JPS595230B2 - Vapor reflux device - Google Patents

Vapor reflux device

Info

Publication number
JPS595230B2
JPS595230B2 JP12973776A JP12973776A JPS595230B2 JP S595230 B2 JPS595230 B2 JP S595230B2 JP 12973776 A JP12973776 A JP 12973776A JP 12973776 A JP12973776 A JP 12973776A JP S595230 B2 JPS595230 B2 JP S595230B2
Authority
JP
Japan
Prior art keywords
cooler
paper
gasoline
gas
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
Application number
JP12973776A
Other languages
Japanese (ja)
Other versions
JPS53137204A (en
Inventor
三次 種市
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP12973776A priority Critical patent/JPS595230B2/en
Publication of JPS53137204A publication Critical patent/JPS53137204A/en
Publication of JPS595230B2 publication Critical patent/JPS595230B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は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、ガソリンの
みを貯蔵タンクに還流する装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for recovering evaporated gasoline (paper) from a storage tank installed at a gas station or the like and returning only the gasoline to the storage tank.

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
に放出されている。
Gasoline naturally evaporates from the storage tank and is constantly released into the atmosphere.

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。
Therefore, collecting paper is very beneficial in terms of both effective use of resources and prevention of pollution.

特にペーパーはタンクローリ−から貯蔵タンクにガソリ
ンを補給する際にタンク内に蓄積すれていたものを含め
て大量に放散されるので、給油時のペーパーをも完全に
回収すればその効果がより一層顕著になる。
In particular, when refilling gasoline from a tank truck to a storage tank, a large amount of paper is released, including what had accumulated in the tank, so the effect will be even more noticeable if paper is completely recovered during refueling. become.

本発明は上記の点に鑑み、通常時に生じるペーパーはも
とより給油時などの特定の時期にも確実にペーパーを液
状のガソリンとして回収することができるペーパー還流
装置を提供することを目的とする。
In view of the above-mentioned points, an object of the present invention is to provide a paper reflux device that can reliably recover paper as liquid gasoline not only during normal times but also at specific times such as during refueling.

上記目的を達成する発明の要旨は、貯蔵タンクから発生
する蒸発ガソリンの回収回路に水分除去用の第1の冷却
器、ガソリン分離用の第2の冷却器および特定の時期に
前記第2の冷却器による冷却後のガスを冷却する第3の
冷却器を設けたことにある。
The gist of the invention to achieve the above object is that a recovery circuit for evaporated gasoline generated from a storage tank includes a first cooler for moisture removal, a second cooler for gasoline separation, and a second cooler for separating gasoline at a specific time. The third cooler is provided to cool the gas after it has been cooled by the cooler.

以下本発明を添付図面を参照しながら詳細に説明する。The present invention will be described in detail below with reference to the accompanying drawings.

第1図において、1は貯蔵タンク内に発生したペーパー
を導入して冷却する1次冷却器、2は2次冷却器であり
、1次冷却器1は水分を除去するためのもので、冷却温
度は一5℃程度に設定する。
In Figure 1, 1 is a primary cooler that introduces and cools the paper generated in the storage tank, 2 is a secondary cooler, and the primary cooler 1 is for removing moisture. Set the temperature to about -5℃.

また、2次冷却器2は1次冷却器1で水滴として第1の
気液分離部3で分離した水分除去後のガスを冷却して液
状のガソリンに戻すためのもので、その冷却温度は一2
5℃以下に設定する。
Further, the secondary cooler 2 is used to cool the gas separated into water droplets in the first gas-liquid separator 3 after water removal in the primary cooler 1 and return it to liquid gasoline, and the cooling temperature is 12
Set the temperature below 5℃.

4は液状のガソリンと空気とを分離する第2の気液分離
部、5は三方弁、6は冷却蓄冷器、7は第3の気液分離
部であり、三方弁5は前記第2の気液分離部4の空気排
出口に連通ずる空気流通管8に挿設してその一方の出口
を大気に連通させ、また他方の出口を冷却蓄冷器6のペ
ーパー人口に接続する。
4 is a second gas-liquid separation section that separates liquid gasoline and air; 5 is a three-way valve; 6 is a cooling regenerator; 7 is a third gas-liquid separation section; It is inserted into an air flow pipe 8 that communicates with the air outlet of the gas-liquid separation section 4, one outlet of which communicates with the atmosphere, and the other outlet of which is connected to the paper tube of the cooling regenerator 6.

