JP4754727B2 - Liquefied gas vaporizer - Google Patents

Liquefied gas vaporizer Download PDF

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Publication number
JP4754727B2
JP4754727B2 JP2001220866A JP2001220866A JP4754727B2 JP 4754727 B2 JP4754727 B2 JP 4754727B2 JP 2001220866 A JP2001220866 A JP 2001220866A JP 2001220866 A JP2001220866 A JP 2001220866A JP 4754727 B2 JP4754727 B2 JP 4754727B2
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Japan
Prior art keywords
valve
liquefied gas
gas
vaporized
pressure regulating
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 - Fee Related
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JP2001220866A
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Japanese (ja)
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JP2003028396A (en
Inventor
弘 岩木
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ITO KOKI CO., LTD.
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ITO KOKI CO., LTD.
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Priority to JP2001220866A priority Critical patent/JP4754727B2/en
Publication of JP2003028396A publication Critical patent/JP2003028396A/en
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Description

【0001】
【発明の属する技術分野】
この発明は気化圧力調整弁周辺の結露・凍結を防止し円滑な作動を保証した液化ガスの気化装置に関する。
【0002】
【従来の技術】
液化ガスの気化装置としてこれまで採用されてきたものは図3に示すように液化ガス供給源から延びる配管31が気化ガス圧力調整弁32に接続され、この気化ガス圧力調整弁32を通過した液化ガスは熱交換器33に導かれて気化し、ガス溜め34に蓄溜される。
【0003】
上記気化ガス圧力調整弁32は、保安弁32a と切替え弁32b とダイヤフラム室32c と切替えレバー32d とからなっており、ダイフラム室32c には上記ガス溜め34から延びる連通管35が接続されてガス溜め34の内圧に対応して気化ガス圧力調整弁32が作動するようになっている。
【0004】
上記ガス溜め34には、安全弁34a と圧力計34b と温度センサー34d とが付設され、温度センサー34d の出力によって作動する液流出防止弁34c がガス溜め34の出口に取り付けられて気化してないガスの流出を防止するようになっている。
【0005】
【発明が解決しようとする課題】
上記のように構成するこれまでの液化ガス気化装置では、気化圧力を0.1MPaとすると液化ガスの温度は−25℃になり、気化ガス圧力調整弁も−25℃となってダイヤフラムが極低温に晒されることとなり、ダイヤフラムは、この極低温でも正常に作用する特性が要求される。
【0006】
一方、気化圧力調整弁がこのように極低温になることにより周辺の大気中の水分が結露し凍結に至ることがあり、これによりダイヤフラムを押さえているバネ室の通気孔を塞ぐこととなって調圧機能が不安定になる問題を抱えている。
【0007】
この問題を回避するために熱伝導面積を小さくしたり、作動部までの距離を長くしたものがあるが、それによって装置が大型化する。また、作動部分に温水を循環させるものがあるが、それによって構造が複雑になり、ガスの消費がないときは温度のバランスが崩れて高温となってダイヤフラムをはじめゴム・プラスチックを材料とする部品の劣化を促進する問題がある。
【0008】
以上の問題に鑑みこの発明は、気化ガス圧力調整弁を大型化・構造の複雑化をせず、強制加熱によるダイヤフラムなどの部品の劣化を促進するような問題のない液化ガス気化装置を提供しようとするものである。
【0009】
【課題を解決するための手段】
