JPS6238116Y2 - - Google Patents
Info
- Publication number
- JPS6238116Y2 JPS6238116Y2 JP8324083U JP8324083U JPS6238116Y2 JP S6238116 Y2 JPS6238116 Y2 JP S6238116Y2 JP 8324083 U JP8324083 U JP 8324083U JP 8324083 U JP8324083 U JP 8324083U JP S6238116 Y2 JPS6238116 Y2 JP S6238116Y2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- fuel
- liquid fuel
- vaporizer
- liquid
- 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 44
- 239000000446 fuel Substances 0.000 claims description 36
- 239000007789 gas Substances 0.000 claims description 32
- 239000006200 vaporizer Substances 0.000 claims description 27
- 239000002737 fuel gas Substances 0.000 claims description 14
- 239000002828 fuel tank Substances 0.000 claims description 11
- 238000010438 heat treatment Methods 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 238000001514 detection method Methods 0.000 claims description 3
- 239000012071 phase Substances 0.000 description 12
- 239000003915 liquefied petroleum gas Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 235000020681 well water Nutrition 0.000 description 2
- 239000002349 well water Substances 0.000 description 2
- 238000005265 energy consumption Methods 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により負荷側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 by 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、これにより稼動
効率を向上し、かつ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
We aim to provide a liquid fuel gas supply device with a simple configuration and easy handling that can significantly reduce commercial energy consumption, thereby improving operating efficiency and reducing running costs. It is in.
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
熱交換媒体たる常温水（例えば井戸水約15℃）を
導入するための熱媒体送給管５には、電磁バルブ
等による自動開閉バルブ１４が介装されており、
ベーパライザＶ内にて熱交換を終つた熱媒体は、
熱媒体排出管６から排出される。 Furthermore, the outlet side of the vaporizer V is connected to the load side L of a boiler or the like through a supply pipe 3 with an on-off valve 4 interposed therebetween, and the vaporizer V is supplied with room temperature water (for example, well water of about 15°C) as a heat exchange medium. An automatic opening/closing valve 14 such as a solenoid valve is installed in the heat medium feed pipe 5 for introducing the heat medium.
The heat medium that has completed heat exchange in the vaporizer V is
The heat medium is discharged from the heat medium discharge pipe 6.
ここで上記自動開閉バルブ１４は、前記した液
体燃料送給管１に介装された圧力計等による圧力
検知素子１５と接続されてON−OFF制御される
ものである。 Here, the automatic opening/closing valve 14 is connected to a pressure sensing element 15 such as a pressure gauge installed in the liquid fuel feed pipe 1, and is controlled to be turned on and off.
つまり、圧力検知素子１５は、予め定めてある
所定圧力値よりも、液体燃料送給管１内の液圧が
低下するに至つたとき信号を発して、自動開閉バ
ルブ１４を、それまでの閉成状態から開成状態に
作動させ、これにより熱媒体を熱媒体送給管５か
らベーパライザＶへ供与できるよう構成されてい
る。 In other words, the pressure sensing element 15 issues a signal when the liquid pressure in the liquid fuel supply pipe 1 becomes lower than a predetermined pressure value, and switches the automatic opening/closing valve 14 from the previous closing position. It is configured such that the heating medium can be supplied from the heating medium feed pipe 5 to the vaporizer V by operating the heating medium from the open state to the open state.
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.
このような気化ガスの供給状態が続くと、燃料
タンクＴの気相部１２は次第に減圧され、当該減
圧に起因して液体燃料２、すなわち液相部１２の
温度は降下していくことになる。 If such a supply state of vaporized gas continues, the pressure in the gas phase portion 12 of the fuel tank T will gradually decrease, and the temperature of the liquid fuel 2, that is, the liquid phase portion 12 will decrease due to the pressure reduction. .
また上記の如く気相部１２の減圧が、気液自動
切換弁１０を切換作動するに至れば、気化ガス送
給管１１は閉成されると共に液体燃料送給管１が
開成されて、同送給管１とガイド管１３とが連通
状態となり、今度は液体燃料送給路１から液体燃
料２がベーパライザＶへ供給される。 Further, as described above, when the reduced pressure in the gas phase section 12 causes the gas-liquid automatic switching valve 10 to switch, the vaporized gas feed pipe 11 is closed, and the liquid fuel feed pipe 1 is opened. The feed pipe 1 and the guide pipe 13 are brought into communication, and the liquid fuel 2 is now supplied from the liquid fuel feed path 1 to the vaporizer V.
