JPS5867788A - Fluid compound fuel of carbonized plant and its preparation - Google Patents
Fluid compound fuel of carbonized plant and its preparationInfo
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- JPS5867788A JPS5867788A JP16585181A JP16585181A JPS5867788A JP S5867788 A JPS5867788 A JP S5867788A JP 16585181 A JP16585181 A JP 16585181A JP 16585181 A JP16585181 A JP 16585181A JP S5867788 A JPS5867788 A JP S5867788A
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- carbonized
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Abstract
Description
【発明の詳細な説明】
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チ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。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a composite fluid fuel comprising charcoal obtained from woody biomass and herbaceous biomass, oils, and alcohol containing about 10 g of pine resin, and a method for producing the same.
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6.500 kcat/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?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。In today's modernized life, gasified fuel or liquid fuel with a capacity of 6,500 kcat/kg or more is mostly used for household fuel, and for various industrial uses? Liquid fuel (heavy oil or kerosene), which is easy to use and has a high calorific value, is also used as oil fuel or agricultural fuel.
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。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.
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、ウデノ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。Firewood, processed ogalite, udenox, etc. are produced and used as fuel directly from biomass. Originally, herbaceous biomass, mainly wood, is an amorphous solid phase that contains a large amount of water.
Its apparent bulk specific gravity is small, and its constituent components contain many oxygen atoms, so its absolute calorific value is low, and its range of uses as a fuel is limited.
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・ぐイオマス、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
。In addition, the apparent specific gravity, which is a problem in transportation, is 0.8 for oil and 0.7 for coal, but it is extremely small at 0.1 for wood/guinea mass and herbaceous biomass. It has many disadvantages compared to other fuels, such as low heat and disadvantages in terms of transportation costs. 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.
本発明は上記の現況に鑑み、木質系バイオマス、□草本
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。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 herbaceous biomass into a fluid composite fuel. do.
最近バイオマスという言葉がよく使用されるが・ぐイオ
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ウコトになる。バイオマス
は陸域・々イオマスト水域バイオマスに大別される。陸
域・ぐイオマスとしては、■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J 1981 (3゜
56年)5月号P、10〜16には、このうち■。The word biomass is often used these days, but if we define biomass, it means that it is accumulated on a quantitative scale and is used to generate energy and energy.
Ukoto refers to living organisms that serve as a resource for food and industrial raw materials, or objects produced along with biological activities. Biomass is broadly divided into terrestrial and iomast water biomass. Terrestrial biomass includes ■starchy biomass, ■carbohydrate biomass, ■woody biomass, ■herbaceous biomass,
It can be divided into ■hydrocarbon biomass and ■waste biomass. Magazine "Wood Industry J 1981 (3゜56) May issue P, 10-16 includes ■.
■を原料とした複合流体燃料の総説が掲載されている。Contains a review of composite fluid fuels made from ■.
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。The second object of the present invention is to provide an easy-to-use fluid fuel using charred materials of (1) woody biomass and (2) herbaceous biomass as raw materials.
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チを占め、どこの家庭にも木炭の1俵や2
俵はころがっていたものである。Until the 1950s, the consumption of wood energy accounted for 80cm of total energy consumption, and every household had one or two bales of charcoal.
The bales were lying around.
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
ってしまった。過疎地帯の山村農家まで電力、化石燃料
に変ってしまったが、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。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.
そこで発明者は使用し易い流体燃料化の研究を行った結
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4.500 k cal/kl/だが木炭は
平均7. OOOk ca17ftg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。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. Dry firewood has an average value of 4.500 kcal/kl/, but charcoal has an average value of 7.500 kcal/kl/. OOOk ca17ftg and unlike firewood, it is flameless. When wood is heated, it decomposes into gaseous substances and charcoal. This phenomenon is called wood pyrolysis.
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
っている。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1
40℃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。Charcoal has the 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 1
The temperature is around 40℃. 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 charcoal at a temperature of approximately 450°C.