上記課題を解決するためにこの発明は、液化ガス供給源から延びる配管を気化ガス圧力調整弁に接続し、気化ガス圧力調整弁を経た液化ガスを熱交換器に導いて液化ガスを気化する装置において、上記気化ガスの流路にオリフィスを設け、該オリフィスの上流側と下流側から連通管を延設して上記気化ガス圧力調整弁のダイヤフラム室に接続し、上記熱交換器の後段にガス溜めを形成したものである。
【0010】
上記の如く構成するこの発明によれば、気化ガスの流路に設けたオリフィスの上流側と下流側では微小圧力差が発生する。従って、熱交換器で加温されて気化したガスがオリフィスの上流側から延びた連通管を経てダイヤフラム室に向けて流れ、下流側から延びた連通管を経てガス溜めに向けて流れて循環することとなり結露・凍結が防止される。しかも、運転時(ガス消費時)だけの加温となるのでダイヤフラムなどの劣化を招くこともない。
【0011】
【発明の実施の形態】
次に第一実施形態を図1を参照しながら説明する。図示しない二基の液化ガス供給源から延びる配管11は、保安弁12aと切替えレバー12dによって作動する切替え弁12bとを備えた気化ガス圧力調整弁12に繋がれ、気化ガス圧力調整弁12を通過した液化ガスは、熱交換器13に導かれ、ここで温水により加温されて気化しガス溜め14に蓄溜される。
【0012】
ガス溜め14の出口にはオリフィス16が設けられ、その上流側と下流側から連通管15a ,15b が延び気化ガス圧力調整弁12のダイヤフラム室12c に接続されている。
【0013】
ガス溜め14には安全弁14a と圧力計14b と温度センサー14d が付設され、ガス溜め14の出口には上記温度センサー14d の出力によって作動する液流出防止弁14c (サーモバルブ)が取付けられている。
【0014】
上記のように構成するこの実施形態では、ガス溜め14の出口に設けたオリフィス16の前後で圧力差が生じ、熱交換器13で加温されて気化したガスが、連通管15a 、ダイヤフラム室12c 、連通管15b 、ガス溜め14の順に循環するようになり、気化ガス圧力調整弁12に結露・凍結が発生せず、異常加温もされないのでダイヤフラムなどのゴム・プラスチック製部品を劣化される恐れもなくなる。
【0015】
次に第二実施形態を図2を参照しながら説明する。図示しない二基の液化ガス供給源から延びる配管21は、切替え弁27を経て液化ガス供給路28に接続され、熱交換器23の温水流路に付設された温度センサー28c の出力により作動する過剰供給制御弁28a (サーモバルブ)と異常圧力制御弁28b とを経て気化ガス圧力調整弁22で気化圧力に調整されて熱交換器23に導かれ温水で加温されて気化しガス溜め24に蓄溜される。なお、28d は温度センサーのリードパイプ、24b はドレン抜きプラグである。
【0016】
ガス溜め24に深く差し込まれたガス消費管路29にはオリフィス26が設けられ、その上流側と下流側から連通管25a ,25b が延び気化ガス圧力調整弁22のダイヤフラム室22c に接続されている。
【0017】
上記のように構成するこの実施形態では、ガス消費管路29に設けたオリフィス26の前後で圧力差が生じ、熱交換器23で加温されて気化したガスが、連通管25a 、ダイヤフラム室22c 、連通管25b 、ガス消費管路29の順に循環するようになり、気化ガス圧力調整弁22に結露・凍結が発生せず、異常加温もされないのでダイヤフラムなどのゴム・プラスチック製部品を劣化される恐れもなくなる。
【0018】
【発明の効果】
以上説明した通りこの発明は、気化ガスの流路に設けたオリフィスの上流側と下流側で発生する微小圧力差を利用して、熱交換器で加温・気化したガスが、オリフィスの上流側から延ばした連通管、ダイヤフラム室、下流側から延ばした連通管の順に循環することとなり結露・凍結が防止される。しかも、運転時(ガス消費時)だけの加温となるので異常加温もなくダイヤフラムなどゴム・プラスチック製部品の劣化を招くこともない。
【図面の簡単な説明】
【図1】第一実施形態の構成図
【図2】第二実施形態の構成図
【図3】従来の液化ガス気化装置の構成図
【符号の説明】
10,20,30 液化ガス気化装置
11,21,31 配管
12,22,32 気化ガス圧力調整弁
12a ,32a 保安弁
12b ,32b 切替え弁
12c ,32c ダイヤフラム室
12d ,32d 切替えレバー
13,23,33 熱交換器
14,24,34 ガス溜め
15a ,25a 連通管(上流側)
15b ,25b 連通管(下流側)
16,26 オリフィス
27 切替え弁
28 液化ガス供給路
28a 過剰供給制御弁
28b 異常圧力制御弁
28c 温度センサー
28d リードパイプ
29 ガス消費管路
35 連通管
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a liquefied gas vaporizer that prevents condensation and freezing around a vaporization pressure regulating valve and ensures smooth operation.
