JPS6264700A - Thrustor - Google Patents
ThrustorInfo
- Publication number
- JPS6264700A JPS6264700A JP60205076A JP20507685A JPS6264700A JP S6264700 A JPS6264700 A JP S6264700A JP 60205076 A JP60205076 A JP 60205076A JP 20507685 A JP20507685 A JP 20507685A JP S6264700 A JPS6264700 A JP S6264700A
- Authority
- JP
- Japan
- Prior art keywords
- heat exchanger
- heater
- gas
- fixing rod
- nozzle
- 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.)
- Pending
Links
- 239000003380 propellant Substances 0.000 claims description 13
- 238000000354 decomposition reaction Methods 0.000 claims description 9
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 claims description 4
- 238000007599 discharging Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 description 34
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 26
- 238000010438 heat treatment Methods 0.000 description 10
- 230000003197 catalytic effect Effects 0.000 description 9
- 239000003054 catalyst Substances 0.000 description 8
- 238000010586 diagram Methods 0.000 description 5
- 239000002245 particle Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 230000020169 heat generation Effects 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen(.) Chemical compound [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B64—AIRCRAFT; AVIATION; COSMONAUTICS
- B64G—COSMONAUTICS; VEHICLES OR EQUIPMENT THEREFOR
- B64G1/00—Cosmonautic vehicles
- B64G1/22—Parts of, or equipment specially adapted for fitting in or to, cosmonautic vehicles
- B64G1/40—Arrangements or adaptations of propulsion systems
- B64G1/411—Electric propulsion
- B64G1/415—Arcjets or resistojets
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Remote Sensing (AREA)
- Aviation & Aerospace Engineering (AREA)
- Air-Conditioning For Vehicles (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は1例えば人工衛星の軌道制御のため人工衛星
に推力を与えるスラスタに関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a thruster that provides thrust to an artificial satellite for controlling the orbit of the artificial satellite, for example.
第3図は、従来の触媒式スラスタの説明図である。説明
の都合上、推薬としてヒドラジンを用いて以下説明する
。第3図において、(1)は配管、(2)はフィルタ、
(3)は推薬弁、(4)はフィードチューブ。FIG. 3 is an explanatory diagram of a conventional catalytic thruster. For convenience of explanation, the following explanation uses hydrazine as a propellant. In Figure 3, (1) is piping, (2) is filter,
(3) is the propellant valve, and (4) is the feed tube.
+5+ (d 分解チェンバ、(6)はノズル、tts
ハスロート。+5+ (d decomposition chamber, (6) is nozzle, tts
Hasrot.
(l[9はインジェクタ、αηは触媒、Ollはこの触
媒の流出を防止するメツシュでアル。(l[9 is the injector, αη is the catalyst, and Oll is the mesh that prevents the catalyst from flowing out.
従来の触媒式スラスタは、上記のように構成され、推薬
であるヒドラジンは加圧ガスで所定の圧力に加圧されて
配管fi+により供給されており、推薬弁(3)を駆動
信号により開状態にすることによりフィルタ(2)を通
り、推薬弁(3)からフイードチュープ+41を通り分
解チェンバ(5)へ供給される0インジエクタαeは供
給されたヒドラジンを触媒<171に接触させるため噴
霧状態にする。触媒aηに接触したヒドラジンは分解発
熱反応を起こし、アンモニア。The conventional catalytic thruster is configured as described above, and the propellant, hydrazine, is pressurized to a predetermined pressure with pressurized gas and supplied through the piping fi+, and the propellant valve (3) is controlled by a drive signal. By opening the injector αe, which passes through the filter (2) and from the propellant valve (3) through the feed tube +41 to the decomposition chamber (5), brings the supplied hydrazine into contact with the catalyst <171. Make it into a spray state. Hydrazine in contact with the catalyst aη undergoes a decomposition exothermic reaction, producing ammonia.
窒素および水素のガスに分解され、ノズル(6)から宇
宙空間にこの分解ガスを排出することにより推力を得る
ものであった。It was decomposed into nitrogen and hydrogen gas, and thrust was obtained by discharging this decomposed gas into space from a nozzle (6).
スラスタの比推力は、理論上1分解ガスの絶対温度の平
方根に比例し、比推力が高いほど衛星に搭載する必要推
薬量は少なくてすむ。The specific impulse of a thruster is theoretically proportional to the square root of the absolute temperature of the decomposed gas, and the higher the specific impulse, the smaller the amount of propellant required to be carried on the satellite.
