JPS6240599B2 - - Google Patents
Info
- Publication number
- JPS6240599B2 JPS6240599B2 JP22849183A JP22849183A JPS6240599B2 JP S6240599 B2 JPS6240599 B2 JP S6240599B2 JP 22849183 A JP22849183 A JP 22849183A JP 22849183 A JP22849183 A JP 22849183A JP S6240599 B2 JPS6240599 B2 JP S6240599B2
- Authority
- JP
- Japan
- Prior art keywords
- pipe
- lpg
- accumulator
- body pipe
- vaporizer
- 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
- 239000003915 liquefied petroleum gas Substances 0.000 description 43
- 239000006200 vaporizer Substances 0.000 description 18
- 238000010438 heat treatment Methods 0.000 description 14
- 239000007789 gas Substances 0.000 description 13
- 239000007788 liquid Substances 0.000 description 9
- 230000008016 vaporization Effects 0.000 description 8
- 238000009834 vaporization Methods 0.000 description 7
- 238000009835 boiling Methods 0.000 description 4
- 230000000630 rising effect Effects 0.000 description 3
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C7/00—Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
- F17C7/02—Discharging liquefied gases
- F17C7/04—Discharging liquefied gases with change of state, e.g. vaporisation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2201/00—Vessel construction, in particular geometry, arrangement or size
- F17C2201/01—Shape
- F17C2201/0104—Shape cylindrical
- F17C2201/0109—Shape cylindrical with exteriorly curved end-piece
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2201/00—Vessel construction, in particular geometry, arrangement or size
- F17C2201/01—Shape
- F17C2201/0104—Shape cylindrical
- F17C2201/0119—Shape cylindrical with flat end-piece
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/0323—Valves
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2221/00—Handled fluid, in particular type of fluid
- F17C2221/03—Mixtures
- F17C2221/032—Hydrocarbons
- F17C2221/035—Propane butane, e.g. LPG, GPL
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
- F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
- F17C2223/0146—Two-phase
- F17C2223/0153—Liquefied gas, e.g. LPG, GPL
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
- F17C2223/04—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by other properties of handled fluid before transfer
- F17C2223/042—Localisation of the removal point
- F17C2223/046—Localisation of the removal point in the liquid
- F17C2223/047—Localisation of the removal point in the liquid with a dip tube
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/04—Methods for emptying or filling
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は液化石油ガス(以下LPGという。)の
気化装置に関する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a vaporizer for liquefied petroleum gas (hereinafter referred to as LPG).
(従来の技術)
従来、LPGの気化装置としては一般に第3図に
概略縦断面図として示したような気化装置A′が
知られている。即ち、この気化装置A′は内部に
LPGの熱交換用フイン2を多段に充填した胴パイ
プ1の下部にLPG容器3に連通する導入管4を、
その先端部の立上り管4′を胴パイプ1内に底部
から挿通して設け、又、胴パイプ1の上部に減圧
弁5を介装した導出管6を連通し、胴パイプ1の
外周をヒーター7及び温度制御スイツチ8を組み
込んだ加熱媒体9(例えば鋳物)で環設し、更に
ドレーン排出弁11を介装したドレーン管10を
導入管4の立上り管4′の下端部に連設した構造
となつている。なお、12はLPG容器3の開閉バ
ルブである。(Prior Art) Conventionally, as an LPG vaporizer, a vaporizer A' as shown in a schematic vertical cross-sectional view in FIG. 3 is generally known. That is, this vaporizer A′ has
An introduction pipe 4 communicating with an LPG container 3 is installed at the bottom of a body pipe 1 filled with LPG heat exchange fins 2 in multiple stages.
A riser pipe 4' at the tip thereof is inserted into the body pipe 1 from the bottom, and an outlet pipe 6 in which a pressure reducing valve 5 is interposed is connected to the upper part of the body pipe 1, and the outer periphery of the body pipe 1 is heated. A structure in which a heating medium 9 (for example, cast metal) incorporating a temperature control switch 8 and a drain pipe 10 is connected to the lower end of the riser pipe 4' of the introduction pipe 4. It is becoming. Note that 12 is an on-off valve for the LPG container 3.