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、
前記様々の目的を達成するためこの粉状木炭に油類と松
やにを10俤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ケ゛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だめに燃
料全重量に対して水分量を10〜25チに調整し粘度を
250〜5,0OOcPとするように構成したものであ
る。As mentioned above, charcoal does not contain oxygen atoms in its molecular structure like firewood, so its calorific value is high;
Considering that it is easier to pulverize compared to wood,
In order to achieve the various purposes mentioned above, this powdered charcoal is mixed with alcohol containing 10 g of oil and pine resin, mixed and kneaded in a mortar to make the charcoal into a uniform fine powder, which is then turned into a stable colloidal fluid fuel. In order to make the water-soluble surfactant 0.
5 to 1.5%, and 0.06 to 0.5% of a vegetable caking agent or a synthetic polymer aqueous solution to the total weight as an additive. The water content is adjusted to 10 to 25 inches relative to the weight, and the viscosity is 250 to 5.0 OOcP.
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。The charred materials used in the present invention include charred wood biomass, charred herbaceous biomass (for example, charred rice husk, charred sugarcane, etc.), charred waste paper, and the like.
アルコールハ、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チ添加する
と松やにはアルコール中によく溶解する。Alcohol, ethyl alcohol, or methyl alcohol may be used, but if 10 g of pine resin is added to this alcohol, the pine resin will dissolve well in the alcohol.
界面活性剤としては中性、水溶液型のものを使用する。As the surfactant, a neutral, aqueous type surfactant is used.
一般に使用できるものは
α−オレフィン系(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。Generally usable products are mixtures of α-olefins (anions), higher alcohols (anions), fatty acids (non-ions), and higher alcohols (non-ions), with some of them removed. Can be used. For example, simple surfactants include linear alkylbenzene type and higher alcohol type (anion).
Mixtures can be used as dispersants.
中性界面活性剤の添加量は全重量に対して最低1.5チ
を要する。なお上限は1.5チでそれ以上は効果として
同一である。The amount of neutral surfactant added must be at least 1.5 inches based on the total weight. The upper limit is 1.5 inches, and the effect is the same beyond that.
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
、海藻をすシ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 (ポリエチレンクリコール)
トカ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、250〜5.0’ OOcPの範囲に調整する
ものである。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 crushing seaweed. PEG (polyethylene glycol) is added to these highly viscous plant-based substances.
A mixture containing 50% of Toka PvA (polyvinyl alcohol), etc., which is 0.06 to 0.06% of the total weight.
5%, it is adjusted to a range of 250 to 5.0' OOcP.
又、水分の含有量を5〜20チとする。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
とによるものである。Further, the water content is set to 5 to 20 inches. As mentioned above, this is for colloidal dispersion and for adjusting the viscosity, and also because the combustibility of the fluid fuel is good within this range.
本発明のコロイダル状混合物を得る攪拌は、高速攪拌機
か、または乳鉢状すりつぶし方式がよい。Stirring to obtain the colloidal mixture of the present invention is preferably performed using a high-speed stirrer or a mortar-like grinding method.
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。In both cases, a hot method is used since powdered coal may explode.
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
チ添加エチルアルコール(EA)の重量組成側にそれぞ
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チ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。Tables 1 to 3 show the results of typical experimental examples, and Table 1 shows the calorific value measurement results of charcoal, ethyl alcohol containing 10% pine resin, and kerosene composite fuel. Also, Table 2 shows charcoal, pine tar, 10
These are the calorific value measurement results when kerosene was added to the weight composition side of ethyl alcohol (EA). Furthermore, Table 3 shows the measurement results of the calorific value of charcoal, 10% ethyl alcohol added to pine resin, and kerosene/water-based composite fuel as a function of water content (MC) changes.
第1表 木炭・口・シン10チを含む エチルアルコール・石油複合燃料 次に本発明の実施例をさらに詳細に説明する。Table 1 Including charcoal, mouth, and thin 10 pieces Ethyl alcohol/petroleum composite fuel Next, embodiments of the present invention will be described in more detail.