上記のような従来の触媒式ヒドラジンスラスタでは、と
ドラジンの分解ガス温度は触媒によるヒドラジンの化学
反応エネルギーに限定され870℃から980℃程度が
限度であり、比推力としては220III!cから24
5wt程度に限定されるという問題点があった。In the conventional catalytic hydrazine thruster as described above, the temperature of the decomposed gas of hydrazine is limited to about 870°C to 980°C due to the chemical reaction energy of hydrazine by the catalyst, and the specific impulse is 220III! c to 24
There was a problem that it was limited to about 5wt.
この発明は、かかる問題点を解決するためになされタモ
ので、ヒドラジンの分解ガスにヒータを用いて熱エネル
ギーを与え2分解ガスの粒子の運動エネルギーを高め、
従来の触媒式ヒドラジンスラスタと比べ高い比推力を得
ることを目的とする〇〔問題点を解決するための手段〕
この発明に係わる電気加熱式スラスタは、触媒によって
分解されたヒドラジンの分解ガスをヒータを内蔵した熱
交換器に分解ガスを通し、ヒータの電気加熱により分解
ガスに熱エネルギーを与え。The present invention was made to solve these problems, and therefore, it provides thermal energy to the decomposed gas of hydrazine using a heater to increase the kinetic energy of the particles of the decomposed gas.
[Means for solving the problem] The electrically heated thruster according to the present invention aims to obtain a higher specific impulse than the conventional catalytic hydrazine thruster. The cracked gas is passed through a heat exchanger with a built-in heat exchanger, and the electrical heating of the heater gives thermal energy to the cracked gas.
分解ガスの粒子の運動エネルギーを高めてからノズルか
ら宇宙空間に分解ガスを排出するようにしたものである
。この発明に係る電気加熱式スラスタの熱交換器は、熱
伝達特性のよい三重円筒形状をした熱交換体の内側にヒ
ータ固定棒に螺旋状にtJつけられたヒータのエレメン
トを備えておシ。This system increases the kinetic energy of the decomposed gas particles before ejecting the decomposed gas from the nozzle into space. The heat exchanger for an electrically heated thruster according to the present invention includes a heater element spirally attached to a heater fixing rod inside a triple cylindrical heat exchanger having good heat transfer characteristics.
分解ガスは、三重円筒形状の外部熱交換体の一端にガス
導入管から供給され、三1円筒形状の外部熱交換体、中
間熱交換体、内部熱交換体およびと−タエレメントを備
えたヒータ固定棒で囲まれた間隙を通過し9円筒形状の
他端側からノズルに排出されるような構造となっている
。The cracked gas is supplied from a gas inlet pipe to one end of the triple-cylindrical external heat exchanger, and the heater is equipped with a triple-cylindrical external heat exchanger, an intermediate heat exchanger, an internal heat exchanger, and a heater element. The structure is such that it passes through a gap surrounded by a fixed rod and is discharged from the other end of the cylindrical shape to a nozzle.
この発明においては、熱交換器に供給されたヒドラジン
の分解ガスの加熱をヒータエレメントによる直接加熱と
ヒータによって放射加熱された三重円筒形状の熱交換体
の外部熱交換体の内表面。In this invention, the decomposition gas of hydrazine supplied to the heat exchanger is heated by direct heating by a heater element and by radiant heating by a heater on the inner surface of an external heat exchanger of a triple-layered cylindrical heat exchanger.
中間熱交換体の内表面及び外表面、内部熱交換体の内表
面及び外表面とヒータによって伝導加熱されたヒータ固
定棒の外表面からの面発熱によって行われるので分解ガ
スと接触する発熱表面積が大きくとれるため熱交換量が
大きくなり2分解ガスが発熱面と接触する時間が長くな
ることから2分解ガスにより多くの熱エネルギーを与え
ることができる。これによって2分解ガスは、多くの熱
エネルギーを得て高温状態になシ22分解ガス粒子の運
動エネルギーは高まりスラスタの比推力の向上がはかれ
る。加熱抵抗ヒータでは、その許容温度の1650℃〜
2000°0程度まで分解ガス温度を昇温させることか
でき、従来の触媒式スラスタと比較して比推力が30チ
〜40%向上させることができる。This is done by surface heat generation from the inner and outer surfaces of the intermediate heat exchanger, the inner and outer surfaces of the internal heat exchanger, and the outer surface of the heater fixing rod that is conductively heated by the heater, so the heat generation surface area that comes into contact with the cracked gas is Since it can be made larger, the amount of heat exchange becomes larger, and the time during which the bicomponent gas is in contact with the heat generating surface becomes longer, so that more thermal energy can be given to the bicomponent gas. As a result, the 2 decomposition gas obtains a large amount of thermal energy and is brought into a high temperature state, increasing the kinetic energy of the 22 decomposition gas particles and improving the specific impulse of the thruster. For heating resistance heaters, the allowable temperature is 1650℃~
The cracked gas temperature can be raised to about 2000°0, and the specific impulse can be improved by 30 to 40% compared to conventional catalytic thrusters.
