JPS595229B2 - Vapor reflux device - Google Patents
Vapor reflux deviceInfo
- Publication number
- JPS595229B2 JPS595229B2 JP12973676A JP12973676A JPS595229B2 JP S595229 B2 JPS595229 B2 JP S595229B2 JP 12973676 A JP12973676 A JP 12973676A JP 12973676 A JP12973676 A JP 12973676A JP S595229 B2 JPS595229 B2 JP S595229B2
- Authority
- JP
- Japan
- Prior art keywords
- paper
- gasoline
- cooling
- recovery circuit
- reflux device
- 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
- 238000010992 reflux Methods 0.000 title claims description 10
- 238000001816 cooling Methods 0.000 claims description 23
- 238000011084 recovery Methods 0.000 claims description 18
- 238000003860 storage Methods 0.000 claims description 16
- 239000007788 liquid Substances 0.000 description 20
- 239000003507 refrigerant Substances 0.000 description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 238000009423 ventilation Methods 0.000 description 6
- 238000000926 separation method Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 238000005192 partition Methods 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
【発明の詳細な説明】
本発明&iガソリンスタンドなどに設置された貯蔵タン
クの蒸発ガソリン(ペーパー)を回収、処理してガソリ
ンのみを貯蔵タンクに還流する装置、特にペーパーの冷
却に用いる熱交換器の構造に関する。Detailed Description of the Invention: The present invention &i A device for recovering and processing evaporated gasoline (paper) in storage tanks installed at gas stations, etc., and returning only gasoline to the storage tank, especially a heat exchanger used for cooling the paper. Regarding the structure of
貯蔵タンクからはガソリンが自然に気化して常に大気中
に放出されており、特にタンクローリ−から給油する際
にはタンク内に蓄積されていたものを含めて大量に放散
される。Gasoline naturally evaporates from the storage tank and is constantly released into the atmosphere, and especially when refueling from a tank truck, a large amount of gasoline is released, including the gasoline that had been accumulated in the tank.
気化したガソリン、いわゆるペーパーは資源の浪費とな
るばかりでなく、ペーパーの中の炭化水素は光化学スモ
ッグの一因とみられている。Not only is vaporized gasoline, or paper, a waste of resources, but the hydrocarbons in paper are thought to contribute to photochemical smog.
このため、ペーパーを回収することは資源の有効利用と
公害防止の両面で大変有益であるが、回収しようとする
ペーパーは極めて引火性の強いガソリンであるため、加
圧したり、あるい6コ化学反応を生じるような方法では
危険性があり、安全性にすぐれた回収手段の開発が要望
されている。For this reason, collecting paper is very beneficial in terms of both effective resource use and pollution prevention, but since the paper to be recovered is extremely flammable gasoline, it must be pressurized or Methods that cause reactions are dangerous, and there is a need for the development of safe collection methods.
このような要望に応え得る回収手段としては「ガスを冷
却すると液体になる」という物理的性質を利用すること
が考えられる。As a recovery means that can meet such demands, it is conceivable to utilize the physical property that "gas becomes liquid when cooled."
この回収手段−加圧したり、化学反応を生じないので安
全性が高いが、効率よく液状のガソリンに戻すためには
熱交換率が良く、かつ低コストの熱交換器が必要となる
。This recovery means is highly safe because it does not pressurize or cause chemical reactions, but in order to efficiently return it to liquid gasoline, a low-cost heat exchanger with a good heat exchange rate is required.
そこで、本発明は効率よくペーパーを冷却し得るととも
に、低コストで製作することができる熱交換器を備えた
ペーパー還流装置を提供しようとするものである。Therefore, the present invention aims to provide a paper reflux device equipped with a heat exchanger that can efficiently cool paper and can be manufactured at low cost.