(発明が解決しようとする問題点)
しかし、かかる従来のLPG気化装置A′にあつ
ては、LPGは導入管4を経て胴パイプ1の下部か
ら胴パイプ1内に入り、胴パイプ1内に一旦貯留
された後、胴パイプ1内を上昇する間に所定の温
度に加熱制御された胴パイプ1の内壁面と加熱用
フイン2の表面に接触させて気化させる構造であ
るため、その接触加熱が不均一となり完全な過熱
ガスにまで気化されることなく一部気化しないミ
スト状のLPGを含んだ状態で消費側に供給され、
これが消費側の外気温度が低下した場合には再液
化を生ずる場合がある。そこで、従来の装置では
かかる現象を避けるため、熱交換面積を過大に設
定する必要があり、熱交換用フイン2の充填量が
増大する。又、底部にLPGの貯留容積を必要とす
ることもあつて従来の気化装置の容積はかなり大
型化するという問題点があつた。更に、高、中沸
点成分のLPGドレーンは気化装置下部のLPG導入
管の立上り管4′により分離する構造となつてい
るため、ドレーンの分離効率が悪く、大部分のド
レーンは胴パイプ1の内壁に固着したり、消費側
の気化ガスに混入されたまま放出されてしまうと
いう問題点があつた。(Problems to be Solved by the Invention) However, in the conventional LPG vaporizer A', LPG enters the body pipe 1 from the lower part of the body pipe 1 through the introduction pipe 4, and enters the body pipe 1 through the introduction pipe 4. Once stored, the inner wall surface of the body pipe 1, which is heated to a predetermined temperature and the surface of the heating fin 2, is brought into contact with the surface of the heating fin 2 while rising inside the body pipe 1 to vaporize, so the contact heating is supplied to the consumer side in a state containing mist-like LPG that is not completely vaporized into superheated gas and partially vaporized.
This may result in reliquefaction if the outside air temperature on the consumer side drops. Therefore, in order to avoid such a phenomenon in the conventional apparatus, it is necessary to set the heat exchange area to be excessively large, and the filling amount of the heat exchange fins 2 increases. Furthermore, since a storage volume for LPG is required at the bottom, there is a problem in that the volume of the conventional vaporizer is considerably large. Furthermore, since the LPG drain containing high and medium boiling point components is separated by the riser pipe 4' of the LPG introduction pipe at the bottom of the vaporizer, the separation efficiency of the drain is poor, and most of the drain is separated from the inner wall of the body pipe 1. There were problems in that the gas would stick to the gas or be released while being mixed with the vaporized gas on the consumption side.
本発明はかかる従来の気化装置の問題点に鑑が
み、伝熱効率の向上によつて装置容量の小型化を
はかるとともに、高、中沸点成分からなるドレー
ンの分離効率の良いLPGの気化装置を提供するこ
とを目的としてなされたものである。 In view of the problems of such conventional vaporizers, the present invention aims to reduce the device capacity by improving heat transfer efficiency, and provides an LPG vaporizer with high efficiency in separating drains consisting of high and medium boiling point components. It was made for the purpose of providing.
(問題点を解決するための手段)
以下に本発明を実施例を示す添付の図面に基づ
いて説明する。(Means for Solving the Problems) The present invention will be explained below based on the attached drawings showing embodiments.
第1図に本発明のLPG気化装置Aの概略断面図
を示す。なお、以下の説明において第3図に示す
従来のLPG気化装置A′と同一部分については同
一符号を用いた。 FIG. 1 shows a schematic cross-sectional view of an LPG vaporizer A of the present invention. In the following description, the same reference numerals are used for the same parts as in the conventional LPG vaporizer A' shown in FIG. 3.
