JPS588794A - Mixed fuel - Google Patents
Mixed fuelInfo
- Publication number
- JPS588794A JPS588794A JP56106857A JP10685781A JPS588794A JP S588794 A JPS588794 A JP S588794A JP 56106857 A JP56106857 A JP 56106857A JP 10685781 A JP10685781 A JP 10685781A JP S588794 A JPS588794 A JP S588794A
- Authority
- JP
- Japan
- Prior art keywords
- oil
- coal
- mixed fuel
- water
- mixed
- 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.)
- Granted
Links
Landscapes
- Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
- Liquid Carbonaceous Fuels (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、長期安定性と流動性の良い混合燃料に関する
。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a mixed fuel with long-term stability and good flowability.
近年、石油が高騰し1代替エネルギーが色々検削されて
いる。その中に、微粉炭と油を混合した膠質燃料がある
。ただ単に油中に微粉炭を混合するのけ、ストークスの
式が示す如く、ただちに微粉炭が沈降するので、それを
防止するため、水と界面活性剤を石炭/油混合物中に添
加する方法(特開昭54−40809号公報等)や石炭
を超微粉化して油の中に分散させる方法(特開昭54−
40808号公報)等が横1されている。しかしながら
界面活性剤添加法は多くの場合界面活性剤の添加量が多
く経済的に問題があり、一方石炭を超微粉化する方法は
粉塵爆発の危険性や粉砕に多大なエネルギーを必要とす
るため工業的実施に問題がある 加えて、いずれの場合
も分散安定性および流動性が必らずしも充分でない。In recent years, oil prices have soared, and various alternative energy sources are being explored. Among them is colloid fuel, which is a mixture of pulverized coal and oil. If you simply mix pulverized coal in oil, the pulverized coal will immediately settle out, as shown by the Stokes equation.To prevent this, there is a method of adding water and a surfactant to the coal/oil mixture. JP-A-54-40809, etc.) and a method of ultra-finely pulverizing coal and dispersing it in oil (JP-A-54-40809, etc.)
40808) etc. are shown horizontally. However, the surfactant addition method is often economically problematic because the amount of surfactant added is large, while the method of ultra-finely pulverizing coal poses the risk of dust explosions and requires a large amount of energy for pulverization. In addition, dispersion stability and fluidity are not always sufficient in either case.
本発明者らは前述の実情にかんがみ、鋭意研究を重ねた
結果、タンカーやパイプラインによる大量輸送に適した
流動性と長期安定性を有する混合燃料を完成するに致っ
た。In view of the above-mentioned circumstances, the inventors of the present invention have conducted intensive research and have completed a mixed fuel that has fluidity and long-term stability suitable for mass transportation by tankers and pipelines.
すなわち、本発明は1石炭重油、水及び超微粒子状シリ
カとからなる混合燃料である。That is, the present invention is a mixed fuel consisting of 1 coal heavy oil, water, and ultrafine particulate silica.
本発明に用いられる石炭は、無煙炭、歴青炭、褐炭々ど
種々のもので良い。その粒度は100メツシユ篩過10
0チであれば貞いが、好1しくけ200メツシユ篩過8
0〜90係が良い。これより荒い粒径では石炭が沈降し
てし1い、超微粒子例えば5μ271以下迄粉砕するの
は、炭塵爆発の恐れがあり1g済的にも不利である。The coal used in the present invention may be of various types, such as anthracite, bituminous coal, and brown coal. Its particle size is 100 mesh sieved.
If it's 0, it's good, but it's good to pass 1 sieve and 200 mesh sieves.
0-90 is good. If the particle size is coarser than this, the coal will settle, and if it is crushed to ultra-fine particles, for example, 5μ271 or less, there is a risk of coal dust explosion, and it is disadvantageous in terms of cost per gram.