[0002]
[Prior art]
As a liquefied gas vaporizer, a pipe 31 extending from a liquefied gas supply source is connected to a vaporized gas pressure regulating valve 32 as shown in FIG. The gas is guided to the heat exchanger 33 and vaporized, and stored in the gas reservoir 34.
[0003]
The vaporized gas pressure regulating valve 32 comprises a safety valve 32a, a switching valve 32b, a diaphragm chamber 32c, and a switching lever 32d. A communication pipe 35 extending from the gas reservoir 34 is connected to the diaphragm chamber 32c to store the gas. Corresponding to the internal pressure 34, the vaporized gas pressure regulating valve 32 operates.
[0004]
The gas reservoir 34 is provided with a safety valve 34a, a pressure gauge 34b, and a temperature sensor 34d, and a liquid outflow prevention valve 34c that is actuated by the output of the temperature sensor 34d is attached to the outlet of the gas reservoir 34 and is not vaporized. Is designed to prevent spills.
[0005]
[Problems to be solved by the invention]
In the conventional liquefied gas vaporizer configured as described above, when the vaporization pressure is 0.1 MPa, the temperature of the liquefied gas becomes -25 ° C, the vaporized gas pressure adjustment valve also becomes -25 ° C, and the diaphragm is at a very low temperature. Therefore, the diaphragm is required to have a property of functioning normally even at this extremely low temperature.
[0006]
On the other hand, when the vaporizing pressure regulating valve becomes extremely low in this way, moisture in the surrounding atmosphere may condense and freeze, thereby blocking the vent hole of the spring chamber holding the diaphragm. The pressure regulation function is unstable.
[0007]
In order to avoid this problem, there are some in which the heat conduction area is reduced or the distance to the working part is increased, but this increases the size of the apparatus. In addition, there is something that circulates hot water in the operating part, but this makes the structure complicated, and when there is no gas consumption, the temperature balance is broken and the temperature becomes high, and parts made of rubber and plastic including diaphragms There is a problem of promoting the deterioration of
[0008]
In view of the above problems, the present invention aims to provide a liquefied gas vaporizer that does not increase the size of the vaporized gas pressure regulating valve and does not complicate the structure, and promotes the deterioration of parts such as a diaphragm due to forced heating. It is what.
[0009]
[Means for Solving the Problems]
The invention to solve the above problems, a pipe extending from a liquefied gas supply source connected to the vaporized gas pressure regulator valve, to vaporize the liquefied gas liquefied gas passing through the vaporized gas pressure regulating valve leading to the heat exchanger device The vaporized gas flow path is provided with an orifice, a communication pipe is extended from the upstream side and the downstream side of the orifice, connected to the diaphragm chamber of the vaporized gas pressure regulating valve, and a gas is provided downstream of the heat exchanger. A reservoir is formed.
[0010]
According to the present invention configured as described above, a minute pressure difference is generated between the upstream side and the downstream side of the orifice provided in the vaporized gas flow path. Therefore, the gas heated and vaporized by the heat exchanger flows toward the diaphragm chamber through the communication pipe extending from the upstream side of the orifice, and flows and circulates toward the gas reservoir through the communication pipe extended from the downstream side. As a result, condensation and freezing are prevented. Moreover, since the heating is performed only during operation (gas consumption), the diaphragm and the like are not deteriorated.