本発明に係るペーパー還流装置64、貯蔵タンクから発
生する蒸発ガソリンの回収回路と冷却回路とを独立回路
とし、冷却回路との間で熱交換を行う回収回路の所定の
位置に、管体内に伝熱性の小球を充填して構成した熱交
換器を挿設したことを特徴とする。The paper reflux device 64 according to the present invention has a recovery circuit for evaporated gasoline generated from a storage tank and a cooling circuit as independent circuits, and a paper reflux device 64 is installed in a pipe body at a predetermined position of the recovery circuit that exchanges heat with the cooling circuit. It is characterized by the insertion of a heat exchanger filled with thermal globules.
以下本発明を図面に示す実施例に基づいて詳細に説明す
る。The present invention will be described in detail below based on embodiments shown in the drawings.
第1図において、1−ガソリンスタンドなどに設置され
る貯蔵タンク、2はこの貯蔵タック1に設けた通気管で
あり、タンク1は一般に地下に設置され、通気管2が地
上に突出している。In FIG. 1, 1 is a storage tank installed at a gas station or the like, and 2 is a ventilation pipe provided in this storage tack 1. The tank 1 is generally installed underground, and the ventilation pipe 2 protrudes above ground.
この通気管2の中間に仕切板3を配設して内部空間を2
・分するとともに、その貯蔵タンク1側からタンク1内
のペーパーを導出し、フィルタ4を介して1次冷却器5
および2次冷却器6に順次流通させる。A partition plate 3 is arranged in the middle of this ventilation pipe 2 to divide the internal space into two.
・At the same time, the paper in the tank 1 is taken out from the storage tank 1 side and passed through the filter 4 to the primary cooler 5.
and the secondary cooler 6 in sequence.
1次冷却器56コ水分を除去するためのもので、冷却温
度6コ一5°C程度に設定する。The 56 primary coolers are for removing moisture, and the cooling temperature is set at about 5°C for each of the 6 primary coolers.
また、2次冷却器6Llペーパー中のガソリンを液体に
戻して空気と分離するためのもので、冷却温度Ll −
25°C以下に設定する。In addition, the secondary cooler 6Ll is used to return the gasoline in the paper to liquid and separate it from the air, and the cooling temperature Ll -
Set the temperature below 25°C.
なお、前記仕切板3は後述する配管の取付板の役目をも
兼ねている。Note that the partition plate 3 also serves as a mounting plate for piping, which will be described later.
7は1次冷却器で水滴とPつたペーパー中の水分を残り
のガス体と分離する第1の気液分離部、86コ水滴を受
ける第1の補助クック、9は2次冷却器で液体に戻され
て第2の気液分離部21において空気と完全に分離され
たガソリン(回収ガソリン)を貯める第2の補助タンク
であり、この第2の補助タンク9は前記通気管2の内部
を通って貯蔵タンク1内に臨む配管10を介して貯蔵タ
ンク1と連通ずる。7 is a primary cooler that separates the water droplets and moisture in the paper from the rest of the gas, 86 is a first auxiliary cook that receives water droplets, and 9 is a secondary cooler that separates the liquid from the remaining gas. This is a second auxiliary tank that stores gasoline (recovered gasoline) that has been returned to the air and is completely separated from air in the second gas-liquid separation section 21. It communicates with the storage tank 1 through a pipe 10 that passes through and faces into the storage tank 1.
すなわち、配管1064仕切板3を貫通してその下端が
貯蔵タンク1内に位置し、他端(上端)が通気管2の管
壁を貫通して第2の補助クック9の吐出口に接続される
。That is, the pipe 1064 passes through the partition plate 3 and its lower end is located in the storage tank 1, and the other end (upper end) passes through the pipe wall of the ventilation pipe 2 and is connected to the discharge port of the second auxiliary cooker 9. Ru.
また、通気管2の上方空間と第2の気液分離部21の空
気排出口とは連結管により接続される。Further, the upper space of the ventilation pipe 2 and the air outlet of the second gas-liquid separation section 21 are connected by a connecting pipe.
