JPS5817300A - High- or low-temperature material supply system, and supply conduit - Google Patents
High- or low-temperature material supply system, and supply conduitInfo
- Publication number
- JPS5817300A JPS5817300A JP56113717A JP11371781A JPS5817300A JP S5817300 A JPS5817300 A JP S5817300A JP 56113717 A JP56113717 A JP 56113717A JP 11371781 A JP11371781 A JP 11371781A JP S5817300 A JPS5817300 A JP S5817300A
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- pipe
- low
- space
- conduit
- 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
- 238000005192 partition Methods 0.000 claims abstract description 6
- 239000000126 substance Substances 0.000 claims description 7
- 208000011117 substance-related disease Diseases 0.000 claims 1
- 239000003507 refrigerant Substances 0.000 abstract description 14
- 239000007788 liquid Substances 0.000 abstract description 8
- 239000006200 vaporizer Substances 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 3
- 230000008016 vaporization Effects 0.000 abstract description 3
- 238000001816 cooling Methods 0.000 abstract description 2
- 238000009834 vaporization Methods 0.000 abstract 2
- 239000007789 gas Substances 0.000 description 5
- 230000004888 barrier function Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000009413 insulation Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000002513 implantation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16L—PIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
- F16L59/00—Thermal insulation in general
- F16L59/06—Arrangements using an air layer or vacuum
- F16L59/075—Arrangements using an air layer or vacuum the air layer or the vacuum being delimited by longitudinal channels distributed around the circumference of a tube
Landscapes
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Thermal Insulation (AREA)
- Pipeline Systems (AREA)
Abstract
Description
【発明の詳細な説明】
氷見−は低温状態にある液体あるいは気体を供給する冷
媒供給システムおよびその供給システムに用いる導管に
関する。DETAILED DESCRIPTION OF THE INVENTION Himi relates to a refrigerant supply system for supplying liquid or gas at low temperature and to a conduit used in the supply system.
液体窒素(LN、)は蒸着装置、インプランテーシ嘗ン
装置の油拡散真空ポンプの冷媒に用いられている。この
LN、の供給は耐圧容1)(いわゆるマホーヒン)k入
れて供給する方法、あるいは導管内を流して供給する方
法とがある。Liquid nitrogen (LN) is used as a refrigerant for oil diffusion vacuum pumps in evaporation equipment and implantation equipment. This LN can be supplied by charging it into a pressure-resistant capacity 1) (so-called Mahohin) or by flowing it through a conduit.
しかし、従来の耐圧容器による供給では供給効率◆1s
O%以下となってしまさ。また、用役プラントとして二
重パイプを設置し、LN、の流動する外側を真!1にし
て保温しLN、を供給したところ、使用箇所ではLN、
は気化し、冷媒として使用できなかった。これは供給効
率0%に相当する。However, with conventional pressure-resistant containers, the supply efficiency is ◆1s.
It's below 0%. In addition, a double pipe is installed as a utility plant, and the outside where LN flows is connected to the true! When LN was supplied while keeping it warm at 1, LN was used at the point of use.
vaporized and could not be used as a refrigerant. This corresponds to a supply efficiency of 0%.
ここで、供給効率とは下記の弐によるものである。Here, the supply efficiency is based on the following 2.
したがって、本発明の目的は、冷媒液体を使用箇所まで
何部変化しないよう冷却を伴なった保温をしながら供給
するととにあり、液体が昇温したり気化してしまう率を
低下させることにある。Therefore, an object of the present invention is to supply refrigerant liquid to the point where it is used while keeping it warm while cooling it so that it does not change, thereby reducing the rate at which the liquid heats up or vaporizes. be.
このような目的な達成するために本発明は、高温または
低温物質供給源と使用部とを三重以上の構造の供給導管
で連結するとともに、導管の最内部の中心管内に高温ま
たは低温物質を流し、かつ、中心管とその外側の隔雪、
隔管と隔雪、隔管と最外管との間の空間は恒温空間ある
いは使用済の高温または低温物質を流すようにしてなる
ものであって、以下実施例により本発明を説明する。In order to achieve these objectives, the present invention connects a high-temperature or low-temperature substance supply source and a usage part with a supply conduit having a triple or more structure, and also allows the high-temperature or low-temperature substance to flow into a central pipe in the innermost part of the conduit. , and the central canal and its outer septa,
The space between the septum and the septum and between the septum and the outermost tube is a constant temperature space or a space through which used high-temperature or low-temperature substances can flow.The present invention will be explained below with reference to Examples.