[0011]
DETAILED DESCRIPTION OF THE INVENTION
Next, a first embodiment will be described with reference to FIG. A pipe 11 extending from two liquefied gas supply sources (not shown) is connected to a vaporized gas pressure regulating valve 12 having a safety valve 12a and a switching valve 12b operated by a switching lever 12d, and passes through the vaporized gas pressure regulating valve 12. The liquefied gas is led to the heat exchanger 13 where it is heated by hot water and vaporized and stored in the gas reservoir 14.
[0012]
An orifice 16 is provided at the outlet of the gas reservoir 14, and communication pipes 15 a, 15 b extend from the upstream side and the downstream side thereof and are connected to the diaphragm chamber 12 c of the vaporized gas pressure regulating valve 12.
[0013]
The gas reservoir 14 is provided with a safety valve 14a, a pressure gauge 14b, and a temperature sensor 14d, and a liquid outflow prevention valve 14c (thermo valve) that is operated by the output of the temperature sensor 14d is attached to the outlet of the gas reservoir 14.
[0014]
In this embodiment configured as described above, a pressure difference is generated before and after the orifice 16 provided at the outlet of the gas reservoir 14, and the gas heated and vaporized by the heat exchanger 13 is connected to the communication pipe 15a and the diaphragm chamber 12c. Then, the communication pipe 15b and the gas reservoir 14 are circulated in this order, and the vaporized gas pressure regulating valve 12 does not cause condensation or freezing, and is not heated abnormally, so that rubber or plastic parts such as a diaphragm may be deteriorated. Also disappear.
[0015]
Next, a second embodiment will be described with reference to FIG. A pipe 21 extending from two liquefied gas supply sources (not shown) is connected to a liquefied gas supply path 28 via a switching valve 27 and is operated by an output of a temperature sensor 28c attached to a hot water flow path of the heat exchanger 23. After passing through the supply control valve 28a (thermo valve) and the abnormal pressure control valve 28b, the vaporized gas pressure regulating valve 22 adjusts the vaporized pressure, guides it to the heat exchanger 23, warms it with hot water, vaporizes it, and stores it in the gas reservoir 24. Accumulated. Reference numeral 28d denotes a temperature sensor lead pipe and 24b denotes a drain plug.
[0016]
An orifice 26 is provided in the gas consumption pipe 29 deeply inserted into the gas reservoir 24, and communication pipes 25 a and 25 b extend from the upstream side and the downstream side thereof and are connected to the diaphragm chamber 22 c of the vaporized gas pressure regulating valve 22. .
[0017]
In this embodiment configured as described above, a pressure difference is generated before and after the orifice 26 provided in the gas consumption pipe 29, and the gas heated and vaporized by the heat exchanger 23 is connected to the communication pipe 25a and the diaphragm chamber 22c. The communication pipe 25b and the gas consumption pipe 29 are circulated in this order, and the vaporized gas pressure regulating valve 22 does not cause condensation or freezing, and is not heated abnormally, so that rubber and plastic parts such as a diaphragm are deteriorated. There is no fear of it.
[0018]
【The invention's effect】
As described above, the present invention uses the minute pressure difference generated between the upstream side and the downstream side of the orifice provided in the flow path of the vaporized gas so that the gas heated and vaporized by the heat exchanger is upstream of the orifice. The communication pipe extended from the diaphragm, the diaphragm chamber, and the communication pipe extended from the downstream side are circulated in this order to prevent condensation and freezing. In addition, since heating is performed only during operation (gas consumption), there is no abnormal heating, and deterioration of rubber / plastic parts such as a diaphragm is not caused.
[Brief description of the drawings]
FIG. 1 is a block diagram of a first embodiment. FIG. 2 is a block diagram of a second embodiment. FIG. 3 is a block diagram of a conventional liquefied gas vaporizer.