冷却蓄冷器6のペーパー人口は後述する熱交換器を介し
て第3の気液分離部7の入口と連通しており、回収ガソ
リンは貯蔵タンクに配管9を通して還流し、空気は中間
に弁10を有する排気管11を経て大気に放出する。
The paper part of the cooling regenerator 6 communicates with the inlet of the third gas-liquid separation section 7 via a heat exchanger to be described later, and the recovered gasoline is returned to the storage tank through a pipe 9, and the air is passed through a valve 10 in the middle. It is discharged into the atmosphere through an exhaust pipe 11 having a diameter.

一方、12は冷媒ガスの流通路に配設した第1の冷媒流
通制腑、13は第2の冷媒流通制御弁であり、これらの
第1.第2の制御弁12,13はある時間間隔で開閉し
て冷媒ガスを間欠的に供給する。
On the other hand, 12 is a first refrigerant flow control valve disposed in the refrigerant gas flow path, and 13 is a second refrigerant flow control valve. The second control valves 12 and 13 open and close at certain time intervals to intermittently supply refrigerant gas.

第1.第2の制屯弁12,13の開閉時間間隔は、1次
、2次冷却器1,2の冷却温度に応じて変化させ、冷却
温度を常に所定の温度に維持する。
1st. The opening/closing time interval of the second control valves 12 and 13 is changed according to the cooling temperature of the primary and secondary coolers 1 and 2, and the cooling temperature is always maintained at a predetermined temperature.

すなわち、絞り弁による冷却器の膨張室への噴射間隔を
調節して温度を側脚する構成としたものである。
That is, the configuration is such that the temperature is controlled by adjusting the interval of injection into the expansion chamber of the cooler using the throttle valve.

14は前記冷却蓄冷器6の冷媒ガス入口の付近に配設し
た弁であり、通常は開放状態とし、冷却蓄冷器6の配置
が不要なとき、あるいは運転停止のときに閉止する。
Reference numeral 14 denotes a valve disposed near the refrigerant gas inlet of the cooling regenerator 6, which is normally open and closed when the cooling regenerator 6 is not required or when the operation is stopped.

また、1次冷却器1.2次冷却器2および冷却蓄冷器6
の冷媒ガス出口は図示しない圧縮機の吸入口に接続する
In addition, the primary cooler 1, the secondary cooler 2, and the cooling regenerator 6
The refrigerant gas outlet of is connected to the suction port of a compressor (not shown).

圧縮機は低圧でよいが、大きな排気量を有することが望
ましく、吸引作用を主とする。
The compressor may have a low pressure, but it is desirable to have a large displacement, and its main function is suction.

圧縮機の排出口から排出した冷媒ガスは加熱器を通過す
る際に冷却し、所要の温度、圧力として前記第1.第2
の制(財)弁12.13および弁14に供給し、いわゆ
るクローズドサイクルの冷却回路を構成する。
The refrigerant gas discharged from the discharge port of the compressor is cooled as it passes through the heater, and is brought to the required temperature and pressure as described above in the first paragraph. Second
It is supplied to the control valves 12, 13 and 14, forming a so-called closed cycle cooling circuit.

前記1次冷却器1は第2図に示すようにフレオンあるい
は液体空気など冷媒を貯える冷媒タンク1aと膨張室1
bとを一体構造とし、タンク1a内にペーパー回収回路
に挿設する熱交換器20を配設するとともに、膨張室1
bに絞り弁(ノズル)21を突出させた構成としている
As shown in FIG. 2, the primary cooler 1 includes a refrigerant tank 1a for storing a refrigerant such as freon or liquid air, and an expansion chamber 1.
A heat exchanger 20 is installed in the tank 1a to be inserted into the paper recovery circuit, and an expansion chamber 1 is integrated with the tank 1a.
It has a configuration in which a throttle valve (nozzle) 21 is protruded from b.

