例 1
林地内残材を炭化した含水率20%前後の微粉木
炭250gに対して10%のロジンを含むエチルアル
コール(含水率5%)100gと灯油100gを高速撹
拌器に入れて混合撹拌した後、α―オレフイン系
(陰イオン)、高級アルコール系(陰イオン)、高
級アルコール系(非イオン)、脂肪酸系(非イオ
ン)よりなる界面活性剤に水を加えて濃度を35%
に調製処方された中性タイプの分散安定剤15g
(純物5.25g)と、低品質糖蜜(含水率30%)20
gを徐々に添加しながら高速撹拌を続けると、粘
稠な流体燃料が480gが得られた。この流体燃料
の粘度は2300cpで2ケ月後粘度を測定しても変
化がなく安定であつた。
本実施例の仕込量と発熱量を表示すれば第4表
の通りである。[Table] Next, examples of the present invention will be described in more detail. Example 1 100 g of ethyl alcohol (5% water content) containing 10% rosin and 100 g of kerosene were mixed and stirred in a high-speed stirrer against 250 g of finely powdered charcoal with a water content of around 20% obtained by carbonizing forest residue. After that, water was added to the surfactant consisting of α-olefin type (anion), higher alcohol type (anion), higher alcohol type (non-ion), and fatty acid type (non-ion) to make the concentration 35%.
15g of neutral type dispersion stabilizer formulated in
(5.25g pure) and low quality molasses (30% moisture content)20
By continuing to stir at high speed while gradually adding 480 g of viscous fluid fuel. The viscosity of this fluid fuel was 2300 cp, and it remained stable with no change even when the viscosity was measured two months later. Table 4 shows the amount of preparation and calorific value in this example.
【表】
実施例 2
木材工場内樹皮廃材を炭化した含水率40%前後
の粉状炭300gに対して、10%のロジンを含むエ
チルアルコール(含水率5%)100gと灯油100g
を高速撹拌器の中に入れ、混合撹拌を約3分間お
こなつた後、分散安定剤15g(純物で5.25g)と
アルギン酸ソーダ0.03%水溶液28gを徐々に添加
しながら高速撹拌を続けると、粘稠な流体燃料が
543g得られる。この流体燃料の粘度は3100cp
で、2ケ月後粘度を測定したが約100cpの低下を
示したのみである。
本実施例の仕込量と発熱量を表示すれば第5表
の通りである。[Table] Example 2 100 g of ethyl alcohol (5% water content) containing 10% rosin and 100 g of kerosene to 300 g of powdered charcoal with a water content of around 40% obtained by carbonizing bark waste in a lumber factory.
was placed in a high-speed stirrer, mixed and stirred for about 3 minutes, and then high-speed stirring was continued while gradually adding 15 g of dispersion stabilizer (5.25 g in pure form) and 28 g of a 0.03% sodium alginate aqueous solution. viscous fluid fuel
543g obtained. The viscosity of this fluid fuel is 3100cp
After two months, the viscosity was measured, but it only showed a decrease of about 100 cp. Table 5 shows the amount of preparation and calorific value in this example.
【表】
実施例 3
農業廃棄物モミガラを流効炭化炉で炭化した含
水率30%前後の微粉炭化物300gに対してロジン
を10%添加したエチルアルコール(含水率10%)
100gと灯油100gを高速撹拌器中に入れて混合撹
拌を約3分間おこなう。以後、分散安定剤18g
(純物で6g)とCMC1%水溶液30gを徐々に添
加しながら高速撹拌を続けると粘稠な流体燃料が
748g得れる。この流体燃料の粘度は2800cpで、
3ケ月後粘度を測定したところ、約50cpの粘度
上昇を示した。
本実施例の仕込量と発熱量を表示すれば第6表
の通りである。[Table] Example 3 Ethyl alcohol with 10% rosin added to 300g of pulverized carbide with a moisture content of around 30% obtained by carbonizing agricultural waste rice husk in a flowing-effect carbonization furnace (water content 10%)
Put 100g and 100g of kerosene into a high-speed stirrer and mix and stir for about 3 minutes. After that, 18g of dispersion stabilizer
(6g in pure form) and 30g of CMC 1% aqueous solution are gradually added and high-speed stirring is continued to form a viscous fluid fuel.