また、この発明においては、熱又換器が、上記のような
構造となっているので熱交換効率が良(。Further, in this invention, since the heat exchanger has the above-described structure, the heat exchange efficiency is good.
ヒータ加熱に要する電力を少なくすることができるO
〔実施例〕
第1図は、この発明の一実施例を示す説明図である。(
1)〜(6)は、上記従来装置と全く同一のものである
。(7)はガス導入管、(8)はヒータを内蔵した熱交
換器である。The electric power required for heater heating can be reduced. [Embodiment] FIG. 1 is an explanatory diagram showing an embodiment of the present invention. (
1) to (6) are completely the same as the conventional device described above. (7) is a gas introduction pipe, and (8) is a heat exchanger with a built-in heater.
第2図は、この発明の特徴である上記熱交換器(8)の
一実施例の基本構造を示す断面図である。(9)は熱伝
達特性の良い円筒形状をした外部熱交換体。FIG. 2 is a sectional view showing the basic structure of an embodiment of the heat exchanger (8), which is a feature of the present invention. (9) is a cylindrical external heat exchanger with good heat transfer characteristics.
αCは熱伝達特性の良い円筒形状をした中間熱交換体、
αυは熱伝達特性の良い円筒形状をした内部熱交換体、
α2はヒータ固定棒、αJはヒータエレメントで、ヒー
タ固定棒α2に螺旋状に巻かれている。αC is a cylindrical intermediate heat exchanger with good heat transfer characteristics;
αυ is a cylindrical internal heat exchanger with good heat transfer characteristics.
α2 is a heater fixing rod, and αJ is a heater element, which is spirally wound around the heater fixing rod α2.
Iはヒータの電力のリード線、uっけノズルl+31の
スロートである□
上記のように構成された電気加熱式スラスタにおいては
1分解チェンバ(5)において触媒aDによって熱分解
されたヒドラジ/の分解ガスは、ガス導入管(7)で熱
交換器(8)に送られ、外部熱交換体(9)。I is the power lead wire of the heater, and the throat of the U-shaped nozzle L+31. The gas is sent by a gas inlet pipe (7) to a heat exchanger (8) and an external heat exchanger (9).
中間熱交換体Ql、内部熱父換体αυとヒータ固定棒α
りで囲まれた間隙を通過し、スロー)u!19からノズ
ル(6)に排出される。ヒータエレメントa3はリード
線α4を通した電力によって電気的に発熱が行われ。Intermediate heat exchanger Ql, internal heat exchanger αυ and heater fixing rod α
pass through the gap surrounded by 19 and is discharged to the nozzle (6). Heater element a3 electrically generates heat using electric power passed through lead wire α4.
また、ヒータエレメントα3に接しているヒータ固定棒
α2は熱伝導によって加熱され9分解ガスに対して面発
熱が行われる。また、内部熱交換体αυは熱放射によっ
てヒータエレメントα3およびヒータ固定棒α2に加熱
され1分解ガスに対して面発熱が行われる。さらに中間
熱交換体αeと外部熱交換体(9)は熱伝導および熱放
射によって加熱され1分解ガスに対して面発熱が行われ
ることにより分解ガスが接触する発熱表面積が大きくと
れ、熱交換時間を長くとれるので2分解ガスに対する熱
交換量を大きくすることができる。分解ガスは、上記の
ように熱交換器(8)を通過する間に加熱され、高温状
態になってノズル(6)から宇宙空間に排出される。Further, the heater fixing rod α2 in contact with the heater element α3 is heated by thermal conduction, and surface heating is performed on the decomposed gas. Further, the internal heat exchanger αυ is heated by the heater element α3 and the heater fixing rod α2 by thermal radiation, and surface heating is performed for the decomposed gas. Furthermore, the intermediate heat exchanger αe and the external heat exchanger (9) are heated by thermal conduction and thermal radiation, and surface heating is performed for each cracked gas, so that the heating surface area that the cracked gas comes into contact with is large, and the heat exchange time is Since the length can be increased, the amount of heat exchanged with the bicomponent gas can be increased. The decomposed gas is heated while passing through the heat exchanger (8) as described above, becomes high temperature, and is discharged into space from the nozzle (6).