石炭と油の混合割合は、石炭の種類や粒度および油独に
より、また要求される安定性や流動性によって異なるが
、一般には石炭/油の重量比を3/7〜7/3の範囲に
選定するのか良い。もちろん3/7よシ少ない石炭混入
量でも流動性および安定性は良好であるが、混合燃料の
本来の意味からして、経済的有利性がなくなる。また7
/3以上の石炭混入は、粘度が高くなり過きて流動性が
低下し実用に供しなくなる。The mixing ratio of coal and oil varies depending on the type and particle size of the coal, the oil content, and the required stability and fluidity, but in general, the coal/oil weight ratio is in the range of 3/7 to 7/3. It's good to choose. Of course, fluidity and stability are good even if the amount of coal mixed is less than 3/7, but from the original meaning of mixed fuel, it is no longer economically advantageous. Also 7
If coal is mixed in at a ratio of /3 or more, the viscosity becomes too high and the fluidity decreases, making it impractical.
水は本発明の混合螺:料中で超微粒子状シリカと作用し
、後述の網目構造形成に寄与するので、該混合燃料中に
6存在しなければならない。その含有皿ニ1、全体に対
し約o、i〜20 ! m−%であり。Since water acts with the ultrafine particulate silica in the mixed screw material of the present invention and contributes to the formation of the network structure described below, it must be present in the mixed fuel. Its content is approximately o, i~20 for the entire dish! m-%.
0.1係以下で仁J光分カ網目構造を形成せず、2oチ
以上では水の体積分だけ輸送費や貯#l費が高くカリ、
単位体積当りの発熱量も減少するので好丑(7くない。At a ratio of less than 0.1, no network structure is formed, and at a ratio of 2 or more, the transportation and storage costs are high due to the volume of water.
This is a good thing because the amount of heat generated per unit volume also decreases.
この水は石炭、油、超イ+fi粒子状シリカと共に持ち
込1れる水、!fたけ、θ1だに添加する水のどちらで
も良い。This water is brought in with coal, oil, and super-fi+fi particulate silica! Either f or θ1 water may be added.
本発明に用いる超沓粒子状シリカとけ、約40μm以下
のオiL径の粒子であり、8i02を約60−以上含有
する混合物または化合物を云う、1
超イノシ粒子状シリカには例えば、
(1) フェロシリコンを原料として傅らねる超可1
次粒子状無水シリカ(アエロジル■日本アエロジル社製
)
(2) コロイダルシリカを濃縮したもの(3)
シリカゲルを約40μm以下の粒子にしたものがあ、・
・0この中で最も好ましいのけ。超微粒子状無水シリカ
である。。The particulate silica particles used in the present invention are particles with an oil diameter of about 40 μm or less, and refer to a mixture or compound containing about 60 or more 8i02. Examples of the particulate silica include (1) Super easy to use ferrosilicon as raw material 1
Secondary particulate anhydrous silica (Aerosil ■manufactured by Nippon Aerosil Co., Ltd.) (2) Concentrated colloidal silica (3)
There are silica gel particles of approximately 40 μm or less.
・0 The most preferred of these. Ultrafine particulate anhydrous silica. .
該超イj″J粒子状シリカが本発明の混合燃料の有力な
分数安定剤と力る理由し1定がでないが、該微粒子状シ
リカが油中にて水と作用し網目構造を形成し、石炭の沈
降を防止するものと考えられる。The reason why the ultra-high-density particulate silica is an effective fractional stabilizer for the mixed fuel of the present invention is not certain, but the reason is that the particulate silica interacts with water in oil to form a network structure. , is thought to prevent coal from settling.
該超微粒子状シリカの添加量は2石炭の種類やその粒度
および油種により、また要求される安定性および流動性
の度合により異なるが、一般的には混合物中に少なくと
も0.1重用チ程度添加しなければ効果がない。望まし
くけ0.5〜10重ff1− Z程度である。0.1%
り下では安定性が劣り、10チ以上ではこれ以上添加し
ても効果は同じであり、経済的にも不利である。The amount of ultrafine particulate silica added varies depending on the type of coal, its particle size, oil type, and the required degree of stability and fluidity, but generally it is at least about 0.1 silica in the mixture. It has no effect unless added. Desirably, it is about 0.5 to 10 weights ff1-Z. 0.1%
At lower temperatures, the stability is poor, and at higher temperatures than 10 cm, the effect is the same even if more is added, which is economically disadvantageous.