一方、11は圧縮機、12は放熱器、13は冷却ファン
、14は圧力クッション用タンク、156J第1の冷媒
派通制仰弁、16は第1の絞り弁(調節弁)、17は1
次冷却器5の冷却温度を検出する第1の温度検出器、1
8は第2の冷媒流通側(財)弁、19(ツ第2の絞り弁
、20は2次冷却器6の冷却温度を検出する第2の温度
検出器であり、これらは1次冷却器5.2次冷却器6と
共に前述のペーパー回収回路から独立した冷却回路を構
成している。On the other hand, 11 is a compressor, 12 is a radiator, 13 is a cooling fan, 14 is a pressure cushion tank, 156J is a first refrigerant distribution control valve, 16 is a first throttle valve (control valve), and 17 is a 1
a first temperature detector for detecting the cooling temperature of the secondary cooler 5;
8 is a second refrigerant flow side valve, 19 is a second throttle valve, and 20 is a second temperature detector that detects the cooling temperature of the secondary cooler 6; 5. Together with the secondary cooler 6, it constitutes a cooling circuit independent from the paper recovery circuit described above.
すなわち、1次冷却器56′;i第2図および第3図に
示すようにフレオノあるい一液体空気などの冷媒を貯え
る冷媒タンク5aと膨張室5bとを一体構造とし、冷媒
タック5a内にペーパー回収回路に挿設する熱交換器2
2を配設するとともに、膨張室5bに第1の絞り弁16
の噴出口16aを突出させたものであり、第1の温度検
出器17の感温筒17a、圧力計接続口21などを有す
る。That is, as shown in FIGS. 2 and 3, the primary cooler 56' has a refrigerant tank 5a for storing a refrigerant such as Freon or liquid air, and an expansion chamber 5b in an integral structure, and the refrigerant tuck 5a is Heat exchanger 2 installed in the paper recovery circuit
2 and a first throttle valve 16 in the expansion chamber 5b.
It has a protruding spout 16a, a temperature sensing cylinder 17a of the first temperature detector 17, a pressure gauge connection port 21, etc.
熱交換器22Gコスパイラル状に形成した30mmφ程
度の管体22aに熱伝導率の高い材質の小球、例えば8
〜12mmφの鋼球22bを充填し、その出口の部分に
小孔22cを有する阻止板22dを配設して鋼球22b
の移動を阻止する構成とし、支持円筒22ec!:クッ
ク5aの内周面との間に挟持している。Heat exchanger 22G Small balls made of a material with high thermal conductivity, for example, 8
The steel balls 22b are filled with steel balls 22b having a diameter of ~12 mm, and a blocking plate 22d having a small hole 22c is disposed at the outlet of the steel balls 22b.
The supporting cylinder 22ec! is configured to prevent movement of the supporting cylinder 22ec! : It is held between the inner peripheral surface of the cooker 5a.
阻止板22clその図示左方の第1の気液分離部7側か
ら支持棒22fで支えている。The blocking plate 22cl is supported by a support rod 22f from the first gas-liquid separating section 7 side on the left side in the figure.
また、前記第1の冷媒流通側脚弁15は所要の時間間隔
て開閉して間欠的に冷媒ガスを供給するためのものであ
り、その時間間隔は第1の温度検出器17の検出出力に
応じて自動的に設定し、常に冷却温度を一5℃程度に維
持させる。Further, the first refrigerant flow side leg valve 15 is opened and closed at required time intervals to supply refrigerant gas intermittently, and the time interval is determined by the detection output of the first temperature detector 17. The cooling temperature is automatically set to maintain the cooling temperature at around -5°C.
なお、前記支持筒22e−下部周壁に多数の貫通孔を設
けて筒内外の冷媒液を流通自在としており、またタンク
5aの底部に液排出口5cおよびガス排出口5dを設け
ている。Note that a large number of through holes are provided in the lower peripheral wall of the support tube 22e to allow the refrigerant liquid to freely flow inside and outside the tube, and a liquid outlet 5c and a gas outlet 5d are provided at the bottom of the tank 5a.
このような冷却器の構成および冷却温度の制菌は2次冷
却器6でも略同様であり、冷却温度を一25°C以下の
温度に設定する点が異なる。The structure of such a cooler and the bactericidal control of the cooling temperature are substantially the same for the secondary cooler 6, except that the cooling temperature is set at -25°C or less.
