JPS6011995B2 - Production method of altered kerosene - Google Patents
Production method of altered keroseneInfo
- Publication number
- JPS6011995B2 JPS6011995B2 JP11754680A JP11754680A JPS6011995B2 JP S6011995 B2 JPS6011995 B2 JP S6011995B2 JP 11754680 A JP11754680 A JP 11754680A JP 11754680 A JP11754680 A JP 11754680A JP S6011995 B2 JPS6011995 B2 JP S6011995B2
- Authority
- JP
- Japan
- Prior art keywords
- kerosene
- altered
- production method
- acid value
- bpeh
- 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
- 239000003350 kerosene Substances 0.000 title claims description 34
- 238000004519 manufacturing process Methods 0.000 title claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 5
- FVQMJJQUGGVLEP-UHFFFAOYSA-N (2-methylpropan-2-yl)oxy 2-ethylhexaneperoxoate Chemical compound CCCCC(CC)C(=O)OOOC(C)(C)C FVQMJJQUGGVLEP-UHFFFAOYSA-N 0.000 claims description 3
- 150000002978 peroxides Chemical class 0.000 description 11
- 239000002253 acid Substances 0.000 description 10
- 238000000034 method Methods 0.000 description 10
- 239000011347 resin Substances 0.000 description 7
- 229920005989 resin Polymers 0.000 description 7
- 230000004075 alteration Effects 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 6
- 238000012360 testing method Methods 0.000 description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000001678 irradiating effect Effects 0.000 description 1
Landscapes
- Liquid Carbonaceous Fuels (AREA)
Description
【発明の詳細な説明】 本発明は、灯油を変質させた変質油の製造法に関する。[Detailed description of the invention] The present invention relates to a method for producing denatured oil obtained by denaturing kerosene.
Z灯油を燃料とする
燃焼機器の燃焼特性、寿命などを調べるために、促進試
験として変質した灯油を燃焼させて評価する方法が探ら
れる。ここに使用される変質油は、従来、灯油を加熱し
たり、空気を吹き込んだり、紫外線を照射したZり、あ
るいは灯油の劣化する環境に暴露させたりする方法によ
り作成されていた。In order to investigate the combustion characteristics, lifespan, etc. of combustion equipment that uses Z-kerosene as fuel, a method of evaluating the combustion of degraded kerosene as an accelerated test is being explored. The altered oil used here has conventionally been produced by heating kerosene, blowing air into it, irradiating it with ultraviolet rays, or exposing it to an environment that degrades the kerosene.
しかし、これらの方法では、いずれも変質油を得るのに
2週間ないし1年以上も要するなど長時間かかる上に、
再現性に乏しく、また任意の変質度のものが得られない
などの欠点があった。さらに具体的に述べると、試験用
変質灯油を得る方法としては、以下のものが代表的であ
った。However, all of these methods take a long time, from two weeks to more than a year, to obtain altered oil.
There were drawbacks such as poor reproducibility and inability to obtain a desired degree of alteration. More specifically, the following methods were typical for obtaining altered kerosene for testing.
m 180qo以上に加熱して空気を吹き込む。■ 紫
外線を照射して空気を吹き込む。(3} 屋外に放置す
る。Heat to 180 qo or more and blow air into it. ■ Irradiates ultraviolet light and blows air. (3) Leave it outdoors.
【1}、【2}の方法によると、強度の酸価(0.1以
上)の灯油が得られるので、酸価0.01〜0.03の
通常の変質灯油の酸価にするため、希釈して試料として
用いられている。According to methods [1} and [2], kerosene with a strong acid value (0.1 or more) can be obtained, so in order to make the acid value equal to that of ordinary degraded kerosene, which has an acid value of 0.01 to 0.03, It is diluted and used as a sample.
