JPS631441B2 - - Google Patents
Info
- Publication number
- JPS631441B2 JPS631441B2 JP13895379A JP13895379A JPS631441B2 JP S631441 B2 JPS631441 B2 JP S631441B2 JP 13895379 A JP13895379 A JP 13895379A JP 13895379 A JP13895379 A JP 13895379A JP S631441 B2 JPS631441 B2 JP S631441B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- ammonia
- pressure
- working fluid
- heat
- 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
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 37
- 239000012530 fluid Substances 0.000 claims description 27
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 18
- 229910021529 ammonia Inorganic materials 0.000 claims description 18
- 239000000203 mixture Substances 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 24
- 239000007789 gas Substances 0.000 description 11
- 238000010521 absorption reaction Methods 0.000 description 6
- 238000009835 boiling Methods 0.000 description 6
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 5
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 235000011114 ammonium hydroxide Nutrition 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 230000000704 physical effect Effects 0.000 description 4
- 229910000881 Cu alloy Inorganic materials 0.000 description 3
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 3
- 229910052753 mercury Inorganic materials 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- 125000004430 oxygen atom Chemical group O* 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 125000004433 nitrogen atom Chemical group N* 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 239000000908 ammonium hydroxide Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010494 dissociation reaction Methods 0.000 description 1
- 230000005593 dissociations Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- -1 hydroxide ions Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 229910052701 rubidium Inorganic materials 0.000 description 1
- IGLNJRXAVVLDKE-UHFFFAOYSA-N rubidium atom Chemical compound [Rb] IGLNJRXAVVLDKE-UHFFFAOYSA-N 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Landscapes
- Lubricants (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Description
【発明の詳細な説明】
本発明は熱機関に使用される作業流体に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to working fluids used in heat engines.
従来廃熱を利用しようとするシステムとしては
ランキンサイクルを基礎とした二流体結合タービ
ンがある。それは水蒸気の飽和圧力の低過ぎるこ
とによつて生ずる廃気末端のふくれあがる廃気を
始末するため、フレオン、アンモニア、ヘリウ
ム、炭化水素等のガスを作業流体とすることが提
案されこのうち実機関としてはフレオンが使用さ
れている。 A conventional system that attempts to utilize waste heat is a two-fluid coupled turbine based on the Rankine cycle. In order to dispose of the swelling waste gas at the end of the exhaust gas caused by the saturation pressure of water vapor being too low, it has been proposed to use gases such as freon, ammonia, helium, and hydrocarbons as working fluids. Freon is used.
又、ランキンサイクル機関として200℃以上で
の炭酸ガスの効率面の優位性を利用しようとする
考えもある。 There is also an idea to utilize the superior efficiency of carbon dioxide gas at temperatures above 200°C as a Rankine cycle engine.
しかしこれ等の作業流体は常温・常圧下では気
相であり使用目的も異なるので熱機関には使用す
ることは出来ない。又高温タービンとしての臨界
温度が有利であるとして水銀、ナトリウム、カリ
ウム、ルビジウム等の液体、金属を作業流体とし
た二流体サイクルタービンが考えられており実機
関としては水銀が使用されているが水銀による各
金属の腐蝕がはげしく問題となつている。 However, these working fluids are in the gas phase at normal temperature and pressure, and their purpose of use is different, so they cannot be used in heat engines. In addition, two-fluid cycle turbines are being considered that use liquids and metals such as mercury, sodium, potassium, and rubidium as working fluids because of their advantageous critical temperature as a high-temperature turbine.In actual engines, mercury is used, but mercury Corrosion of various metals due to this has become a serious problem.
其の他熱の超伝導を計ることを目的としたヒー
トパイプが研究されている。しかしヒートパイプ
中に使用される有機無機の作動流体は本発明のよ
うな圧力を作るための作業流体ではない。尚太陽
熱発電を目的としてクローズドシステム機関とし
てアセトンH3COCH3を熱媒体とするものが発明
されているがアセトンは100℃で2797.3mmHgを示
し圧力を得るための熱媒体としては適当とは考え
難い。従つて作流流体の物性として具備する条件
は
(1) 少ない吸熱によつて高圧が得られること
(2) 常温・常圧で速やかに凝結すること
(3) 着火し難いこと
(4) 腐蝕性が少ないこと
(5) 湿り蒸気の発生が少ないこと
等である。 In addition, heat pipes are being researched to measure heat superconductivity. However, the organic and inorganic working fluid used in the heat pipe is not a working fluid for creating pressure as in the present invention. A closed system engine using acetone H 3 COCH 3 as a heating medium has been invented for the purpose of solar power generation, but acetone has a temperature of 2797.3 mmHg at 100°C, so it is difficult to think of it as suitable as a heating medium for obtaining pressure. . Therefore, the physical properties of the working fluid must be (1) high pressure can be obtained with little heat absorption, (2) rapid condensation at normal temperature and pressure, (3) difficulty in ignition, and (4) corrosivity. (5) There is little generation of wet steam.