このため、従来の触媒式ヒドラジンスラスタよシも比推
力を高めることができる。Therefore, the specific impulse of the conventional catalytic hydrazine thruster can also be increased.
ところで、上記実施例では、推薬としてヒドラジンを用
いて説明したが、触媒と化学反応を起こす他の推薬を用
いても良いことはいうまでもない。Incidentally, in the above embodiment, hydrazine was used as the propellant, but it goes without saying that other propellants that cause a chemical reaction with the catalyst may be used.
また、スロート住9の位置を軸方向の円筒端面上でなく
てもよい。同様にガス導入管(7)と円筒軸方向面に設
けても同様な動作が期待できる。Moreover, the position of the throat housing 9 does not have to be on the cylindrical end face in the axial direction. Similarly, a similar operation can be expected even if it is provided on the cylindrical axis direction surface with the gas introduction pipe (7).
この発明は1以上説明したとおり、熱伝達特性の良い三
重円筒形状の外部熱交換体、中間熱交換体、内部熱交換
体とヒータエレメントが螺旋状に巻きつけられたヒータ
固定棒の間隙を分解ガスが通過できるという簡単な構造
の熱交換器によって触媒による推薬の分屏ガスをヒータ
を用いて効率良く電気加熱し1分解ガスを高温状態にし
て2分解ガスの粒子の運動エネルギーを高め従来の触媒
式スラスタと比較し比推力を高くでき人工衛星の必要推
薬量を軽減できるという効果がある。As explained above, this invention solves the gap between the heater fixing rod, in which the triple cylindrical external heat exchanger, intermediate heat exchanger, internal heat exchanger, and heater element with good heat transfer characteristics are spirally wound. Using a heat exchanger with a simple structure that allows gas to pass through, the propellant separated by the catalyst is efficiently electrically heated using a heater, and the 1st decomposed gas is brought to a high temperature, which increases the kinetic energy of the 2nd decomposed gas particles. Compared to catalytic thrusters, this has the effect of increasing specific impulse and reducing the amount of propellant required for satellites.
また、この発明の上記の熱交換器は1分解ガスに対する
接触発熱面積が大きくとれ、さらに熱交換時間が長くと
れるために熱交換効率が良く2ヒータ電力を節電できる
という効果がある。Furthermore, the above-mentioned heat exchanger of the present invention has a large catalytic heating area for one cracked gas, and also has a long heat exchange time, resulting in good heat exchange efficiency and the ability to save electric power for two heaters.
【図面の簡単な説明】
第1図は、この発明の一実施例を示すスラスタの説明図
、第2図はこの発明の熱交換器の一実施例の基本構造を
示す断面説明図、第3図は、従来の触媒式ヒドラジンス
ラスタの説明図でめる0図において、(1)は配管、(
2)はフィルタ、(3)は推薬弁、(4)はフィードチ
ューブ、(5)は分解チェンバ。
(6)はノズル、(7)はガス導入管、(8)は熱交換
器、(9)は外部熱交換体、 CIGは中間熱交換体、
(illは内部熱交換体、α2はヒータ固定棒、 Q
3はヒータエレメント、α4はリード線、霞はスロート
、αeはインジェクタ、 Q7)は触媒、a秒はメツシ
ュである。
なお2図中同一符号は同一または相当部分を示すO[Brief Description of the Drawings] Fig. 1 is an explanatory diagram of a thruster showing an embodiment of the present invention, Fig. 2 is an explanatory cross-sectional diagram showing the basic structure of an embodiment of a heat exchanger of the invention, and Fig. 3 The figure is an explanatory diagram of a conventional catalytic hydrazine thruster, in which (1) is the piping;
2) is a filter, (3) is a propellant valve, (4) is a feed tube, and (5) is a decomposition chamber. (6) is a nozzle, (7) is a gas introduction pipe, (8) is a heat exchanger, (9) is an external heat exchanger, CIG is an intermediate heat exchanger,
(ill is the internal heat exchanger, α2 is the heater fixing rod, Q
3 is the heater element, α4 is the lead wire, Kasumi is the throat, αe is the injector, Q7) is the catalyst, and a second is the mesh. Note that the same symbols in the two figures indicate the same or corresponding parts.