第1図において本発明のLPG気化装置Aは、外
周に加熱媒体9を環設し、内部に熱交換用フイン
2を多段に充填した胴パイプ1に、胴パイプ1内
下部即ち、胴パイプ1の底壁に近い位置に連通口
13を有する中空管状のアキユムレータ14を垂
直方向に貫設し、液量調節弁15を介装した導入
管4を胴パイプ1内上部に連設すると共に、減圧
弁5を介装し、液量調節弁15に管16を介して
連通する導出管6をアキユムレータ14内の上部
に連設し、更に、ドレーン排出弁11を介装した
ドレーン管10をアキユムレータ14の底部に具
備させて構成される。なお、図中3はLPG容器、
7は加熱媒体9の加熱用ヒーター、8は加熱媒体
9の温度制御スイツチ、12はLPG容器3の開閉
バルブである。 In FIG. 1, the LPG vaporizer A of the present invention has a body pipe 1 in which a heating medium 9 is arranged around the outer periphery and heat exchange fins 2 are filled in multiple stages inside the body pipe 1. A hollow tubular accumulator 14 having a communication port 13 is installed vertically close to the bottom wall of the body pipe 1, and an inlet pipe 4 with a liquid volume control valve 15 is connected to the upper part of the body pipe 1. A drain pipe 6 with a valve 5 interposed therein and communicating with the liquid volume control valve 15 via a pipe 16 is connected to the upper part of the accumulator 14 , and a drain pipe 10 with a drain discharge valve 11 interposed therein is connected to the accumulator 14 . It is equipped on the bottom of the In addition, 3 in the figure is an LPG container,
7 is a heater for heating the heating medium 9; 8 is a temperature control switch for the heating medium 9; and 12 is an opening/closing valve for the LPG container 3.
(作 用)
以下に、本発明のLPG気化装置Aの作用につい
て説明する。(Function) The function of the LPG vaporizer A of the present invention will be explained below.
先ず、気化装置Aの胴パイプ1、熱交換用フイ
ン2及びアキユムレータ14をヒーター7及び温
度制御スイツチ8により加熱媒体9を一定温度に
加熱してLPGの気化に必要な所定の温度に予め昇
温させる。 First, the body pipe 1, heat exchange fins 2, and accumulator 14 of the vaporizer A are heated to a predetermined temperature necessary for vaporizing LPG by heating the heating medium 9 to a constant temperature using the heater 7 and the temperature control switch 8. let
次に、LPG容器3の開閉バルブ12を開き、液
量調節弁15を通過させて消費側の消費に見合う
所定量のLPGを胴パイプ1の上部から熱交換用フ
イン2の上面に供給させる。供給されたLPGは胴
パイプ1の内壁面と多段に充填された熱交換用フ
イン2の表面を交互に矢印方向に流下する間に気
化され、胴パイプ1の下部に設けられたアキユム
レータ14の連通口13からアキユムレータ14
の下部に流入し、低流速で更にアキユムレータ1
4の中空管内を上昇する間に過熱される。 Next, the on-off valve 12 of the LPG container 3 is opened, and a predetermined amount of LPG corresponding to consumption on the consumer side is supplied from the upper part of the body pipe 1 to the upper surface of the heat exchange fin 2 by passing through the liquid amount control valve 15. The supplied LPG is vaporized while flowing down alternately in the direction of the arrow on the inner wall surface of the body pipe 1 and the surface of the heat exchange fins 2 packed in multiple stages. Accumulator 14 from mouth 13
It flows into the lower part of the accumulator 1 at a low flow rate.
It is heated up while rising in the hollow tube of 4.
アキユムレータ14は気化されたLPGガスの過
熱化に必要とする十分な加熱通路を提供する作用
がある。 The accumulator 14 functions to provide a sufficient heating path necessary for superheating the vaporized LPG gas.
又、LPGの高、中沸点成分からなるドレーンは
アキユムレータ14の底部に設けられたドレーン
管10より外部に分離除去される。この場合、ア
キユムレータ14は、ドレーンのLPGガスからの
分離を効果的に行なわせる作用をも有する。 Further, drain consisting of high and medium boiling point components of LPG is separated and removed to the outside through a drain pipe 10 provided at the bottom of the accumulator 14. In this case, the accumulator 14 also has the function of effectively separating the drain from the LPG gas.