次に複合サイクル機関に適応した作業流体とし
て有望な分子の分子量から検討してみる。水素
H2の分子量は2.016、窒素N2は28.01、酸素O2は
32.00、メチルアルコールCH3OH32.04、エチル
エーテルC2H5OC2H5は74.12、アンモニアNH3は
17.03、水H2Oは18である。先ず水素原子2、酸
素原子1からなる水は化学結合の強い安定した不
活性な分子である。それは100〜1000℃の熱い水
分子の過程を経なければ酸素と水素に分解され難
い。水の熱解離は1000℃で0.027%、1800℃で0.6
%、2000℃で1.8%、2800℃で15%程度となる。
一方窒素原子1に対して活性に考えられる水素原
子3からなるアンモニアの分子量は17.03であり
分子量18の水に対して大きな差はない。アンモニ
アは常温20℃のもとで8.46atmを掛ければ容易に
液化されて常温1atmで既に窒素と水素に分解し
ている。このことは水に対してアンモニアがわず
かな吸熱によつて膨大にふくれあがり大きなガス
圧が得られることを意味している。アンモニアは
よく知られているようにアルカリ性を示してい
る。このことは水に溶けたアンモニアNH3の一
部が水と化合して水酸化アンモニアNH3+H2O
NH4OHとなり、そして水酸化アンモニウムは
次のように電離して水酸イオンを放つていること
になる。NH4OHNH4 ++OH-これは水よりも
分子量が少ないにもかかわらずいくぶん低い沸点
を示しアンモニアよりも非常に高い沸点を持つア
ンモニア水となる。そして作業流体(化合物)と
して熱すれば活性と考えられるアンモニア分子が
水分子より押し出され容易に高圧ガスとして得ら
れ低温となれば水の性質が勝り速やかに凝結され
良好な物性を持つ作業流体となる。しかしアンモ
ニアは銅合金に対して炭酸ガス、水蒸気、アンモ
ニアの混合気相中では腐蝕性を示し且つ快削性を
持つ銅合金は結晶の断層にそつて水素脆性を与え
るので使用熱機関の銅合金部分を鉄系に変更しな
くてはならない。次にメチルアルコールの沸点は
64.65℃であり、100℃で2598mmHgの圧を示す。
腐蝕性もなく常温で使用できる溶媒としての作業
流体であるが引火性があるので使用機関の状態を
考え水の添加量を考慮しなければならない。次に
エチルエーテルは沸点34.5℃であり100℃で4855
mmHgを示し作業流体として少し低い沸点を有し
ているのでアルコール類(メチルアルコール等)
と混合して使用しなくてはならないが金属への腐
蝕性がなく良好な作業流体となる。しかし引火性
が強いので水の添加を考慮しなくてはならない。
次にメチルアルコールにアンモニア10〜20%を添
加した溶解物は各分子の物性により沸点は50℃前
後となりそれを作業流体とすれば最高の圧が得ら
れる。しかし引火性があるので若干の水を添加す
る必要があり又金属への腐蝕も考慮しなくてはな
らない。Sクラウジウス、サデイ・カルノー等の
理論と水の物性を基本として発展を続けている、
熱機関の中でランキンサイクル機関は現在も天井
知らずの高温下に於いて作業流体を高圧で使用す
る傾向がある。しかし簡単に考えれば熱機関に必
要なのは温度ではなく圧であり常温・常圧
(1atmで50℃以下)で液相を示しわずかな吸熱に
よつて高圧が得られる作業流体があればよいとい
うことになる。従つてこのような考えを基に開発
された本発明の作業流体をオツト・ランキン複合
サイクル機関に使用すれば水では得られなかつた
高効率の熱気関が得られることになる。 Next, we will consider the molecular weight of molecules that are promising as working fluids suitable for combined cycle engines. hydrogen
The molecular weight of H2 is 2.016, nitrogen N2 is 28.01, oxygen O2 is
32.00, methyl alcohol CH 3 OH 32.04, ethyl ether C 2 H 5 OC 2 H 5 74.12, ammonia NH 3
17.03, water H2O is 18. First, water, which consists of two hydrogen atoms and one oxygen atom, is a stable and inert molecule with strong chemical bonds. It is difficult to decompose into oxygen and hydrogen without going through the process of hot water molecules at 100 to 1000 degrees Celsius. Thermal dissociation of water is 0.027% at 1000℃ and 0.6 at 1800℃
%, 1.8% at 2000℃, and about 15% at 2800℃.