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25
0gに対して10チのロジンを含むエチルアルコール(
含水率5%)100gと灯油100Iを高速攪拌器に入
れて混合攪拌した後、α−オレフィン系(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チに調製処方された中性タイプの
分散安定剤15g(鈍物5.259 )と、低品質糖蜜
(含水率30%)20gを徐々に添加しながら高速攪拌
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2.300cPで2ケ月後粘度を測
定しても変化がなく安定であった。Example 1 Finely powdered charcoal 25 with a moisture content of around 20% obtained by carbonizing forest residues
Ethyl alcohol containing 10 g of rosin (
After mixing and stirring 100 g of kerosene (water content 5%) and 100 I of kerosene in a high-speed stirrer, α-olefin (anion),
Add water to a surfactant consisting of a higher alcohol type (anion), a higher alcohol type (nonionic), or a fatty acid type (nonionic) to a concentration of 35%. 15g of a formulated neutral type dispersion stabilizer ( By gradually adding 20 g of low quality molasses (water content 30%) and continuing high speed stirring, 480 g of viscous fluid fuel was obtained. The viscosity of this fluid fuel was 2.300 cP, and it was stable with no change even when the viscosity was measured two months later.
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 4 shows the amount of preparation and calorific value in this example.
実施例2
木材工場内樹皮廃材を炭化した含水率40チ前後の粉状
炭300gに対して、1OaIbのロノンを含むエチル
アルコール(含水率5%)100gと灯油100gを高
速攪拌器の中に入れ、混合攪拌を約3分間おこなった後
、分散安定剤15g(鈍物で5.25/)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
速攪拌を続けると、粘稠な流体燃料が543 g”得ら
れる。この流体燃料の粘度は3100 cPで、2ケ月
後粘度を測定しだが約100 cPの低下を示したのみ
である。Example 2 100 g of ethyl alcohol (5% water content) containing 1 OaIb of ronone and 100 g of kerosene were placed in a high-speed stirrer to 300 g of powdered charcoal with a water content of around 40 g obtained by carbonizing bark waste in a wood factory. After mixing and stirring for about 3 minutes, 15g of dispersion stabilizer (5.25/ml with a blunt material) and 28g of a 0.03% sodium alginate aqueous solution are gradually added and high-speed stirring is continued, resulting in a viscous fluid fuel. The viscosity of this fluid fuel was 3100 cP, and when the viscosity was measured two months later, it only showed a decrease of about 100 cP.
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 5 shows the amount of preparation and calorific value in this example.
実施例3
農業廃棄物モミがうを流動炭化炉で炭化した含水率30
%前後の微粉炭化物300gに対してロノンを10%添
加したエチルアルコール(含水率10チ)100gと灯
油100gを高速攪拌器中に入れて混合攪拌を約3分間
おこなう。以後、分散安定剤18g(鈍物で6.9)と
CMCI%水溶液30gを徐々に添加しながら高速攪拌
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2,800cP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。Example 3 Agricultural waste rice sac was carbonized in a fluidized carbonization furnace with a moisture content of 30
% of ethyl alcohol (water content: 10%) and 100 g of kerosene are placed in a high-speed stirrer and mixed and stirred for about 3 minutes. Thereafter, 18 g of dispersion stabilizer (6.9 g for blunt material) and 30 g of CMCI% aqueous solution were gradually added while high-speed stirring was continued to obtain 748 g of viscous fluid fuel. The viscosity of this fluid fuel was 2,800 cP, and when the viscosity was measured after 3 months, it showed an increase in viscosity of about 50 cP.
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 6 shows the amount of preparation and calorific value in this example.
実施例
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、ロノンを10
チ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線混合すると、
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(鈍物で8g)と、PEG 50
チ水溶液20gとを徐々に加えながら自動混合乳鉢中で
攪拌を続けると、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。Example: For 300 g of carbonized agricultural waste sugarcane with a water content of around 15%, which was carbonized in a simple carbonization furnace, 10% of Ronone was added.
When 50 g of ethyl alcohol (moisture content 10%) and 100 g of A heavy oil are placed in an automatic mortar and mixed,
The carbide is pulverized in oil and alcohol. Add 20g of dispersion stabilizer (8g of blunt material) and PEG 50 to this pulverized coal liquid.
When stirring is continued in an automatic mixing mortar while gradually adding 20 g of the aqueous solution, the viscosity increases rapidly after 10 minutes to obtain 490 g of stable colloidal fluid fuel.
この流体燃料の粘度は製造直後も3ケ月経過後も3.4
00cPO値を示した。The viscosity of this fluid fuel is 3.4 both immediately after production and after 3 months.
00cPO value was shown.
