JPS6238115Y2 - - Google Patents
Info
- Publication number
- JPS6238115Y2 JPS6238115Y2 JP8008283U JP8008283U JPS6238115Y2 JP S6238115 Y2 JPS6238115 Y2 JP S6238115Y2 JP 8008283 U JP8008283 U JP 8008283U JP 8008283 U JP8008283 U JP 8008283U JP S6238115 Y2 JPS6238115 Y2 JP S6238115Y2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- fuel
- vaporizer
- liquid fuel
- vaporized
- 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
- 239000007788 liquid Substances 0.000 claims description 38
- 239000000446 fuel Substances 0.000 claims description 31
- 239000007789 gas Substances 0.000 claims description 30
- 239000006200 vaporizer Substances 0.000 claims description 26
- 239000002737 fuel gas Substances 0.000 claims description 13
- 239000002828 fuel tank Substances 0.000 claims description 11
- 238000010438 heat treatment Methods 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 239000003915 liquefied petroleum gas Substances 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 235000020681 well water Nutrition 0.000 description 1
- 239000002349 well water Substances 0.000 description 1
Landscapes
- Feeding And Controlling Fuel (AREA)
Description
【考案の詳細な説明】
この考案は、液化石油ガス（LPG）等の液体燃
料をベーパライザで気化させ、これにより得た燃
料ガスをボイラー等の負荷側へ供給する装置の改
良に関する。[Detailed Description of the Invention] This invention relates to an improvement in a device that vaporizes liquid fuel such as liquefied petroleum gas (LPG) using a vaporizer and supplies the resulting fuel gas to the load side of a boiler or the like.
従来のこの種装置は、第１図に示すように、燃
料タンクＴとベーパライザＶとを液体燃料送給管
１で連通接続し、燃料タンクＴ内の液体燃料２を
ベーパライザＶへ送給し、該ベーパライザＶで液
体燃料２を気化させ、これにより得た燃料ガスを
供給管３で負荷側Ｌへ供給するように構成されて
おり、図中４は供給管３に介装された開閉バル
ブ、５はベーパライザＶへ蒸気等の熱源を供給す
るための熱媒体送給管、６は同排出管を夫々示し
ている。 As shown in FIG. 1, a conventional device of this type connects a fuel tank T and a vaporizer V through a liquid fuel supply pipe 1, and supplies liquid fuel 2 in the fuel tank T to the vaporizer V. The liquid fuel 2 is vaporized in the vaporizer V, and the fuel gas obtained thereby is supplied to the load side L through the supply pipe 3. In the figure, 4 indicates an on-off valve installed in the supply pipe 3; Reference numeral 5 indicates a heat medium feed pipe for supplying a heat source such as steam to the vaporizer V, and reference numeral 6 indicates a discharge pipe thereof.
しかしながら、このような従来の燃料ガス供給
装置によるときは、ベーパライザＶで液体燃料２
を即時気化させるため、負荷側Ｌに燃料ガスを供
与しないときでも、ベーパライザＶを予め所要温
度まで予熱しておかねばならず、このため蒸気等
の熱媒体を常時供給しておくことになつて、ラン
ニングコストが嵩み、しかも液体燃料２がそのま
まベーパライザＶへ送られ、これを気化させねば
ならないため、そのための熱媒体にも多量の熱エ
ネルギーが要求され、この結果、当該加熱のため
にも蒸気発生等に多くの商用エネルギーが消費さ
れることとなり、前記ランニングコストと相俟つ
て、装置全体の稼動効率が低く、かつ稼動費が著
るしく嵩むという問題を有していた。 However, when using such a conventional fuel gas supply device, the vaporizer V supplies liquid fuel 2.
In order to vaporize immediately, the vaporizer V must be preheated to the required temperature even when fuel gas is not supplied to the load side L, and therefore a heat medium such as steam must be constantly supplied. , the running cost is high, and since the liquid fuel 2 must be directly sent to the vaporizer V and vaporized, a large amount of thermal energy is also required for the heating medium, and as a result, a large amount of thermal energy is required for the heating. A large amount of commercial energy is consumed for steam generation, etc., which, together with the running cost, causes problems such as low operating efficiency of the entire device and a significant increase in operating costs.
この考案は、かかる問題を解決すべく創案され
たものであつて、その目的とするところは、LPG
等の液体燃料ガス供給装置において、商用エネル
ギーの消費量を大幅に低減でき、これによりラン
ニングコストを低減することができる構成簡易に
して取扱い至便なものを提供しようとするにあ
る。 This invention was devised to solve this problem, and its purpose is to
It is an object of the present invention to provide a liquid fuel gas supply device such as the above, which has a simple structure and is easy to handle, which can significantly reduce commercial energy consumption and thereby reduce running costs.