第1図は本発明の一実施例による冷媒供給システムを示
す概略図である。同図に示すように、冷媒供給源である
LN、タンク1と、冷媒使用部である各種の装置2群と
は、マニホルド3およびパルプ4を介して導管5で連結
している。この導管5は第2図で示すよ’l、三重構造
の導管となっている。すなわち、中心管6は丸パイプと
なり、この中心管6の搬送空間7内kLN、タンク1か
ら送り出される冷媒(LNりが流れる。中心管6の外側
には三角形断面の角管からなる隔雪8が嵌金されている
。中心管6の外周を形作る円は隔雪8の内周円となって
いる。この隔雪8と中心管6との間の空間は断熱空間(
恒温空間)9を形作り、この実施例では真空化領域とな
り、断熱効果を一層高めている。FIG. 1 is a schematic diagram showing a refrigerant supply system according to an embodiment of the present invention. As shown in the figure, LN and tank 1, which are refrigerant supply sources, and two groups of various devices, which are refrigerant using sections, are connected by a conduit 5 via a manifold 3 and a pulp 4. As shown in FIG. 2, this conduit 5 has a triple structure. That is, the central pipe 6 is a round pipe, and the refrigerant (LN) sent out from the tank 1 flows within the conveying space 7 of the central pipe 6. Outside the central pipe 6, there is a partition 8 made of a square pipe with a triangular cross section. The circle that forms the outer periphery of the center tube 6 is the inner circumference of the snow barrier 8. The space between the snow barrier 8 and the center tube 6 is a heat insulating space (
In this embodiment, a constant temperature space) 9 is formed, which becomes a vacuum area, further enhancing the heat insulation effect.
一方、三角形断連構造の隔雪8の外周円を内周を形作る
円とする最外管10が隔雪8に嵌置されている。この丸
パイプからなる最外管1oと隔雪8との間の空間はリタ
ーン空間11となり、各種装置2で使用済となった冷媒
を流して供給源側に戻す。このリターン空間は戻りパイ
プ12に連通するため、使用済冷媒は気化器13に入る
よ5tCなっている。気化器13はLN!タンク1とも
パイプ14を介して接続されている。また、気化器13
内で気化してN、ガスとなると、とのN1ガスは放出管
阜5から大気中に放出されるか、N。On the other hand, an outermost tube 10 is fitted into the septum 8 having a triangular interrupted structure, with the outer circumference being a circle forming the inner periphery. The space between the outermost pipe 1o made of a round pipe and the partition 8 becomes a return space 11, through which the refrigerant used in the various devices 2 flows and is returned to the supply source side. Since this return space communicates with the return pipe 12, the used refrigerant enters the vaporizer 13 at a temperature of 5 tC. Carburetor 13 is LN! It is also connected to the tank 1 via a pipe 14. In addition, the vaporizer 13
When the N1 gas is vaporized into N and gas, it is released into the atmosphere from the discharge pipe 5.
ガスとして使用するようkなっている。It is designed to be used as a gas.
このような実施例では、LN、タンク1から送り出され
るLN、は搬送空間7を流れて各種装置2に送られ、各
種装置2を冷却する。また、使用済となったLN、(そ
の多くは降温してN、ガスに変化している。)は今度は
最外管1oと隔雪8との間のリターン空間11を流れて
、導管5、特に内側の中心管6の温度上昇を断つ役割を
果しながら気化器13に流れ込む。また、隔雪8と中心
管6との間の断熱空間9は真空化状態にあるため、断熱
効果が高く、外気による中心管6の昇温、すなわち、中
心管6の搬送空間7内を流れるLN。In such an embodiment, the LN, which is sent out from the tank 1, flows through the conveyance space 7 and is sent to the various devices 2 to cool the various devices 2. In addition, the used LN (most of which has cooled and changed to N and gas) now flows through the return space 11 between the outermost pipe 1o and the snow barrier 8, and flows through the conduit 5. In particular, it flows into the vaporizer 13 while playing the role of cutting off the temperature rise in the inner central pipe 6. In addition, since the insulation space 9 between the snow partition 8 and the center pipe 6 is in a vacuum state, the insulation effect is high, and the temperature of the center pipe 6 due to outside air increases. LN.
の気化を防止する。Prevents evaporation.
したがって、この実施例では、冷媒供給源から遠く離れ
た冷媒使用部KLN、を気化させることなく供給できる
ため、供給効率が100%と高くなり、経済性が高くな
る。Therefore, in this embodiment, since the refrigerant can be supplied to the refrigerant-using part KLN far away from the refrigerant supply source without vaporizing it, the supply efficiency is as high as 100%, and the economic efficiency is high.
また、供給導管は中心から偶数番Hの管が多角形状の角
管となっていること、また、この角管の内周円あるいは
外周円を内径あるいは外径とする円管としていることか
ら、製作が容易である。In addition, since the supply conduit is a polygonal square tube with an even number H from the center, and it is a circular tube whose inner diameter or outer diameter is the inner circumference or outer circumference of this square tube, Easy to manufacture.
なお、氷見、明、は前記実施例Vcl11%定されない
。すなわち、隔雪をさらに増加させて、三重を越える多
重供給導管としてもよい。また、恒温空間、戻り空間は
交互にあるいは連続するように配設してもよい。Incidentally, Himi and Akira are not determined in the above-mentioned Example Vcl11%. That is, the number of alternate snows may be further increased to provide multiple supply conduits of more than three layers. Further, the constant temperature space and the return space may be arranged alternately or consecutively.
また、本発明では冷媒のような低温物質以外K。In addition, in the present invention, K other than low-temperature substances such as refrigerants.
高温物質を供給するよ5Kしてもよい。It is also possible to supply a high temperature substance for 5K.