On the other hand, the molecular weight of ammonia consisting of 3 hydrogen atoms, which is considered to be active with respect to 1 nitrogen atom, is 17.03, which is not much different from water, which has a molecular weight of 18. Ammonia can be easily liquefied by applying 8.46 atm at room temperature of 20°C, and has already decomposed into nitrogen and hydrogen at room temperature of 1 atm. This means that ammonia swells to a large extent due to a small amount of heat absorption relative to water, creating a large gas pressure. As is well known, ammonia is alkaline. This means that part of the ammonia NH 3 dissolved in water combines with water to form ammonia hydroxide NH 3 + H 2 O.
It becomes NH 4 OH, and ammonium hydroxide ionizes and releases hydroxide ions as shown below. NH 4 OHNH 4 + +OH - This results in aqueous ammonia, which has a somewhat lower boiling point than water, but has a much higher boiling point than ammonia, although it has a lower molecular weight than water. When heated as a working fluid (compound), ammonia molecules, which are considered to be active, are pushed out from water molecules and easily obtained as a high-pressure gas.When the temperature is low, the properties of water prevail and it condenses quickly, creating a working fluid with good physical properties. Become. However, ammonia is corrosive to copper alloys in a mixed gas phase of carbon dioxide gas, water vapor, and ammonia, and copper alloys with free machining properties exhibit hydrogen embrittlement along crystalline fault lines, so copper alloys used in heat engines are Some parts must be changed to iron. Next, the boiling point of methyl alcohol is
64.65℃, showing a pressure of 2598mmHg at 100℃.
Although it is a working fluid as a solvent that is not corrosive and can be used at room temperature, it is flammable, so the amount of water to be added must be determined in consideration of the conditions of the engine in which it will be used. Next, ethyl ether has a boiling point of 34.5℃ and 4855 at 100℃
mmHg and has a slightly lower boiling point as a working fluid, so alcohols (such as methyl alcohol)
Although it must be used in combination with other materials, it is not corrosive to metals and is a good working fluid. However, since it is highly flammable, consideration must be given to adding water.
Next, a melt of methyl alcohol with 10 to 20% ammonia added has a boiling point of around 50°C depending on the physical properties of each molecule, and if this is used as the working fluid, the highest pressure can be obtained. However, it is flammable, so it is necessary to add some water, and corrosion to metal must also be taken into consideration. It continues to develop based on the theories of S Clausius, Sadej Carnot, etc. and the physical properties of water.
Among heat engines, Rankine cycle engines still tend to use working fluids at high pressures and at sky-high temperatures. However, if you think about it simply, what is needed for a heat engine is not temperature but pressure, and all that is needed is a working fluid that exhibits a liquid phase at room temperature and pressure (below 50 degrees Celsius at 1 atm) and can obtain high pressure by absorbing a small amount of heat. become. Therefore, if the working fluid of the present invention developed based on this idea is used in an Otto-Rankine combined cycle engine, a highly efficient hot air flow that cannot be obtained with water will be obtained.
其の他熱吸収によつて得られる多くの原動機に
利用すれば低温度燃焼によつて効率よく得られる
熱エネルギー変換にとどまらず低温度燃焼による
ボイラ等の排煙中のNOxの成生量も少なくなる。 In addition, when used in many prime movers that obtain heat absorption, it not only converts thermal energy efficiently through low-temperature combustion, but also reduces the amount of NOx produced in flue gas from boilers, etc. due to low-temperature combustion. It becomes less.