以下、第２図に示す実施例にもとづき、この考
案を詳細に説明する。 This invention will be explained in detail below based on the embodiment shown in FIG.
閉成される燃料タンクＴには、LPG等の液体燃
料２が収容されており、同燃料２の表面より上方
には、同燃料２からの自然気化ガスによる気相部
１２が形成されることになる。 A liquid fuel 2 such as LPG is stored in the fuel tank T to be closed, and a gas phase portion 12 is formed above the surface of the fuel 2 by naturally vaporized gas from the fuel 2. become.
この燃料タンクＴには、液体燃料２をベーパラ
イザＶ側へと送給する液体燃料送給管１と、同タ
ンクＴの気相部１２に開口されて、その気化ガス
をベーパライザＶ側へと送給する気化ガス送給管
１１とが各別に連通接続されており、さらに同各
管１，１１の他端間には、所定設定圧（約２Kg／
cm2Ｇ程度）で各管１，１１を開閉制御をする気液
自動切換弁１０が接続されており、同切換弁１０
の切換出口側には、ガイド管１３を介してベーパ
ライザＶの入口側が連通接続されている。 This fuel tank T includes a liquid fuel feed pipe 1 that feeds liquid fuel 2 to the vaporizer V side, and a liquid fuel feed pipe 1 that is opened to a gas phase portion 12 of the tank T to send the vaporized gas to the vaporizer V side. The vaporized gas feed pipes 11 to be supplied are connected to each other separately, and a predetermined set pressure (approximately 2 kg/
cm2
The inlet side of the vaporizer V is connected to the switching outlet side of the vaporizer V via a guide pipe 13 .
また、さらにベーパライザＶの出口側は開閉バ
ルブ４を介設した供給管３により、ボイラー等の
負荷側Ｌに連通接続され、同ベーパライザＶには
熱交換媒体たる常温水（例えば井戸水（約15℃）
を導入する熱媒体送給管５と、これを排出する熱
媒体排出管６とが接続されており、同各管５，６
を通じて常温水はベーパライザＶ内を回流するこ
とで液体燃料２を加温気化させ得る構成となつて
いる。 Further, the outlet side of the vaporizer V is connected to the load side L of a boiler etc. through a supply pipe 3 with an on-off valve 4 interposed therebetween, and the vaporizer V is connected to the load side L of a boiler etc. )
A heat medium feed pipe 5 that introduces the heat medium and a heat medium discharge pipe 6 that discharges the heat medium are connected.
By circulating room temperature water through the vaporizer V, the liquid fuel 2 can be heated and vaporized.
そこで今、上記実施例による装置を稼動し、負
荷側Ｌへ燃料ガスを供与する際には、先ず開閉バ
ルブ４を操作して供給管３を開成すると、同管３
は負荷側Ｌを介して大気に開放される。一方、燃
料タンクＴの気相部１２では、液体燃料２が自然
気化して大気圧以上の高圧状態（約５〜７Kg／cm2
Ｇ程度）となつていることから、前記気液自動切
換弁１０は当該気化ガスの圧力にて、前記気液自
動切換弁１０を作動し、これにより気化ガス送給
管１１とガイド管１３とが連通状態にあるから、
同気化ガスは、気化ガス送給管１１−気液自動切
換弁１０−ガイド管１３−ベーパライザＶ−供給
管３−負荷側Ｌの経路にて送給され、従つて前記
の如く開閉バルブ４の開成と同時に、自然気化に
よる燃料ガスが供与されて、負荷側Ｌの需要を充
足できることになり、燃料タンクＴ内は々に減圧
され、従つて液体燃料２は当該降圧に基づき次第
に低温化することになる。 Therefore, when operating the device according to the above embodiment and supplying fuel gas to the load side L, first operate the on-off valve 4 to open the supply pipe 3.
is open to the atmosphere via the load side L. On the other hand, in the gas phase part 12 of the fuel tank T, the liquid fuel 2 is naturally vaporized and is in a high pressure state (approximately 5 to 7 kg/cm 2
G), the gas-liquid automatic switching valve 10 is actuated by the pressure of the vaporized gas, and thereby the vaporized gas supply pipe 11 and the guide pipe 13 are connected to each other. is in communication state,
The vaporized gas is fed through the path of vaporized gas supply pipe 11 - gas-liquid automatic switching valve 10 - guide pipe 13 - vaporizer V - supply pipe 3 - load side L, and therefore, as described above, the on-off valve 4 At the same time as opening, fuel gas is supplied by natural vaporization, and the demand on the load side L can be satisfied, the pressure inside the fuel tank T is gradually reduced, and the temperature of the liquid fuel 2 is gradually lowered based on the pressure reduction. become.