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 7 shows the amount of preparation and calorific value in this example.
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、ロノンを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100
9とを加えて攪拌器で約10分程混合混練する。この混
合物に対して分散安定剤25g(鈍物で79)と、PE
G 50%水溶液20g1更に、澱粉のり5gとを徐々
に加えながら攪拌を続けると、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3,600cP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表の通シである。Implementation/Example 5 Carbide made from waste paper is easily pulverized, but it has no use as a fuel in this state. Moisture content 5%
70g of ethyl alcohol (water content 10%) with 10% ronone added to 300g of waste paper charcoal before and after,
Mixed heavy oil 100 with approximately 30% C heavy oil added to A heavy oil
9 and mix and knead with a stirrer for about 10 minutes. To this mixture, 25 g of dispersion stabilizer (79 g of blunt material) and PE
G 20g of 50% aqueous solution 1 Furthermore, when stirring is continued while gradually adding 5g of starch paste, after about 8 minutes, the viscosity rapidly increases and 520g of uniformly dispersed colloidal fuel is obtained.
can get. The viscosity of this fluid fuel was 3,600 cP, and the viscosity did not change even after two months had passed. Table 8 shows the amount of preparation and calorific value of this example.
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7.000 k cat/Ig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七生産がコンスタントに計画できる
ことである。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 mixed system of charcoal, oil, and alcohol, it has a high calorific value of 7.000 kcat/Ig or more. It has the excellent effect of being fully usable as a general fuel. 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.
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、従って稀薄な
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。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 mixture of air, and the concentration of harmful components in the exhaust gas is also lowered. In addition, the high moisture content reduces NOx
It is also effective in reducing
Claims (2)
、ロノンを含むアルコールを加えた混合物に、その重量
の等量販上の油との混合物であり、かつ界面活性剤及び
グル化剤による中性コロイグル状流体で、水分が10〜
20重量%でその粘度が250〜5,000cPの範囲
にあることを特徴とする植物体炭化物の複合流体燃料。(1) A mixture of carbonized plant material crushed to 200 mesh or less, alcohol containing ronone, and commercially available oil in an equal amount by weight, and neutralized by a surfactant and a gluing agent. A coroiglu-like fluid with a water content of 10~
A composite fluid fuel made of carbonized plant matter, characterized in that the viscosity is in the range of 250 to 5,000 cP at 20% by weight.
、その重量の1/2以下となるようにロノンを含んだア
ルコールを加えた混合物の重量の等量もしくは等量販上
の油類を加えた混合物に、界面活性剤を0.5〜1.5
チ及びグル化剤を助剤として全重量の0.5〜1.5チ
を添加し、かつその−をほぼ中性に又その含水率を5〜
20%に調整し、その粘度を250〜5,0OOcP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。(2) A mixture made by adding alcohol containing ronone to 1/2 or less of the weight of vegetable charcoal crushed to 200 meth or less, or an equivalent amount of commercially available oils. Add surfactant to 0.5 to 1.5
0.5 to 1.5 of the total weight is added as an auxiliary agent and a gluing agent, and the - is almost neutral and the water content is 5 to 5.
20% and the viscosity thereof is 250 to 5,000cP.
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 true JPS5867788A (en) | 1983-04-22 |
JPS6241640B2 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) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61271395A (en) * | 1985-05-27 | 1986-12-01 | Universal Gijutsu Kaihatsu Kenkyusho:Kk | Composite fuel |
JP2010006428A (en) * | 2008-06-27 | 2010-01-14 | Mitsubishi Electric Corp | Packaging device |
-
1981
- 1981-10-19 JP JP16585181A patent/JPS5867788A/en active Granted
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61271395A (en) * | 1985-05-27 | 1986-12-01 | Universal Gijutsu Kaihatsu Kenkyusho:Kk | Composite fuel |
JPH0464640B2 (en) * | 1985-05-27 | 1992-10-15 | Yunibaasaru Gijutsu Kaihatsu Kenkyusho Kk | |
JP2010006428A (en) * | 2008-06-27 | 2010-01-14 | Mitsubishi Electric Corp | Packaging device |
Also Published As
Publication number | Publication date |
---|---|
JPS6241640B2 (en) | 1987-09-03 |
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