第1因は本発明の一実施例による概略図、第2図は同じ
く断間図である。
16.・LN、タンク、2・・・装置、3・−・マニホ
ルド、5・・・導管、6・・・中心管、8・・・隔雪、
1o・・・最外管、13・・・気化器。The first factor is a schematic diagram according to an embodiment of the present invention, and FIG. 2 is a cutaway diagram as well. 16.・LN, tank, 2... device, 3... manifold, 5... conduit, 6... central pipe, 8... alternate snow,
1o... outermost tube, 13... vaporizer.
Claims (1)
用部とを三重以上の多重構造の供給導管で連結するとと
もに、供給導管の最内部の中心管内に高温または低温物
質を流し、かつ中心管とその外側の隔管、隔管と隔管、
隔管と最外管との間の空間は恒温空間あるいは使用済の
高温または低温物質を流すようにしてなる高温または低
温物質供給システム。 1 三重以上の多重構造の導管であって、中心から偶数
II目の管は多角形断Nの角管となりていることを特徴
とする供給導管。[Claims] 1. A high-temperature or low-temperature substance supply source and a high-temperature or low-temperature substance use section are connected by a supply conduit with a multilayer structure of three or more layers, and the high-temperature or low-temperature substance is placed in the innermost central pipe of the supply conduit. A sink, and a central pipe and a septum on the outside, a septum and a septum,
The space between the partition tube and the outermost tube is a constant temperature space or a high temperature or low temperature material supply system through which used high temperature or low temperature materials flow. 1. A supply conduit which is a conduit having a multilayer structure of three or more layers, wherein the even-numbered II-th tube from the center is a square tube with a polygon cross section of N.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56113717A JPS5817300A (en) | 1981-07-22 | 1981-07-22 | High- or low-temperature material supply system, and supply conduit |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56113717A JPS5817300A (en) | 1981-07-22 | 1981-07-22 | High- or low-temperature material supply system, and supply conduit |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5817300A true JPS5817300A (en) | 1983-02-01 |
Family
ID=14619353
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56113717A Pending JPS5817300A (en) | 1981-07-22 | 1981-07-22 | High- or low-temperature material supply system, and supply conduit |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5817300A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05141599A (en) * | 1991-11-13 | 1993-06-08 | Mitsubishi Heavy Ind Ltd | Transportation method for liquified natural gas |
WO1995007434A1 (en) * | 1993-09-10 | 1995-03-16 | Teisan K.K. | Pipe arrangement for low temperature fluid |
-
1981
- 1981-07-22 JP JP56113717A patent/JPS5817300A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05141599A (en) * | 1991-11-13 | 1993-06-08 | Mitsubishi Heavy Ind Ltd | Transportation method for liquified natural gas |
WO1995007434A1 (en) * | 1993-09-10 | 1995-03-16 | Teisan K.K. | Pipe arrangement for low temperature fluid |
JPH0783398A (en) * | 1993-09-10 | 1995-03-28 | Teisan Kk | Piping equipment for low temperature fluid |
US5557925A (en) * | 1993-09-10 | 1996-09-24 | Teisan K.K. | Piping installation for low temperature fluid |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US5390500A (en) | Cryogenic fluid vaporizer system and process | |
KR101314294B1 (en) | Efficient heat exchanger for refrigeration process | |
US4523637A (en) | System for the refrigeration of liquids and/or gases | |
JPS62188899A (en) | Conveyor system of coolant | |
US6578629B1 (en) | Application of heat pipe science to heating, refrigeration and air conditioning systems | |
US3293871A (en) | Cryogenic vaporizer | |
JPS5817300A (en) | High- or low-temperature material supply system, and supply conduit | |
CN105765320B (en) | System and method for cryogenic refrigeration | |
JP2001182894A (en) | Forced circulation type air-temperature liquefied gas vaporizer and method of vaporazing liquefied gas | |
CN205351842U (en) | Cooling cycle system and refrigeration plant | |
JPH0648146B2 (en) | Double pipe type open rack type vaporizer | |
US4566284A (en) | Method and apparatus to upgrade the capacity of ambient-air liquid cryogen vaporizers | |
EP0100554A2 (en) | Process for cooling and fluidizing | |
JPH03229100A (en) | Vaporizer for cryogenic liquefied gas | |
US4289197A (en) | Heat exchanger | |
JPS63254611A (en) | Superconductive distributing line | |
CN218937103U (en) | Fixed air temperature carburetor with ice melting device | |
US4178774A (en) | Absorption refrigeration apparatus | |
CN1237303C (en) | Apparatus and method for transfering cryogenic fluid | |
JPH05118728A (en) | Supercooler for supercooled water manufacturing device | |
CN216048612U (en) | System for use cryogenic liquids system subcooled water | |
JPH06313687A (en) | Liquefied natural gas vaporizer using accumulated cold heat | |
JPH08338692A (en) | Open rack type vaporizer | |
CN207881540U (en) | The loop heat pipe of micro-channel structure auxiliary drive | |
JPH0689879B2 (en) | Air temperature / hot water combined LPG air gas production plant |