本発明の混合燃料は、油、水1石炭トよび超微粒子状シ
リカ全常温で均一混合することにより得られるが、望ま
しいのけ油中に水および超微粒子状シリカを添加し均一
にして、次いで石炭を添加し均一混合するととにより、
より良い分散安定性を有する混合燃料を得ることができ
る3゜以上の如く、安く簡単に、分散安定性を有し。The mixed fuel of the present invention can be obtained by homogeneously mixing oil, water, coal, and ultrafine particulate silica at room temperature. By adding coal and mixing it uniformly,
It is possible to obtain a mixed fuel with better dispersion stability, such as 3 degrees or more, which is cheap, simple, and has dispersion stability.
流動性の良い混合燃料を得ることができた。We were able to obtain a mixed fuel with good fluidity.
以下1本発明を実施例によりさらに詳細に説明する。な
お、実施例における0内の数値及び%d全体量に対する
重相%を示し、粘度は回転式粘度用を用い、ローター随
21回転数12 rpmにて611]定した値である。The present invention will be explained in more detail below with reference to Examples. In addition, the numerical value within 0 and the heavy phase % with respect to the total amount in %d are shown in the examples, and the viscosity is a value determined using a rotational viscosity meter at a rotor speed of 21 rotations and 12 rpm.
実施例1
70℃における比重o、92、粘度30 cps及び発
熱lが10500 K Cat/V4の重油120 f
(47,25)を約70 ’Cの湯浴中で、TKK
ホモミキサーで攪拌しながら別途AEJ%08IL■
(日本アエロジル株式会社製。Example 1 Heavy oil 120 f with specific gravity o at 70°C, 92, viscosity 30 cps, and heat release l of 10500 K Cat/V4
(47,25) in a water bath at about 70'C, TKK
Separately add AEJ%08IL while stirring with a homomixer.
(Manufactured by Nippon Aerosil Co., Ltd.
グレード名aoo 、 OX 50 、 TT 600
、 MOXso、R972の511jJillV )
1.3F (0,5)を水12.8 f (5)に分
散させたものfAtJ記重油中に混合し、 10〜15
分間攪拌分散させた 次いで、この分散液中に豪州産の
ハンタバレー炭を日本精機製作新製の遠心粉砕機ZM−
1を用い、スクリーンの穴径0.25 mmにて粉砕し
て得た微粉炭12Or (47,25)を混合し、20
〜30分間攪拌分散させ、混合燃料を得た。このものの
70℃における粘度はグレード300のとき。Grade name aoo, OX 50, TT 600
, MOXso, R972's 511jJillV)
1.3 F (0,5) dispersed in water 12.8 F (5) fAtJ Mixed in heavy oil, 10-15
The dispersion was then stirred and dispersed for a minute. Next, Australian Hunter Valley charcoal was added to the dispersion using a new centrifugal crusher ZM-
1, mixed with 12Or (47,25) of pulverized coal obtained by crushing it with a screen hole diameter of 0.25 mm,
The mixture was stirred and dispersed for ~30 minutes to obtain a mixed fuel. The viscosity of this product at 70°C is grade 300.
370 cps、OX 50 (7)とき、340 c
ps 、 TT 600のと@ 、 330 cps
、 MOX 80のとき340 cps 、 R97
2のとき340 cpsであった。370 cps, OX 50 (7) at 340 c
ps, TT 600@, 330 cps
, 340 cps at MOX 80, R97
2, it was 340 cps.
次に、この混合燃料f 500 ccのメスシリンダー
に入れ、約70°Cの湯浴中にて150間の放置安定性
試験を行つfc 。Next, this mixed fuel fc was put into a measuring cylinder of 500 cc and subjected to a storage stability test for 150 hours in a hot water bath at about 70°C.