なお、前記圧縮機11は低圧でよいが、大きな排気量を
有することが好ましく、吸引作用を主とする。Note that the compressor 11 may have a low pressure, but preferably has a large displacement, and mainly has a suction effect.
次に上記装置のペーパー還流作用について述べる。Next, the paper reflux function of the above device will be described.
まず、冷却回路では圧縮機11の運転により1次冷却器
5および2次冷却器6の冷媒タック5a、6aから冷媒
ガスが圧縮機11内に吸引され、ここからある圧力(低
圧)で排出されて放熱器12を通過する際に冷却される
。First, in the cooling circuit, when the compressor 11 is operated, refrigerant gas is sucked into the compressor 11 from the refrigerant tacks 5a and 6a of the primary cooler 5 and the secondary cooler 6, and is discharged from there at a certain pressure (low pressure). and is cooled when passing through the radiator 12.
冷却後圧力クッション用タンク14を経て第1.第2の
冷媒流通側脚弁15,18の入口側に達し、各側脚弁1
5.18の間欠的な開閉動作に伴い第1.第2の絞り弁
16.19を介して膨張室5b、6b内に噴出される。After cooling, it passes through the pressure cushion tank 14 to the first. It reaches the inlet side of the second refrigerant flow side leg valves 15 and 18, and each side leg valve 1
Due to the intermittent opening/closing operation of 5.18, the first. It is injected into the expansion chambers 5b, 6b via the second throttle valve 16.19.
この噴出により断熱膨張が行われて低温低圧となり、冷
媒クック5a、6aの冷媒液が低温となる。This jetting causes adiabatic expansion, resulting in low temperature and low pressure, and the refrigerant liquid in the refrigerant cooks 5a, 6a becomes low temperature.
この冷媒液の温度が第1.第2の温度検出器17.20
により各々検出され、設定温度との差に応じて第1.第
2の側脚弁15゜18の開閉時間間隔が調節される。The temperature of this refrigerant liquid is the first. Second temperature sensor 17.20
The first temperature is detected according to the difference from the set temperature. The opening and closing time interval of the second leg valve 15.degree. 18 is adjusted.
これにより1次冷却器5および2次冷却器6の冷却温度
が所定値に維持される。Thereby, the cooling temperatures of the primary cooler 5 and the secondary cooler 6 are maintained at predetermined values.
一方、貯蔵タンクL内のペーパーは通気管2の途中から
導出され、フィルタ4を介して1次冷却器5内に流入す
る。On the other hand, the paper in the storage tank L is led out from the middle of the ventilation pipe 2 and flows into the primary cooler 5 via the filter 4.
この1次冷却器5ではペーパーは上方から下方へと管体
22a内の小球22bの間隙を流通し、この流通過程に
おいてその広い伝熱面積による低温の冷媒液との熱交換
により冷却されて?jttiMガス中の水分が水滴とな
る。In this primary cooler 5, the paper flows from the top to the bottom through the gap between the small balls 22b in the tube body 22a, and during this flow process, the paper is cooled by heat exchange with the low-temperature refrigerant liquid due to its large heat transfer area. ? The moisture in the jttiM gas becomes water droplets.
ペーパー6J上方から下方へとFrL通されているため
、下部(出口側)に6J水分が貯ることになる。Since the FrL is passed through the paper 6J from above to below, 6J water will accumulate in the lower part (outlet side).
すなわち気体はより長い時間管体22a内に滞留するが
液体は下部へと流れ去る。That is, the gas stays in the tube 22a for a longer time, but the liquid flows away to the bottom.
こうして液体(ペーパー)は十分に冷却されて完全な水
分除去がなされ、液化され得ない成分のみが出口にまで
達する。In this way, the liquid (paper) is sufficiently cooled and water is completely removed, and only the components that cannot be liquefied reach the outlet.
このように効率よく、より完全な液化が行われるのであ
る。In this way, more efficient and complete liquefaction is achieved.
水滴は第1の気液分離部7でガスと分離されて第1の補
助タンク8に滴下し、ガスのみが2次冷却器6に流入す
る。The water droplets are separated from the gas in the first gas-liquid separator 7 and drip into the first auxiliary tank 8, and only the gas flows into the secondary cooler 6.