You can get 748g. The viscosity of this fluid fuel is 2800cp,
When the viscosity was measured after 3 months, it was found that the viscosity had increased by about 50 cp. Table 6 shows the amount of preparation and calorific value in this example.
【表】
実施例 4
農業廃棄物サトウキビからを簡易炭化炉で炭化
した含水率15%前後の炭化物300gに対して、ロ
ジンを10%添加したエチルアルコール(含水率10
%)50gと、A重油100gを自動乳鉢に入れて混
練混合すると、炭化物は油とアルコール中で微粉
砕される。この微粉炭液に分散安定剤20g(純物
で8g)と、PEG50%水溶液20gとを徐々に加
えながら自動混合乳鉢中で撹拌を続けると、10分
後には急激に粘性を増して安定なコロイダル状の
流体燃料が490g得られる。この流体燃料の粘度
は製造直後も3ケ月経過後も3400cpの値を示し
た。
本実施例の仕込量と発熱量を表示すれば第7表
の通りである。[Table] Example 4 Ethyl alcohol with 10% rosin added (water content 10
%) and 100 g of heavy oil A are placed in an automatic mortar and kneaded and mixed, and the carbide is finely ground in the oil and alcohol. When 20 g of dispersion stabilizer (8 g of pure material) and 20 g of 50% PEG aqueous solution are gradually added to this pulverized coal liquid while stirring is continued in an automatic mixing mortar, the viscosity increases rapidly after 10 minutes and the colloid becomes stable. 490g of liquid fuel is obtained. The viscosity of this fluid fuel was 3400 cp both immediately after production and after 3 months. Table 7 shows the amount of preparation and calorific value in this example.
【表】
実施例 5
故紙類を原料とした炭化物は容易に微粉化され
るが、このままの状態では燃料としての用途がな
い。含水率5%前後の故紙炭化物300gに対し
て、ロジンを10%添加したエチルアルコール(含
水率10%)を70gと、A重油中にC重油を30%程
度添加した混合重油100gとを加えて撹拌器で約
10分程混合混練する。この混合物に対して分散安
定剤25g(純物で7g)と、PEG50%水溶液20
g、更に、澱粉のり5gとを徐々に加えながら撹
拌を続けると、8分程経過後、急速に粘稠さを増
し、均一に分散したコロイダル燃料が520g得ら
れる。この流体燃料の粘度は3600cpで2ケ月経
過してもその粘度は変化を示さない。本実施例の
仕込量と発熱量を表示すれば第8表の通りであ
る。[Table] Example 5 Carbide made from waste paper is easily pulverized, but it has no use as a fuel in this state. To 300 g of waste paper charcoal with a moisture content of around 5%, add 70 g of ethyl alcohol (water content 10%) containing 10% rosin and 100 g of a mixed heavy oil containing about 30% C heavy oil in A heavy oil. Approximately with a stirrer
Mix and knead for about 10 minutes. To this mixture, add 25 g of dispersion stabilizer (7 g in pure form) and 20 g of 50% PEG aqueous solution.
When stirring is continued while gradually adding 5 g of starch paste and 5 g of starch paste, 520 g of colloidal fuel that rapidly increases in viscosity and is uniformly dispersed is obtained after about 8 minutes. The viscosity of this fluid fuel was 3600 cp, and the viscosity did not change even after two months had passed. Table 8 shows the amount of preparation and calorific value in this example.