このような気化ガスの供給状態が続くと、これ
による気相部１２の減圧が、前記気液自動切換弁
１０を作動するに至り、かくして気化ガス送給管
１１が閉成して、液体燃料送給管１とガイド管１
３とが連通する状態となるよう自動的に切り換わ
る。それ故、液体燃料２は上記送給管１から上記
弁１０を通りガイド管１３を経てベーパライザＶ
へと導入され、同ベーパライザＶ内に導入される
熱媒体により加温気化される。この実施例では、
前記のように、熱媒体として常温水である例えば
井戸水等を使用したとしても、前記したように、
液体燃料２は燃料タンクＴ内の減圧により低温化
するから、15℃程度の常温水を用いても、液体燃
料２と熱媒体との温度差が大きくなり、この結
果、当該温度勾配により迅速な熱伝導による熱交
換が行なわれ、高温熱媒体でなくとも液体燃料２
を充分気化させることができる。 If such a supply state of vaporized gas continues, the resulting pressure reduction in the gas phase section 12 will operate the gas-liquid automatic switching valve 10, thus closing the vaporized gas feed pipe 11 and discharging the liquid fuel. Feed pipe 1 and guide pipe 1
3 are automatically switched to a state where they are in communication. Therefore, the liquid fuel 2 passes from the feed pipe 1 through the valve 10 and the guide pipe 13 to the vaporizer V.
and is heated and vaporized by the heating medium introduced into the vaporizer V. In this example,
As mentioned above, even if room temperature water such as well water is used as a heat medium, as mentioned above,
Since the temperature of the liquid fuel 2 decreases due to the reduced pressure inside the fuel tank T, even if water at room temperature of about 15°C is used, the temperature difference between the liquid fuel 2 and the heat transfer medium becomes large, and as a result, due to the temperature gradient, the temperature decreases rapidly. Heat exchange is performed by thermal conduction, and liquid fuel 2 does not need to be a high-temperature heat carrier.
can be sufficiently vaporized.
尚、燃料ガスの供給を停止する場合には、開閉
バルブ４を閉操作すればよく、これにより液体燃
料２の送給が停止され、燃料タンクＴの気相部１
２が昇圧して、気液自動切換弁１０が切り換えら
れる。 In addition, when stopping the supply of fuel gas, it is sufficient to close the on-off valve 4, and thereby the supply of liquid fuel 2 is stopped and the gas phase section 1 of the fuel tank T is closed.
2 is increased in pressure, and the automatic gas-liquid switching valve 10 is switched.
この考案は、以上説明したように、閉成された
燃料タンクＴ内の液体燃料２に開口する液体燃料
送給路１と、同タンクＴの気相部１２に開口する
気化ガス送給路１１との間に、気相部１２のガス
圧低下により、気化ガス流通状態から液体燃料流
通状態に切換え作動する気液自動切換弁１０を設
け、当該切換弁１０の切換出口側は、負荷側Ｌと
連結され、かつ熱媒体が供与される熱媒体送給路
５を具備したベーパライザＶに連結するようにし
たものであるからベーパライザＶを予熱しなくと
も、負荷側Ｌにて燃料ガスを使用しようとする際
には、自然気化ガスを有効に利用して需要を充足
することができ、自然気化ガスが稀薄になつて液
体燃料２がベーパライザＶに供給されるようにな
れば、この時点で熱媒体をベーパライザＶに供給
してやれば、前記の如く本考案では、気相部１２
の降圧を利用して液体燃料２を低温化するように
したので、熱媒体に蒸気などの高温エネルギーを
用いず常温水を流入させても、充分な温度勾配に
より液体燃料２を気化させることができ、これに
より商用エネルギーの消費量及び熱媒体の使用量
が大幅に低減され、以つてこの種の装置における
ランニングコストを低廉にすることが可能とな
り、その操作も簡便なものを提供し得る。 As explained above, this invention consists of a liquid fuel feed path 1 that opens to the liquid fuel 2 in the closed fuel tank T, and a vaporized gas feed path 11 that opens to the gas phase portion 12 of the tank T. A gas-liquid automatic switching valve 10 is provided between the gas phase section 12 and the gas-liquid automatic switching valve 10, which switches from the vaporized gas flow state to the liquid fuel flow state due to a drop in gas pressure in the gas phase section 12. The fuel gas can be used on the load side L without preheating the vaporizer V because it is connected to the vaporizer V which is connected to the vaporizer V and is equipped with the heat medium feed path 5 to which the heat medium is supplied. In this case, the natural vaporized gas can be used effectively to meet the demand, and if the natural vaporized gas becomes diluted and the liquid fuel 2 is supplied to the vaporizer V, at this point the heat If the medium is supplied to the vaporizer V, as described above, in the present invention, the gas phase part 12
Since the temperature of the liquid fuel 2 is lowered by using the pressure drop of As a result, the amount of commercial energy consumed and the amount of heat medium used can be significantly reduced, thereby making it possible to lower the running cost of this type of device and providing a simple operation.