10, 20, 30 Liquefied gas vaporizer 11, 21, 31 Piping 12, 22, 32 Vaporized gas pressure regulating valve 12a, 32a Safety valve 12b, 32b Switching valve 12c, 32c Diaphragm chamber 12d, 32d Switching levers 13, 23, 33 Heat exchanger 14, 24, 34 Gas reservoir 15a, 25a Communication pipe (upstream side)
15b, 25b communication pipe (downstream)
16, 26 Orifice 27 Switching valve 28 Liquefied gas supply path 28a Excess supply control valve 28b Abnormal pressure control valve 28c Temperature sensor 28d Lead pipe 29 Gas consumption pipe 35 Communication pipe

Claims (6)

液化ガス供給源から延びる配管(11)を気化ガス圧力調整弁(12)に接続し、気化ガス圧力調整弁(12)を経た液化ガスを熱交換器(13)に導いて液化ガスを気化する液化ガスの気化装置において、気化ガスの流路にオリフィス(16)を設け、該オリフィス(16)の上流側と下流側から連通管(15a、15b)を延設して上記気化ガス圧力調整弁(12)のダイヤフラム室(12c)に接続したことを特徴とする液化ガスの気化装置。A pipe (11) extending from a liquefied gas supply source connected to the vaporized gas pressure regulating valve (12), vaporizing liquefied gas vaporized gas pressure regulator valve liquefied gas passing through the (12) leading to the heat exchanger (13) in the vaporizer for liquefied gas, the orifice (16) installed in a flow path of the air gases, communicating conduit from an upstream side and a downstream side of the orifice (16) (15a, 15b) the vaporized gas pressure adjusted by extending the A liquefied gas vaporizer connected to a diaphragm chamber (12c) of a valve (12) . 上記熱交換器(13)の後段にガス溜め(14)を形成したことを特徴とする請求項1に記載の液化ガスの気化装置。The liquefied gas vaporizer according to claim 1, wherein a gas reservoir (14) is formed at a stage subsequent to the heat exchanger (13) . 上記気化ガス圧力調整弁(12)に切替え弁(12b)と保安弁(12a)とを併設したことを特徴とする請求項1または2に記載の液化ガスの気化装置。The liquefied gas vaporizer according to claim 1 or 2, wherein a switching valve (12b) and a safety valve (12a) are provided in addition to the vaporized gas pressure regulating valve (12) . 上記ガス溜め(14)に安全弁(14a)と温度センサー(14d)を付設し、上記温度センサー(14d)の出力により作動する液流出防止弁(14c)を上記ガス溜め(14)の出口に設置したことを特徴とする請求項に記載の液化ガスの気化装置。The gas reservoir (14) to the annexed a safety valve (14a) and a temperature sensor (14d), disposed liquid outflow preventing valve that operates by the output of the temperature sensor (14d) to (14c) to the outlet of the gas reservoir (14) The liquefied gas vaporizer according to claim 2 . 上記液化ガス供給源から延びる配管(21)と気化ガス圧力調整弁(22)との間に切替え弁(27)過剰供給制御弁(28a)および異常圧力制御弁(28b)を配設したことを特徴とする請求項1または2に記載の液化ガスの気化装置。It was provided with switching it valve (27), an excess supply control valve (28a) and abnormal pressure control valve (28b) between the vaporized gas pressure regulating valve (22) pipe (21) extending from the liquefied gas supply source The liquefied gas vaporizer according to claim 1 or 2, 上記過剰供給制御弁(28a)は、温水流路に付設された温度センサー(28c)の出力により作動するようにしたことを特徴とする請求項に記載の液化ガスの気化装置。The liquefied gas vaporizer according to claim 5 , wherein the excess supply control valve (28a) is operated by an output of a temperature sensor (28c) attached to the hot water flow path.
JP2001220866A 2001-07-23 2001-07-23 Liquefied gas vaporizer Expired - Fee Related JP4754727B2 (en)

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