これは2次冷却器についても同様である。This also applies to the secondary cooler.

第3図および第4図は前記冷却蓄冷器6の構造を示すも
のである。
3 and 4 show the structure of the cooling regenerator 6. FIG.

すなわち、外側タンク6a内に支持台6bを介して内側
タンク6cを設置し、置タンク6a、6c間の空間を真
空として、いわゆる真空断熱槽を形成するとともに、内
側タンク6c内にスパイラル状の熱交換器6dおよび環
状の冷媒ガス流通管6eに垂設した冷媒液溜バイブロf
を収納し、さらに不凍液6gを満たしている。
That is, the inner tank 6c is installed inside the outer tank 6a via the support stand 6b, and the space between the placed tanks 6a and 6c is evacuated to form a so-called vacuum insulation tank, and a spiral heat is generated inside the inner tank 6c. A refrigerant reservoir vibrof installed vertically in the exchanger 6d and the annular refrigerant gas distribution pipe 6e.
It is also filled with 6g of antifreeze.

冷媒ガス流通管6eの入口は前記弁14に接続し、出口
は圧縮機の吸入口に接続している。
The inlet of the refrigerant gas flow pipe 6e is connected to the valve 14, and the outlet is connected to the suction port of the compressor.

一方、熱交換器6dは上端口をペーパー流入管6hを介
して外側クンクロa外の前記三方弁5の他方の出口に連
結してその途中に安全弁61を取付け、また下端口をタ
ンク6a外に引出して前記第3の気液分離部7に接続し
ている。
On the other hand, the heat exchanger 6d has an upper end connected to the other outlet of the three-way valve 5 outside the outer tank a through a paper inflow pipe 6h, a safety valve 61 installed in the middle, and a lower end connected to the outside of the tank 6a. It is pulled out and connected to the third gas-liquid separation section 7.

なお、6jは不凍液流入管、6には不凍液排出管、61
は真空排気口、6mは真空弁である。
Note that 6j is an antifreeze inflow pipe, 6 is an antifreeze discharge pipe, and 61 is an antifreeze inflow pipe.
is a vacuum exhaust port, and 6m is a vacuum valve.

次に上記装置によるペーパー還流作用について述べる。Next, the paper reflux effect by the above device will be described.

まず、通常の状態では貯蔵タンク内に常に発生している
ペーパーが1次冷却器1に導入されて熱交換器20を通
る際に冷却され、ペーパー中の水分が水滴となって第1
の気液分離部3で除去される。
First, paper, which is always generated in the storage tank under normal conditions, is introduced into the primary cooler 1 and cooled down as it passes through the heat exchanger 20, and the moisture in the paper becomes water droplets.
is removed in the gas-liquid separation section 3.

水分除去後のペーパーは2次冷却器2に導入され、これ
により液状のガソリンに戻されて第2の気液分離部4で
ガソリンが空気と分離され、配管9を経て貯蔵タンクに
還流される。
The paper after moisture removal is introduced into the secondary cooler 2, where it is returned to liquid gasoline, where the gasoline is separated from air in the second gas-liquid separation section 4, and then returned to the storage tank via piping 9. .

この状態では三方弁5は大気側の出口が開放されており
、分離後の空気は三方弁5を経て大気に放出される。
In this state, the outlet of the three-way valve 5 on the atmosphere side is open, and the separated air is discharged to the atmosphere through the three-way valve 5.

この放出空気はペーパー量が1次および2次冷却器1,
2による処理能力量以下であるため、その中に炭化水素
は殆ど含まれず、公害防止に効果がある。
This discharged air has a paper amount in the primary and secondary coolers 1,
Since the processing capacity is less than the processing capacity of 2, it contains almost no hydrocarbons and is effective in preventing pollution.