この2次冷却器6でも1次冷却器5と同様にペーパーの
冷却が行われるが、冷却温度が低いため、今度はペーパ
ーが液化して気化して空気と分離され、液状のガソリン
は第2の補助タック9に貯えられる。This secondary cooler 6 also cools the paper in the same way as the primary cooler 5, but since the cooling temperature is low, the paper liquefies and vaporizes and is separated from the air, and the liquid gasoline is transferred to the second cooler 6. is stored in the auxiliary tack 9.
この回収ガソリンの量が一定量以上になると、配管10
を経て貯蔵タンク1に還流される。When the amount of recovered gasoline exceeds a certain level, the pipe 10
It is refluxed to storage tank 1 through .
また、ガソリン分離後の空気は通気管2を経て大気中に
放出される。Furthermore, the air after gasoline separation is discharged into the atmosphere through the vent pipe 2.
この放出空気中には炭化水素は殆ど含まれていない。This emitted air contains almost no hydrocarbons.
すなわち、ペーパーの回収回路には全く圧力を加えず、
しかも触媒による化学反応も利用せず、単に温度条件と
平衡蒸気圧のみの関係で処理、回収することになる。In other words, no pressure is applied to the paper recovery circuit;
Furthermore, no chemical reaction using a catalyst is used, and the process and recovery are performed based solely on the relationship between temperature conditions and equilibrium vapor pressure.
この場合、ペーパー6」管体22a内に充填した小球2
2bの間隙を、いわゆる細管の長経路を通るような形で
流通して水滴や液状のガソリンに戻り、このガソリンの
みが極めて高い回収効率で貯蔵タンク1内に還流される
ようになり、大きな経済効果が得られる。In this case, the paper 6" small balls 2 filled in the tube body 22a
2b through the long path of a thin tube and return to water droplets and liquid gasoline, and only this gasoline is returned to the storage tank 1 with extremely high recovery efficiency, resulting in great economic savings. Effects can be obtained.
以上詳述したように本発明によるペーパー還流装置(コ
、ペーパー回収回路とクローズドサイクルの冷却回路と
で構成し、かつ冷却器に内設する熱交換器を管体内に小
球を充填して構成し、温度条件と平衡蒸気圧のみの関係
で処理、回収するので、熱交換器の製作が簡単で低コス
トになるとともに、小形の割に6J熱交換率が高くなる
。As described in detail above, the paper reflux device (1) according to the present invention is composed of a paper recovery circuit and a closed cycle cooling circuit, and the heat exchanger installed inside the cooler is constructed by filling small spheres in the tube. However, since the heat exchanger is processed and recovered based only on the relationship between temperature conditions and equilibrium vapor pressure, the production of the heat exchanger is simple and low cost, and the 6J heat exchange rate is high despite its small size.
しかも、安全性にすぐれ、かつ回収効率が高くなり、資
源の有効利用と公害防止の両面で大変有益である。Moreover, it has excellent safety and high recovery efficiency, which is very beneficial in terms of both effective use of resources and prevention of pollution.
また、熱交換器において、ペーパーを上方から下方へと
流通させるように回収回路を配置したので、より効率高
く、完全な液化作用を行うことができる。Further, in the heat exchanger, the recovery circuit is arranged so that the paper flows from the top to the bottom, so that more efficient and complete liquefaction can be performed.