上記の如き気液供給の切換作動と同期して、気
相部１２の降圧による液相部の低圧化を、前記の
圧力検知素子１５が検知し、これにより前記の通
り自動開閉バルブ１４が作動して、熱媒体送給管
５が開成され、熱媒体は、ベーパライザＶ内に流
入し同ベーパライザＶ内に流入されて来た液体燃
料２を加温気化し、この強制気化による燃料ガス
が供給管３を通じて負荷側Ｌに送給される。 In synchronization with the gas-liquid supply switching operation as described above, the pressure sensing element 15 detects a decrease in the pressure in the liquid phase due to the pressure drop in the gas phase 12, and this causes the automatic opening/closing valve 14 to operate as described above. Then, the heat medium supply pipe 5 is opened, the heat medium flows into the vaporizer V, heats and vaporizes the liquid fuel 2 that has flowed into the vaporizer V, and fuel gas is supplied by this forced vaporization. It is fed to the load side L through the pipe 3.
この考案では上記実施例のように、熱媒体とし
て常温水の、例えば井戸水等を使用できるのであ
るが、これは、前記の通り液体燃料２が燃料タン
クＴの気相部１２における減圧により低温化する
ため、15℃程度の低温である常温水を用いても、
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からである。 In this invention, as in the above embodiment, room temperature water, such as well water, can be used as the heat medium, but this is because the liquid fuel 2 is lowered in temperature by the pressure reduction in the gas phase part 12 of the fuel tank T, as described above. Therefore, even if you use room temperature water, which is as low as 15℃,
This is because the temperature difference between the liquid fuel 2 and the heat medium increases, and as a result, the temperature gradient causes rapid heat exchange through heat conduction, and the liquid fuel 2 can be sufficiently vaporized even if it is not a high-temperature heat medium. be.
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
れると共に、圧力検知素子１５により自動開閉バ
ルブ１４が作動して熱媒体送給管５を閉成し、熱
媒体のベーパライザＶへの送給は停止される。 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, the automatic gas-liquid switching valve 10 is switched, and the automatic opening/closing valve 14 is operated by the pressure sensing element 15 to close the heat medium feed pipe 5 and feed the heat medium to the vaporizer V. will be stopped.
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に連結すると共に、
前記液体燃料送給路１に設けた圧力検知素子の圧
力検知信号により、熱媒体送給管５に介設した自
動開閉バルブ１４を開閉自在としたものであるか
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ると、自動開
閉バルブ１４の自動開成によつて熱媒体がベーパ
ライザＶに適時供給されるとともに、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. In between, a gas-liquid automatic switching valve 10 is provided which switches from a vaporized gas flow state to a liquid fuel flow state due to a drop in gas pressure in the gas phase section 12, and the switching outlet side of the switching valve 10 is connected to the load side L. Connected to a vaporizer V equipped with a heat medium feed path 5 to which a heat medium is supplied,
Since the automatic opening/closing valve 14 provided in the heat medium feed pipe 5 can be opened and closed by the pressure detection signal from the pressure detection element provided in the liquid fuel feed path 1, the vaporizer V does not need to be preheated. When fuel gas is to be used on the load side L, the demand can be met by effectively utilizing the naturally vaporized gas, and the naturally vaporized gas becomes diluted and the liquid fuel 2 is supplied to the vaporizer V. When the automatic opening/closing valve 14 is automatically opened, the heat medium is supplied to the vaporizer V in a timely manner, and the gas phase section 12 is automatically opened.
Since the temperature of the liquid fuel 2 is lowered by using the pressure drop of As a result, the consumption of commercial energy and the amount of heat medium used can be significantly reduced, making it possible to lower the running costs of this type of equipment and providing 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、５……熱媒体送給管、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、１４……自動開閉バル
ブ、１５……圧力検知素子、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, 5 ... Heat medium feed pipe, 10 ... Gas-liquid automatic switching valve, 11 ... Vaporized gas feed pipe, 12 ... Gas phase section, 13 ... Guide pipe, 14 ... Automatic opening/closing valve , 15...pressure sensing element, 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と共に、前記
液体燃料送給路に設けた圧力検知素子の圧力検
知信号により、熱媒体送給管に介設した自動開
閉バルブを開成自在としてなる燃料ガス供給装
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. The automatic opening/closing valve interposed in the heating medium feeding pipe can be opened by a pressure detection signal from a pressure sensing element provided in the liquid fuel feeding path. A fuel gas supply device. (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 |
|---|---|---|---|
| JP8324083U JPS59191042U (en) | 1983-06-01 | 1983-06-01 | Fuel gas supply device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8324083U JPS59191042U (en) | 1983-06-01 | 1983-06-01 | Fuel gas supply device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59191042U JPS59191042U (en) | 1984-12-18 |
| JPS6238116Y2 true JPS6238116Y2 (en) | 1987-09-29 |
Family
ID=30213199
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8324083U Granted JPS59191042U (en) | 1983-06-01 | 1983-06-01 | Fuel gas supply device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59191042U (en) |
-
1983
- 1983-06-01 JP JP8324083U patent/JPS59191042U/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59191042U (en) | 1984-12-18 |
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