‘3ーの方法では、灯油の設置場所、容器、暴露日数な
どを変える方法が採られる。これらの方法による場合は
、変質させるのに長時間を必要とする上に、作成の都度
変質度が異なるので再現性に乏しく、任意の変質度のも
のが得られなかった。Method 3 involves changing the location of the kerosene, its container, and the number of days of exposure. In the case of these methods, it takes a long time to alter the quality, and the degree of alteration differs each time it is produced, so reproducibility is poor and it is not possible to obtain a product with a desired degree of alteration.
そこで、本発明者らは、以上のような従来の不都合を解
消し、任意の変質度のものを短時間で、再現性良く製造
する方法として、灯油に過酸化物を添加する方法を提案
した(特願昭55−32286)。Therefore, the present inventors proposed a method of adding peroxide to kerosene as a method to eliminate the above-mentioned conventional disadvantages and to produce products of any degree of alteration in a short time and with good reproducibility. (Patent application No. 55-32286).
この方法は、灯油成分と過酸化物とを反応させることに
より、変質灯油を得るものである。本発明者らが市場で
回収された数多くの変質灯油を分析した結果、その大部
分が酸価0.01〜0.0入過酸化物価200〜500
肌、樹脂質量20〜30の9/100のZ灯油であった
。In this method, altered kerosene is obtained by reacting kerosene components with peroxides. As a result of the inventors' analysis of a large number of degraded kerosene collected on the market, most of them had an acid value of 0.01 to 0.0 and a peroxide value of 200 to 500.
It was 9/100 Z kerosene with a resin mass of 20 to 30.
これに対し先に提案した過酸化物添加法では、次表のよ
うに、いずれも市場の変質灯油に近い含有量をもつもの
が得られなかった。On the other hand, with the previously proposed peroxide addition method, as shown in the following table, it was not possible to obtain a product with a content close to that of the modified kerosene on the market.
すなわち表から明らかなようにいずれも樹脂質量が少な
く、醗価、過酸化物価も異なっている。したがって、こ
のような灯油で燃焼試験を行ない、タールが出ないなど
の結果を得ても、市場での変質灯油で同じ結果がでると
は限らない。そこで、本発明者らは市場での変質灯油と
同組成の変質灯油を得るための過酸化物およびその変質
条件を検討した。That is, as is clear from the table, the resin mass is small in all cases, and the alcohol value and peroxide value are also different. Therefore, even if a combustion test is conducted using such kerosene and results are obtained such as no tar being emitted, this does not necessarily mean that the same results will be obtained with degraded kerosene on the market. Therefore, the present inventors investigated peroxides and their alteration conditions in order to obtain altered kerosene having the same composition as altered kerosene on the market.
その結果、t−ブチルパーオキシー2一エチルヘキサノ
ェートを添加することにより、容易に大量の市場での変
質灯油と同組成の合成変質灯油を作成できることを見し
、出した。以下、本発明を実施例により説明する。第1
図は、変質していない正常灯油に1.の重量%のt−ブ
チルパーオキシー2一エチルヘキサノェート(以下BP
EHで表す)を添加し、大気中において各種の温度に加
熱したときの経過時間と灯油中の過酸化物価、酸価およ
び樹脂質量との関係を表したものである。図から明らか
なように、市場で回収された変質灯油の代表的な組成で
ある過酸化物価200〜500脚、酸価0.01〜0.
03、樹脂質量20〜30M/100の‘の変質灯油を
作るには、BPEHの添加量1.の重量%の場合、60
〜70『0で2〜4時間、とくに6530で3時間程度
加熱すればよいことがわかる。As a result, they found that by adding t-butylperoxy-2-ethylhexanoate, it was possible to easily create a synthetic altered kerosene having the same composition as the altered kerosene sold in large quantities on the market. The present invention will be explained below with reference to Examples. 1st
The figure shows normal, unaltered kerosene. of t-butylperoxy-2-ethylhexanoate (hereinafter referred to as BP)
This graph shows the relationship between the elapsed time when kerosene (expressed as EH) was added and heated to various temperatures in the atmosphere, and the peroxide value, acid value, and resin mass in kerosene. As is clear from the figure, the typical composition of degraded kerosene recovered on the market is a peroxide value of 200 to 500, and an acid value of 0.01 to 0.