図面は本発明によるペーパー還流装置の一実施例を示す
もので、第1図は全体の配管系統図、第2図および第3
図61冷却器の平面図および一部破断状態の側面図であ
る。
1・・・・・・貯蔵タンク、2・・・・・・通気管、3
・・・・・・仕切板、5・・・・・・1次冷却器、5a
・・・・・・冷媒タンク、5b・・・・・・膨張室、6
・・・・・・2次冷却器、7・・・・・・第1の気液分
離部、8・・・・・・第1の補助タンク、9・・・・・
・第2の補助タンク、10・・・・・・配管、11・・
・・・・圧縮機、12・・・・・・放熱器、15・・・
・・・第1の冷媒5rL通制岬弁、16・・・・・・第
1の絞り弁、17・・・・・・第1の温度検出器、18
・・・・・・第2の冷媒流通制御□□弁、19・・・・
・・第2の絞り弁、20・・・・・・第2の温度検出器
、21・・・・・・第2の気液分離部、22・・・・・
・熱交換器、22a・・・・・・管体、22b・・・・
・・小球、22c・・・・・・阻止板。The drawings show an embodiment of the paper reflux device according to the present invention, and FIG. 1 is an overall piping system diagram, and FIGS.
FIG. 61 is a plan view and a partially cutaway side view of the cooler. 1...Storage tank, 2...Vent pipe, 3
...Partition plate, 5...Primary cooler, 5a
... Refrigerant tank, 5b ... Expansion chamber, 6
...Secondary cooler, 7...First gas-liquid separation section, 8...First auxiliary tank, 9...
・Second auxiliary tank, 10...Piping, 11...
...Compressor, 12...Radiator, 15...
...First refrigerant 5rL flow control cape valve, 16...First throttle valve, 17...First temperature detector, 18
...Second refrigerant flow control valve, 19...
...Second throttle valve, 20...Second temperature detector, 21...Second gas-liquid separation section, 22...
・Heat exchanger, 22a...Pipe body, 22b...
...Small ball, 22c...Block plate.
Claims (1)
冷却回路とを独立回路とし、冷却回路との間で熱交換を
行う回収回路の所定の位置に、管体内に伝熱性の小球を
充填して構成した熱交換器を挿設したことを特徴とする
ペーパー還流装置。 2 熱交換器をペーパー回収回路の2個所に挿設し、前
段で水分を除去し、後段でガソリンを液化するような冷
却温度とした特許請求の範囲第1項記載のペーパー還流
装置。 3 貯蔵タンクから発生する蒸発ガソリンの回収回路と
冷却回路とを独立回路とし、冷却回路との間で熱交換を
行う回収回路の所定位置に熱交換器を挿設し、この熱交
換器において蒸発ガソリンが上方から下方へと流通する
ように回収回路を配置したことを特徴とするペーパー還
流装置。[Scope of Claims] 1. A recovery circuit for evaporated gasoline generated from a storage tank and a cooling circuit are independent circuits, and a heat conductive tube is installed in a pipe at a predetermined position of the recovery circuit that exchanges heat with the cooling circuit. A paper reflux device characterized by having a heat exchanger filled with small balls inserted therein. 2. The paper reflux device according to claim 1, wherein heat exchangers are inserted at two locations in the paper recovery circuit, and the cooling temperature is such that moisture is removed in the first stage and gasoline is liquefied in the second stage. 3. A recovery circuit for evaporated gasoline generated from a storage tank and a cooling circuit are made independent circuits, and a heat exchanger is inserted at a predetermined position in the recovery circuit that exchanges heat with the cooling circuit. A paper reflux device characterized in that a recovery circuit is arranged so that gasoline flows from above to below.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12973676A JPS595229B2 (en) | 1976-10-28 | 1976-10-28 | Vapor reflux device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12973676A JPS595229B2 (en) | 1976-10-28 | 1976-10-28 | Vapor reflux device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS53137203A JPS53137203A (en) | 1978-11-30 |
| JPS595229B2 true JPS595229B2 (en) | 1984-02-03 |
Family
ID=15016926
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12973676A Expired JPS595229B2 (en) | 1976-10-28 | 1976-10-28 | Vapor reflux device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS595229B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7081938B1 (en) | 1993-12-03 | 2006-07-25 | Semiconductor Energy Laboratory Co., Ltd. | Electro-optical device and method for manufacturing the same |
-
1976
- 1976-10-28 JP JP12973676A patent/JPS595229B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7081938B1 (en) | 1993-12-03 | 2006-07-25 | Semiconductor Energy Laboratory Co., Ltd. | Electro-optical device and method for manufacturing the same |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS53137203A (en) | 1978-11-30 |
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