一方、ドレーンが分離除去されたLPGガスはア
キユムレータ14の上部から減圧弁5を経て導出
管6より消費側へ送られる。ここで、消費側にお
いてガスが使用されていない場合には、管16に
流れて液量調節弁15が閉じ、又、消費側におい
てガスが使用されると液量調節弁15が開き、消
費量に見合つたLPGが気化装置Aに供給されるよ
うに図示しない公知の制御手段より自動的に調節
される。 On the other hand, the LPG gas from which the drain has been separated is sent from the upper part of the accumulator 14 through the pressure reducing valve 5 to the outlet pipe 6 to the consumption side. Here, when gas is not used on the consumption side, it flows into the pipe 16 and the liquid volume control valve 15 is closed, and when gas is used on the consumption side, the liquid volume control valve 15 opens and the consumption amount It is automatically adjusted by a known control means (not shown) so that LPG corresponding to the amount is supplied to the vaporizer A.
(他の実施例)
第2図に本発明のLPG気化装置の他の実施例B
の概略断面図を示す。(Other Embodiments) FIG. 2 shows another embodiment B of the LPG vaporization apparatus of the present invention.
A schematic cross-sectional view is shown.
第2図に示されるLPG気化装置Bは、その主要
部において第1図の気化装置Aと全く同一である
が、導入管4の胴パイプ1上部に連設する部分に
改良が施こされている。 The LPG vaporizer B shown in FIG. 2 is completely the same as the vaporizer A shown in FIG. There is.
即ち、導入管4の液量調節弁15と胴パイプ1
内上部の開口部17との間の管路をアキユムレー
タ14の内部に設けることにより、該管路を補助
熱交換器18に形成したものである。なお、19
は該管路の外周に熱交換面積増加のために付設さ
れたフインである。この実施例の気化装置Bによ
るときは、液量調節弁15を経て胴パイプ1内に
供給されるLPGは補助熱交換器18を通過する際
にアキユムレータ14内を上昇する過熱ガスによ
り予熱され、以後のLPGの気化を促進させる。
又、補助熱交換器18と接触したアキユムレータ
14内の過熱ガスは幾分温度降下して過熱ガス中
の高、中沸点成分は補助熱交換器18の表面でそ
の凝縮が促進され、ドレーン除去が更に有効に達
成される。 That is, the liquid volume control valve 15 of the introduction pipe 4 and the body pipe 1
By providing a conduit between the opening 17 at the inner upper part inside the accumulator 14, the conduit is formed in the auxiliary heat exchanger 18. In addition, 19
are fins attached to the outer periphery of the pipe to increase the heat exchange area. When using the vaporizer B of this embodiment, the LPG supplied into the body pipe 1 via the liquid volume control valve 15 is preheated by the superheated gas rising inside the accumulator 14 when passing through the auxiliary heat exchanger 18. Promotes subsequent vaporization of LPG.
Further, the temperature of the superheated gas in the accumulator 14 that has come into contact with the auxiliary heat exchanger 18 drops to some extent, and the condensation of high and medium boiling point components in the superheated gas is promoted on the surface of the auxiliary heat exchanger 18, and drain removal is facilitated. This can be achieved more effectively.
(発明の効果)
以上詳細に説明したように、本発明のLPG気化
装置においては、外周に加熱媒体を環設し、内部
に熱交換用フインを充填した胴パイプ内に、上部
よりLPGを流下させて気化させ、胴パイプ内に貫
設させた中空管状のアキユムレータの下部から低
流速で上昇させる間に過熱させるように構成した
から、LPGの加熱通路が長大化して伝熱効率が大
幅に向上する。(Effects of the Invention) As explained in detail above, in the LPG vaporizer of the present invention, LPG is flowed from the upper part into the body pipe which has a heating medium ringed around the outer periphery and which is filled with heat exchange fins. The LPG is vaporized and heated while being raised at a low flow rate from the bottom of a hollow tubular accumulator inserted through the body pipe, making the LPG heating path longer and greatly improving heat transfer efficiency. .