【表】
本発明は以上のように構成したので、第1に流
体であるため輸送上有利になること、第2に炭と
油とアルコールの混合系なので7000kcal/Kg以上
の高発熱量となり一般用の燃料として充分に使用
できることという優れた効果を有する。更に特記
すれば、木質バイオマス、草本バイオマスは自然
に放置すると風化し分解してしまうが、これらを
炭化すれば腐朽することがなく炭素源を永久に固
定することができるので、本発明の複合燃料は四
季を通じて生産がコンスタントに計画できること
である。
さらに本発明においては流体燃料は水を含有し
ているので、その理論空燃比は石炭よりも小さ
く、従つて稀薄な混合空気での燃焼が可能であ
り、又排ガス中の有害成分の濃度も低くなるだけ
でなく、含水率が高いのでNOxの低減化にも有
効である。[Table] Since the present invention is constructed as described above, firstly, it is a fluid, which is advantageous for transportation, and secondly, since it is a mixture of charcoal, oil, and alcohol, it has a high calorific value of over 7000 kcal/Kg, which is common. It has the excellent effect of being able to be used sufficiently as a fuel for other purposes. Furthermore, in particular, woody biomass and herbaceous biomass will weather and decompose if left in the natural environment, but if they are carbonized, they will not decay and the carbon source can be permanently fixed, so the composite fuel of the present invention This means that production can be planned constantly throughout the four seasons. Furthermore, in the present invention, since the fluid fuel contains water, its stoichiometric air-fuel ratio is lower than that of coal, and therefore combustion is possible with a lean air mixture, and the concentration of harmful components in the exhaust gas is also low. Not only that, but it also has a high water content, so it is effective in reducing NOx.
Claims (1)
に、ロジンを含むアルコールを加えた混合物に、
その重量の等量以上の油との混合物であり、かつ
界面活性剤及びゲル化剤による中性コロイダル状
流体で、水分が10〜20重量%でその粘度が250〜
5000cpの範囲であることを特徴とする植物体炭
化物の複合流体燃料。 2 200メツシユ以下に粉砕した植物炭化物に対
し、その重量の1/2以下となるようにロジンを含
んだアルコールを加えた混合物の重量の等量もし
くは等量以上の油類を加えた混合物に、界面活性
剤を0.5〜1.5%及びゲル化剤を助剤として全重量
の0.5〜1.5%を添加し、かつそのPHをほぼ中性に
又その含水率を5〜20%に調整し、その粘度を
250〜5000cpとすることを特徴とする植物体炭化
物の複合液体燃料の製造方法。[Claims] 1. A mixture of charred plant matter crushed to 200 mesh or less and alcohol containing rosin,
It is a mixture with oil in an amount equal to or more than its weight, and is a neutral colloidal fluid made of surfactants and gelling agents, with a water content of 10 to 20% by weight and a viscosity of 250 to 250%.
A composite fluid fuel made of carbonized plant material characterized by a range of 5000 cp. 2. To a mixture of vegetable charcoal crushed to 200 mesh or less, to which alcohol containing rosin has been added to make up to 1/2 of the weight or less, and oil in an amount equal to or more than the weight of the mixture, Add 0.5 to 1.5% of the total weight of a surfactant and a gelling agent as an auxiliary agent, adjust the pH to almost neutral and the water content to 5 to 20%, and adjust the viscosity. of
1. A method for producing a composite liquid fuel of charred plant matter, characterized in that the fuel is 250 to 5000 cp.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16585181A JPS5867788A (en) | 1981-10-19 | 1981-10-19 | Fluid compound fuel of carbonized plant and its preparation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16585181A JPS5867788A (en) | 1981-10-19 | 1981-10-19 | Fluid compound fuel of carbonized plant and its preparation |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5867788A JPS5867788A (en) | 1983-04-22 |
JPS6241640B2 true JPS6241640B2 (en) | 1987-09-03 |
Family
ID=15820196
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16585181A Granted JPS5867788A (en) | 1981-10-19 | 1981-10-19 | Fluid compound fuel of carbonized plant and its preparation |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5867788A (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61271395A (en) * | 1985-05-27 | 1986-12-01 | Universal Gijutsu Kaihatsu Kenkyusho:Kk | Composite fuel |
JP4832472B2 (en) * | 2008-06-27 | 2011-12-07 | 三菱電機株式会社 | Packing equipment |
-
1981
- 1981-10-19 JP JP16585181A patent/JPS5867788A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS5867788A (en) | 1983-04-22 |
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