第１図は従来の燃料ガス供給装置を示す配管構
成側面説明図、第２図はこの考案に係る燃料ガス
供給装置の配管構成側面説明図である。
１……液体燃料送給管、２……液体燃料、３…
…供給管、１０……気液自動切換弁、１１……気
化ガス送給管、１２……気相部、１３……ガイド
管、Ｌ……負荷側、Ｔ……燃料タンク、Ｖ……ベ
ーパライザ。
FIG. 1 is a side explanatory diagram of the piping configuration of a conventional fuel gas supply device, and FIG. 2 is a side explanatory diagram of the piping configuration of the fuel gas supply device according to this invention. 1...Liquid fuel feed pipe, 2...Liquid fuel, 3...
... Supply pipe, 10 ... Gas-liquid automatic switching valve, 11 ... Vaporized gas supply pipe, 12 ... Gas phase section, 13 ... Guide pipe, L ... Load side, T ... Fuel tank, V ... vaporizer.
Claims (1)
る液体燃料送給路と、同タンクの気相部に開口
する気化ガス送給路との間に、気相部のガス圧
低下により、気化ガス流通状態から液体燃料流
通状態に切換え作動する気液自動切換弁を設
け、当該切換弁の切換出口側は、負荷側と連結
され、かつ熱媒体が供与される熱媒体送給路を
具備したベーパライザに連結するようにした燃
料ガス供給装置。 (2) ベーパライザに供与される熱媒体は、常温水
である実用新案登録請求の範囲第１項記載の燃
料ガス供給装置。[Scope of Claim for Utility Model Registration] (1) Between a liquid fuel feed line that opens to liquid fuel in a closed fuel tank and a vaporized gas feed line that opens to the gas phase of the tank, A gas-liquid automatic switching valve is provided that switches from a vaporized gas distribution state to a liquid fuel distribution state due to a drop in gas pressure in the gas phase, and the switching outlet side of the switching valve is connected to the load side and is supplied with a heat medium. A fuel gas supply device connected to a vaporizer equipped with a heating medium supply path. (2) The fuel gas supply device according to claim 1, wherein the heating medium supplied to the vaporizer is room temperature water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8008283U JPS59186637U (en) | 1983-05-27 | 1983-05-27 | Fuel gas supply device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8008283U JPS59186637U (en) | 1983-05-27 | 1983-05-27 | Fuel gas supply device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59186637U JPS59186637U (en) | 1984-12-11 |
| JPS6238115Y2 true JPS6238115Y2 (en) | 1987-09-29 |
Family
ID=30210073
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8008283U Granted JPS59186637U (en) | 1983-05-27 | 1983-05-27 | Fuel gas supply device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59186637U (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012144208A (en) * | 2011-01-14 | 2012-08-02 | Denso Corp | Cruising range extension device |
-
1983
- 1983-05-27 JP JP8008283U patent/JPS59186637U/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59186637U (en) | 1984-12-11 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4179895A (en) | Cooling system using low potential and high potential energies | |
| JPS6238115Y2 (en) | ||
| JPS6238116Y2 (en) | ||
| JPS6238117Y2 (en) | ||
| JP4273640B2 (en) | Cogeneration system | |
| KR20100132353A (en) | Heating structure of vehicle's vaporator using heat source of exgaust gas | |
| CN104964260B (en) | The device of heat in a kind of utilization high-temperature steam trasfer of solids storage bodies | |
| JPS6124634B2 (en) | ||
| JPH09157667A (en) | Liquefied gas evaporation apparatus of liquified gas carrying vessel | |
| JPH02119061A (en) | Methanol reformer of fuel cell | |
| JPS6234120Y2 (en) | ||
| CN205137068U (en) | Take LNG vaporizer of gas heating | |
| CN218296837U (en) | Air compressor machine waste heat recovery supplies to store up and glues jar heat preservation device | |
| JPS6273033A (en) | Hot water supply system | |
| JPS5824080Y2 (en) | liquefied natural gas vaporizer | |
| CN216620780U (en) | Emergent portable heating system of graphite heat accumulation based on low ebb electricity | |
| JPH0650501A (en) | Heat recovery system for incinerator | |
| JPH0411354U (en) | ||
| JP2561622B2 (en) | Method and apparatus for stable supply of liquefied petroleum gas | |
| JPS63172841A (en) | Hot water feeder | |
| JPS5911279Y2 (en) | Butane gas supply equipment | |
| JP2002139198A (en) | Liquefied gas feeing device | |
| JPS5986800A (en) | Propane gas supply apparatus | |
| JP2000039098A (en) | Evaporating device for bulk container | |
| JPH07254425A (en) | Heat retaining device for piping and equipment in fuel gas system in fuel cell power generation system |