03. To make altered kerosene with a resin mass of 20 to 30 M/100, the amount of BPEH added is 1. 60 if the weight% of
It can be seen that it is sufficient to heat at 0 to 70 for 2 to 4 hours, especially at 6530 for about 3 hours.
次にBPEHの添加量を変えた例について説明する。Next, an example in which the amount of BPEH added is changed will be explained.
第2図は加熱温度6yo、加熱時間を2時間または3時
間として、BPEHの添加量と過酸化物価、酸価および
樹脂質量の関係を示す。図から明らかなように、BPE
H添加量と変質度はほぼ比例するが、BPEH添加量増
加とともに酸価が著しく進行するため、BPEH添加量
は0.5〜2.の重量%、とくに1重量%が好ましいこ
とがわかる。FIG. 2 shows the relationship between the amount of BPEH added and the peroxide value, acid value, and resin mass when the heating temperature was 6yo and the heating time was 2 hours or 3 hours. As is clear from the figure, BPE
The amount of H added and the degree of alteration are almost proportional, but as the amount of BPEH added increases, the acid value increases significantly, so the amount of BPEH added should be 0.5 to 2. % by weight, particularly 1% by weight.
このように本発明によれば、市場での変質灯油に対応す
る変質組成を有する試験用変質灯油を容易に、かつ再現
性よく、短時間に作成できるため、大量に試験用変質灯
油を必要とする燃焼器の燃焼特性試験や寿命推定、寿命
比較が可能となり、燃焼機器の開発等に大いに役立つも
のである。As described above, according to the present invention, it is possible to easily and reproducibly create a test-grade altered kerosene having an altered composition corresponding to the degraded kerosene on the market in a short time, thereby eliminating the need for a large amount of test-grade altered kerosene. This makes it possible to test the combustion characteristics, estimate the lifespan, and compare the lifespan of combustors, which will be of great help in the development of combustion equipment.
第1図はBPEHを1重量%添加した灯油を各種温度で
加熱したときの経過時間と過酸化物価、酸価、樹脂質量
の関係を示した図、第2図は65ooで加熱したときの
BPEH添力o量と過酸化物価、酸価、樹脂質量の関係
を示した図である。
第1図
第2図Figure 1 shows the relationship between elapsed time, peroxide value, acid value, and resin mass when kerosene containing 1% by weight of BPEH is heated at various temperatures. Figure 2 shows the relationship between BPEH when heated at 65 oo It is a figure showing the relationship between the amount of additive o, peroxide value, acid value, and resin mass. Figure 1 Figure 2
Claims (1)
エートを0.5〜2.0重量%添加し、加熱することを
特徴とする変質灯油の製造法。 2 前記加熱条件が、加熱温度60〜70℃、加熱時間
2〜4時間である特許請求の範囲第1項記載の変質灯油
の製造法。[Scope of Claims] 1. A method for producing altered kerosene, which comprises adding 0.5 to 2.0% by weight of t-butylperoxy-2-ethylhexanoate to kerosene and heating the mixture. 2. The method for producing altered kerosene according to claim 1, wherein the heating conditions are a heating temperature of 60 to 70°C and a heating time of 2 to 4 hours.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11754680A JPS6011995B2 (en) | 1980-08-26 | 1980-08-26 | Production method of altered kerosene |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11754680A JPS6011995B2 (en) | 1980-08-26 | 1980-08-26 | Production method of altered kerosene |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5740590A JPS5740590A (en) | 1982-03-06 |
| JPS6011995B2 true JPS6011995B2 (en) | 1985-03-29 |
Family
ID=14714471
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11754680A Expired JPS6011995B2 (en) | 1980-08-26 | 1980-08-26 | Production method of altered kerosene |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6011995B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6390592A (en) * | 1986-10-06 | 1988-04-21 | Nippon Mining Co Ltd | Fuel composition having high ignitability |
-
1980
- 1980-08-26 JP JP11754680A patent/JPS6011995B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5740590A (en) | 1982-03-06 |
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