このように1次および2次冷却器1,2によりペーパー
の回収処理が行われている間にも冷媒ガスが冷却蓄冷器
6の冷媒ガス流通管6eをその入口で分流して半周波合
流するように流れており、液溜バイブロfの部分で断熱
膨張が生じて冷媒ガスの極一部が液化してバイブロf内
に貯まるとともに、次第に低温となる。
In this way, even while the paper recovery process is being performed by the primary and secondary coolers 1 and 2, the refrigerant gas flows through the refrigerant gas distribution pipe 6e of the cooling regenerator 6 at its inlet and joins in half-frequency waves. Adiabatic expansion occurs in the liquid reservoir vibro f, and a small portion of the refrigerant gas is liquefied and stored in the vibro f, and the temperature gradually decreases.

通常状態は相当長期間継続するので、長い間には冷媒ガ
スの液化による冷却で不凍液かガソリンを液化するのに
十分な低温となり、断熱槽の働きで低温が維持される。
Since the normal state continues for a considerable period of time, the temperature becomes low enough to liquefy antifreeze or gasoline due to cooling by liquefaction of the refrigerant gas, and the low temperature is maintained by the action of the insulation tank.

このような状態にあるとき貯蔵タンクにタンクローリ−
から給油する場合には三方弁5の冷却蓄冷器側の出口を
開放する。
When this condition occurs, a tank truck is placed in the storage tank.
When refueling from the tank, the outlet of the three-way valve 5 on the cooling regenerator side is opened.

その結果、2次冷却器2の冷却によりガソリンと分離さ
れた空気が三方弁5を経て冷却蓄冷器6に導入され、そ
の熱交換器6dを流通する。
As a result, air separated from gasoline by cooling in the secondary cooler 2 is introduced into the cooling regenerator 6 via the three-way valve 5, and flows through the heat exchanger 6d.

このとき、低温の不凍液6gで冷却されるようになる。At this time, it will be cooled with 6g of low-temperature antifreeze.

タンクローリ−から給油する際には多量のペーパーが1
次冷却器1,2次冷却器2に導入されるから、2次冷却
器2でガソリンを全て液状に戻すことが無理となり、第
2の気液分離部4からのガスの中にガソリンが含まれる
When refueling from a tank truck, a large amount of paper is
Since the gasoline is introduced into the secondary cooler 1 and the secondary cooler 2, it becomes impossible for the secondary cooler 2 to return all of the gasoline to a liquid state, and the gas from the second gas-liquid separation section 4 contains gasoline. It will be done.

この分は冷却蓄冷器6において冷却されて液状のガソリ
ンに戻され、第3の気液分離部7で空気と分離されて貯
蔵タンクに還流される。
This amount is cooled in the cooling regenerator 6 and returned to liquid gasoline, separated from air in the third gas-liquid separator 7, and returned to the storage tank.

したがって、ペーパーの大部分が液状のガソリンとして
回収されるとともに、大気汚染が防止される。
Therefore, most of the paper is recovered as liquid gasoline and air pollution is prevented.

しかも、特定の時期だけであるから蓄冷構造とすれば補
助的な冷却力で十分であり、装置の稼動率が高くなる。
Moreover, since it is used only during a specific period, if a cold storage structure is used, supplementary cooling power is sufficient, increasing the operating rate of the device.

なお、上記実施例では三方弁を用いたが、複数の弁を組
合せて切換回路を構成してもよい。
Although a three-way valve is used in the above embodiment, a switching circuit may be constructed by combining a plurality of valves.

以上詳述したように本発明によれば、3段の冷却器を設
けて通常は前の2段の冷却器によりペーパー回収処理を
行い、給油時などの特定の時期だけ3段目の冷却器を回
収処理過程にカロえるので、常にペーパーを確実に回収
し得、資源の有効利用と公害防止の両面で大変有益であ
る。
As described in detail above, according to the present invention, a three-stage cooler is provided, and paper recovery processing is normally performed by the previous two-stage cooler, and only at specific times such as during refueling, the third stage cooler is used. Since paper is added to the collection process, paper can always be reliably collected, which is very beneficial in terms of both effective use of resources and prevention of pollution.