ここで本発明の作業流体及びこれと対比すべき
他のいくつかの作業流体が吸熱によつて得られる
圧力について次に示されるようなガス圧試験機に
よつて各作業流体の試験を行なつた。その仕様は
作業流体用タンク300×35φ×4.0tmm鉄製、バン
ドヒーター内径35φ×40b200W×4個温度計0〜
400℃(神鋼電機製)圧力計0〜150Kg/cm2(東京
計器製)である。実測されて作られた第1図の作
業流体の比較線図中水が吸熱することによつて得
られる曲線は日本機械学会の蒸気表からみちびか
れたものではなく実測によるゲージ圧である。又
比較試験であるからゲージ誤差は考慮されていな
い。試験結果は第1図に示される通りである。こ
のうち本発明の作業流体であるメタノールにアン
モニアを12%混合したものの特性については広島
県立西部工業技術センターにおいて実施された同
様の試験によつて確認されている。(広西工技第
1320号)
しかし、ここで注目すべきことは水(分子量
18)とアンモニア12%からなるアンモニア水(分
子量17.884)の作業流体が吸熱によつて得られる
圧力は水よりもむしろ少ない分子量をもつアンモ
ニア水の方が高い圧力を示していることである。 Here, the working fluid of the present invention and several other working fluids to be compared with this were tested for the pressures obtained by heat absorption using a gas pressure tester as shown below. Ta. The specifications are: working fluid tank 300 x 35φ x 4.0tmm made of iron, band heater inner diameter 35φ x 40b 200W x 4, thermometer 0~
400°C (manufactured by Shinko Denki) and a pressure gauge of 0 to 150 Kg/cm 2 (manufactured by Tokyo Keiki). The curve obtained by water absorbing heat in the comparison diagram of working fluids in Figure 1, which was actually measured, is not derived from the steam table of the Japan Society of Mechanical Engineers, but is based on actually measured gauge pressure. Also, since this was a comparative test, gauge errors were not taken into consideration. The test results are shown in FIG. Among these, the properties of the working fluid of the present invention, which is a mixture of methanol and ammonia at 12%, were confirmed in a similar test conducted at the Hiroshima Prefectural Western Industrial Technology Center. (Guangxi Technology No.
1320) However, what should be noted here is that water (molecular weight
18) and ammonia water (molecular weight 17.884) consisting of 12% ammonia due to endothermic action, ammonia water, which has a lower molecular weight, shows a higher pressure than water.
気体の大きな熱膨脹の差については気体になり
やすい物質の分子が持つ原子構造によるものと考
えられる。 The large difference in thermal expansion of gases is thought to be due to the atomic structure of the molecules of substances that easily become gases.
たとえば8個の電子からなる酸素原子1個と、
1個の電子からなる水素原子2個で構成されてい
る水に対し、7個の電子からなる窒素原子1個
と、1個の電子からなる水素原子3個で構成され
ているアンモニアの原子結合(相互引力)を比べ
てみると明らかにアンモニアよりも多い電子から
なる酸素原子の方が2個の水素原子に及ぼす相互
引力は強い。 For example, one oxygen atom consisting of eight electrons,
Atomic bond between water, which consists of two hydrogen atoms each consisting of one electron, and ammonia, which consists of one nitrogen atom consisting of seven electrons, and three hydrogen atoms consisting of one electron. When comparing the (mutual attraction), it is clear that the mutual attraction exerted on two hydrogen atoms by the oxygen atom, which has more electrons, is stronger than that of ammonia.
即ち水はアンモニアより膨脹し難いことにな
る。 In other words, water is more difficult to expand than ammonia.
このように原子結合によつて生ずる分子結合の
相互引力の差が各分子の吸熱によつて得られる熱
膨脹の差となると考えられる。 It is thought that the difference in mutual attraction between molecular bonds caused by atomic bonds is the difference in thermal expansion obtained by endothermic absorption of each molecule.
第1図は本発明の作業流体及び水が吸熱によつ
て得られる圧力変化の実測曲線図である。
FIG. 1 is an actual measurement curve diagram of pressure changes obtained by heat absorption in the working fluid and water of the present invention.
Claims (1)
チルアルコールCH3OHに若干のアンモニアNH3
を添加した作業流体。1 The composition of the working fluid used in heat engines is methyl alcohol CH 3 OH and some ammonia NH 3
Working fluid with added.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13895379A JPS5669409A (en) | 1979-10-26 | 1979-10-26 | Combined otto-rankine cycle engine and working fluid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13895379A JPS5669409A (en) | 1979-10-26 | 1979-10-26 | Combined otto-rankine cycle engine and working fluid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5669409A JPS5669409A (en) | 1981-06-10 |
| JPS631441B2 true JPS631441B2 (en) | 1988-01-12 |
Family
ID=15234012
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13895379A Granted JPS5669409A (en) | 1979-10-26 | 1979-10-26 | Combined otto-rankine cycle engine and working fluid |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5669409A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9915381B2 (en) | 2012-07-13 | 2018-03-13 | Crompton Technology Group Limited | Composite tube |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2421996A (en) * | 2004-12-08 | 2006-07-12 | Philip Morrack Hosken | Steam power source |
| DE102008005040A1 (en) * | 2008-01-18 | 2009-07-23 | Daimler Ag | Method for recovering a heat loss of an internal combustion engine |
-
1979
- 1979-10-26 JP JP13895379A patent/JPS5669409A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9915381B2 (en) | 2012-07-13 | 2018-03-13 | Crompton Technology Group Limited | Composite tube |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5669409A (en) | 1981-06-10 |
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