Claims (1)
状の外部熱交換体、この外部熱交換体内に位置する円筒
形状の中間および内部熱交換体、上記内部熱交換体内に
設けられたヒータ固定棒、上記ヒータ固定棒の軸方向に
所定の間隔で螺旋状に巻かれたヒータエレメント、上記
熱交換体の一端側に設けられ、上記三つの熱交換体およ
び固定棒に囲まれた間隙に上記分解チェンバにより得ら
れた推薬の分解ガスを注入する注入口、上記熱交換体の
他端側に、分解ガスを外部空間に排出するノズルと対向
して設けられたスロートおよび上記ヒータエレメントに
電力を供給するためのリード線とからなり、上記三つの
熱交換体とヒータ固定棒とで囲まれた間隙に上記分解ガ
スを螺旋させながらノズル側へ通過させる熱交換器と、
この熱交換器のスロートと対向して設けられ、上記熱交
換器からの分解ガスを外部空間へ排出するノズルとを具
備したことを特徴とするスラスタ。a decomposition chamber for catalytically decomposing a propellant, a cylindrical external heat exchanger, a cylindrical intermediate and internal heat exchanger located within the external heat exchanger, and a heater provided within the internal heat exchanger. A fixing rod, a heater element spirally wound at predetermined intervals in the axial direction of the heater fixing rod, and a heater element provided at one end of the heat exchanger and in a gap surrounded by the three heat exchangers and the fixing rod. An inlet for injecting the decomposed gas of the propellant obtained from the decomposition chamber, a throat provided on the other end of the heat exchanger facing a nozzle for discharging the decomposed gas to the outside space, and the heater element. a heat exchanger consisting of a lead wire for supplying electric power and causing the cracked gas to spiral through a gap surrounded by the three heat exchangers and the heater fixing rod and pass toward the nozzle side;
A thruster comprising: a nozzle that is provided facing the throat of the heat exchanger and discharges cracked gas from the heat exchanger to an external space.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60205076A JPS6264700A (en) | 1985-09-17 | 1985-09-17 | Thrustor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60205076A JPS6264700A (en) | 1985-09-17 | 1985-09-17 | Thrustor |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6264700A true JPS6264700A (en) | 1987-03-23 |
Family
ID=16501024
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60205076A Pending JPS6264700A (en) | 1985-09-17 | 1985-09-17 | Thrustor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6264700A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2015517621A (en) * | 2012-05-09 | 2015-06-22 | イーシーエイピーエス・アクチボラグ | Improved reactor for ammonium dinitramide based liquid monopropellant and a thruster including such a reactor |
-
1985
- 1985-09-17 JP JP60205076A patent/JPS6264700A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2015517621A (en) * | 2012-05-09 | 2015-06-22 | イーシーエイピーエス・アクチボラグ | Improved reactor for ammonium dinitramide based liquid monopropellant and a thruster including such a reactor |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP2712084B2 (en) | Heating device for catalyst tube for fuel reforming | |
CA1304581C (en) | Compact hydrogen generator | |
CN103796954B (en) | Ammonia generator and for generation of ammonia to reduce the method for the oxynitride in waste gas | |
US5592521A (en) | Process and device for recombining and/or igniting hydrogen contained in an H2 -air-steam mixture, preferably for nuclear power stations | |
CN110118136B (en) | Thrust-adjustable hydrogen peroxide single-component thruster | |
KR20080110901A (en) | Apparatus for liquid ammonia decomposition in gaseous nitrogen and hydrogen | |
US5485721A (en) | Arcjet for a space flying body | |
JP2009537723A (en) | Method and apparatus for supplying air-fuel mixture | |
JPS61254082A (en) | Power generator utilizing exhaust heat | |
JP3153867B2 (en) | Steam generator | |
US4470258A (en) | Thruster for space vehicles | |
JPS6264700A (en) | Thrustor | |
US6290185B1 (en) | Solar thermal rocket | |
CN109698033B (en) | Carbon-enhanced thermally-activated hydrogen fuel reactor | |
JPS61232370A (en) | Thruster | |
US4517798A (en) | Porous catalytic metal plate degeneration bed in a gas generator | |
US4608821A (en) | Heat exchanger for electrothermal devices | |
JP2572251B2 (en) | Fuel reformer | |
JPS5950865B2 (en) | Thermal propulsion device with super heater | |
JPS63176800A (en) | Electric heating type thruster for artificial satellite | |
US3999380A (en) | Subliming solids gas generator with chemical reaction augmentation | |
JPS62216900A (en) | Electric heating type thruster for artificial satellite | |
WO1990014668A2 (en) | Cold fusion propulsion apparatus and energy generating apparatus | |
WO2023205122A1 (en) | Integrated heaters having nonlinear passageways for heating fluids, and apparatuses incorporating same | |
JPS59216798A (en) | Thruster for artificial satellite |