しかも、3段目は冷媒ガス流通路における補助的な冷却
力を利用するため、低コストでの処理が可能となり、ガ
ソリン回収と相俟って経済的な効果を太いに期待できる
などの利点がある。
Moreover, since the third stage utilizes the auxiliary cooling power in the refrigerant gas flow path, it can be processed at low cost, and when combined with gasoline recovery, it can be expected to have significant economic effects. be.

【図面の簡単な説明】[Brief explanation of the drawing]

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図は配管系統図、第2図は冷却器の概略構
成図、第3図および第4図は冷却蓄冷器をその内外側タ
ンクを切欠した状態で示す平面図および側面図である。 1・・・・・・1次冷却器、2・・・・・・2次冷却器
、3・・・・・・第1の気液分離部、4・・・・・・第
2の気液分離部、5・・・・・・三方弁、6・・・・・
・冷却蓄冷器。
The drawings show an embodiment of the paper reflux device according to the present invention, in which Fig. 1 is a piping system diagram, Fig. 2 is a schematic configuration diagram of a cooler, and Figs. 3 and 4 show a cooling regenerator therein. FIG. 6 is a plan view and a side view showing the outer tank in a cutaway state. 1...Primary cooler, 2...Secondary cooler, 3...First gas-liquid separation section, 4...Second gas Liquid separation section, 5... Three-way valve, 6...
・Cooling regenerator.

Claims (1)

【特許請求の範囲】 1 貯蔵タンクから発生する蒸発ガソリンの回収回路に
水分除去用の第1の冷却器、ガソリン分離用の第2の冷
却器および特定の時期に前記第2の冷却器による冷却後
のガスを冷却する第3の冷却器を設けたことを特徴とす
るペーパー還流装置。 2 第2の冷却器による冷却後のガス体流通路に連通先
を大気とするか、または、第3の冷却器とするかを選択
する切換弁を設け、通常は切換弁を大気側に切換え、貯
蔵タンクのガソリン補給時に第3の冷却器側に切換える
ようにした特許請求の範囲第1項記載のペーパー還流装
置。 3 冷媒ガスの流通路に液溜を設けるとともに、この液
溜の部分を断熱構造の容器内に不凍液および第2の冷却
器通流後のガス体を通じる熱交換器と共に収容した特許
請求の範囲第1項または第2項記載のペーパー還流装置
[Claims] 1. A recovery circuit for evaporated gasoline generated from a storage tank includes a first cooler for moisture removal, a second cooler for gasoline separation, and cooling by the second cooler at a specific time. A paper reflux device characterized in that a third cooler is provided to cool the subsequent gas. 2 A switching valve is provided in the gas flow path after cooling by the second cooler to select whether to communicate with the atmosphere or with a third cooler, and normally the switching valve is switched to the atmosphere side. 2. The paper reflux device according to claim 1, wherein the paper reflux device is configured to switch to the third cooler side when the storage tank is refilled with gasoline. 3 Claims in which a liquid reservoir is provided in the flow path of the refrigerant gas, and a portion of this liquid reservoir is housed in a container with an insulating structure together with an antifreeze liquid and a heat exchanger through which the gas body passes through the second cooler. The paper reflux device according to item 1 or 2.
JP12973776A 1976-10-28 1976-10-28 Vapor reflux device Expired JPS595230B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12973776A JPS595230B2 (en) 1976-10-28 1976-10-28 Vapor reflux device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12973776A JPS595230B2 (en) 1976-10-28 1976-10-28 Vapor reflux device

Publications (2)

Publication Number Publication Date
JPS53137204A JPS53137204A (en) 1978-11-30
JPS595230B2 true JPS595230B2 (en) 1984-02-03

Family

ID=15016951

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12973776A Expired JPS595230B2 (en) 1976-10-28 1976-10-28 Vapor reflux device

Country Status (1)

Country Link
JP (1) JPS595230B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005177563A (en) * 2003-12-17 2005-07-07 Mitsubishi Electric Corp Apparatus for recovering vapor of gasoline

Also Published As

Publication number Publication date
JPS53137204A (en) 1978-11-30

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