又、必要な流量は液量調節弁で制御するように
したから、胴パイプの底部にLPGの貯留容積を設
ける必要もなくなり、上記の伝熱効率の向上と相
俟つて装置を小型化することができる。又、ドレ
ーンもアキユムレータ内で効果的に分離され、ア
キユムレータ底部に設けられたドレーン管から円
滑に除去される効果がある。更に、LPG導入管の
胴パイプ内に通ずる管路の一部をアキユムレータ
内に配設し、補助熱交換器として機能させること
により、LPGの気化とドレーンの除去とを同時に
促進させることができる利点を有する。 In addition, since the required flow rate is controlled by a liquid volume control valve, there is no need to provide an LPG storage volume at the bottom of the body pipe, which, together with the above-mentioned improvement in heat transfer efficiency, makes it possible to downsize the device. can. Furthermore, the drain is effectively separated within the accumulator and smoothly removed from the drain pipe provided at the bottom of the accumulator. Furthermore, by arranging a part of the pipe line leading into the body pipe of the LPG introduction pipe in the accumulator and functioning as an auxiliary heat exchanger, it is possible to simultaneously promote LPG vaporization and drain removal. has.
第1図は本発明の液化石油ガス気化装置の概略
縦断面図、第2図は本発明の他の実施例を示す液
化石油ガス気化装置の概略縦断面図、第3図は従
来の液化石油ガス気化装置の概略縦断面図を示
す。
1…胴パイプ、2…熱交換用フイン、3…LPG
容器、4…導入管、6…導出管、8…温度制御ス
イツチ、9…加熱媒体、10…ドレーン管、13
…連通口、14…アキユムレータ、15…液量調
節弁、18…補助熱交換器。
FIG. 1 is a schematic vertical cross-sectional view of a liquefied petroleum gas vaporization device of the present invention, FIG. 2 is a schematic vertical cross-sectional view of a liquefied petroleum gas vaporization device showing another embodiment of the present invention, and FIG. 3 is a schematic longitudinal sectional view of a liquefied petroleum gas vaporization device of the present invention. A schematic vertical cross-sectional view of a gas vaporization device is shown. 1... body pipe, 2... heat exchange fin, 3... LPG
Container, 4... Inlet pipe, 6... Outlet pipe, 8... Temperature control switch, 9... Heating medium, 10... Drain pipe, 13
...Communication port, 14...Accumulator, 15...Liquid amount control valve, 18...Auxiliary heat exchanger.
Claims (1)
インを充填した胴パイプに、該胴パイプ内下部に
連通口を有する中空管状のアキユムレータを貫設
し、液量調節弁を介装した導入管を該胴パイプ内
上部に連設すると共に、減圧弁を介装し該液量調
節弁に連通する導出管を該アキユムレータ内上部
に連設し、ドレーン管を該アキユムレータ底部に
具備させたことを特徴とする液化石油ガス気化装
置。1 A hollow tubular accumulator having a communication port in the lower part of the body pipe is inserted through a body pipe with a heating medium arranged around the outer periphery and heat exchange fins filled inside, and a liquid volume control valve is interposed therein. An inlet pipe is connected to the upper part of the inside of the body pipe, an outlet pipe is connected to the upper part of the accumulator through which a pressure reducing valve is interposed and communicates with the liquid volume control valve, and a drain pipe is provided to the bottom of the accumulator. A liquefied petroleum gas vaporization device characterized by:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58228491A JPS60121397A (en) | 1983-12-05 | 1983-12-05 | Liquefied petroleum gas vaporization equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58228491A JPS60121397A (en) | 1983-12-05 | 1983-12-05 | Liquefied petroleum gas vaporization equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60121397A JPS60121397A (en) | 1985-06-28 |
| JPS6240599B2 true JPS6240599B2 (en) | 1987-08-28 |
Family
ID=16877289
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58228491A Granted JPS60121397A (en) | 1983-12-05 | 1983-12-05 | Liquefied petroleum gas vaporization equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60121397A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105257979A (en) * | 2015-07-02 | 2016-01-20 | 浙江海洋学院 | Liquefied natural gas gasifier fixedly connected with inner heat exchange fins and retractable outer heat exchange fins |
-
1983
- 1983-12-05 JP JP58228491A patent/JPS60121397A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60121397A (en) | 1985-06-28 |
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