15日後、上層、中層、下層に分け、それぞれの70℃
における粘度と比重を測定した。その結果を表−1に示
す
表 −1
実施例2
実施例1にて用いた電油および微れ・炭を用いAE L
、(、OS I L■(日本アエロジル社製)の各柚グ
レード、コロイダルシリカおよびシリカゲルを約20μ
mに粉砕したものにつき、その添加割合、添加水の童お
よび石炭/油の重量比を変え、実施例1と同様の方法で
、混合燃料を得、次いで、この混合燃料を面径約20調
、高さ約200咽の沈降管に入れ、湯浴中にて7日間放
置した。After 15 days, divide into upper layer, middle layer, and lower layer and heat each layer to 70℃.
The viscosity and specific gravity were measured. The results are shown in Table-1 Table-1 Example 2 AE L using the electric oil and fine charcoal used in Example 1
, (,OS I L■ (manufactured by Nippon Aerosil Co., Ltd.) of each yuzu grade, colloidal silica and silica gel in an amount of about 20μ
A mixed fuel was obtained in the same manner as in Example 1 by changing the addition ratio, the weight ratio of added water, and the coal/oil. It was placed in a sedimentation tube with a height of about 200 mm and left in a hot water bath for 7 days.
その結果を表2に示す。The results are shown in Table 2.
弄 −2 注; ○:流動性、安定性ともに良好 ×:流、動性、安定性ともに劣る Δ 流動性、安′JE性やや劣る 特許出願人 旭化成工業株式会社Fuck -2 Note: ○: Both fluidity and stability are good. ×: Poor flow, dynamics, and stability. Δ Liquidity, low JE property is slightly inferior Patent applicant: Asahi Kasei Industries, Ltd.
Claims (1)
る混合燃料 2 微粒子状シリカの量が、0.1〜10重量%である
特許請求の範囲第1項記載の混合燃料3、 水の世が、
0.1〜20重量%である特許請求の範囲第1項記載の
混合燃料 4、 油が、重油または原油である特許請求の範囲第1
項記載の混合燃料 5、 石炭と油の混合割合が、重量比で3/7〜7/3
である特許請求の範囲第1項記載の混合燃料[Scope of Claims] 1. Mixed fuel made from coal, oil, water, and ultra wIIIM childlike silica. 2. The amount of particulate silica is 0.1 to 10% by weight, according to claim 1. Mixed fuel 3, the world of water,
Mixed fuel 4 according to claim 1, wherein the oil is 0.1 to 20% by weight.Claim 1, wherein the oil is heavy oil or crude oil.
Mixed fuel 5 described in Section 5, the mixing ratio of coal and oil is 3/7 to 7/3 by weight
The mixed fuel according to claim 1 which is
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56106857A JPS588794A (en) | 1981-07-10 | 1981-07-10 | Mixed fuel |
AU84275/82A AU552664B2 (en) | 1981-05-29 | 1982-05-28 | Stabilized coal/oil/water slurry |
CA000403992A CA1180554A (en) | 1981-05-29 | 1982-05-28 | Mixed fuels |
DE8282104739T DE3274258D1 (en) | 1981-05-29 | 1982-05-28 | Mixed fuels |
EP82104739A EP0066817B1 (en) | 1981-05-29 | 1982-05-28 | Mixed fuels |
US06/383,922 US4511364A (en) | 1981-05-29 | 1982-06-01 | Mixed fuels |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56106857A JPS588794A (en) | 1981-07-10 | 1981-07-10 | Mixed fuel |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS588794A true JPS588794A (en) | 1983-01-18 |
JPS648679B2 JPS648679B2 (en) | 1989-02-14 |
Family
ID=14444249
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56106857A Granted JPS588794A (en) | 1981-05-29 | 1981-07-10 | Mixed fuel |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS588794A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP7494644B2 (en) | 2020-08-20 | 2024-06-04 | 富士電機株式会社 | Electrostatic Precipitator |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5573787A (en) * | 1978-11-30 | 1980-06-03 | Babcock Hitachi Kk | Modification of ash component in crude of heavy oil |
-
1981
- 1981-07-10 JP JP56106857A patent/JPS588794A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5573787A (en) * | 1978-11-30 | 1980-06-03 | Babcock Hitachi Kk | Modification of ash component in crude of heavy oil |
Also Published As
Publication number | Publication date |
---|---|
JPS648679B2 (en) | 1989-02-14 |
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