JP2001056097A - Carburetor for liquefied gas fuel - Google Patents
Carburetor for liquefied gas fuelInfo
- Publication number
- JP2001056097A JP2001056097A JP11230256A JP23025699A JP2001056097A JP 2001056097 A JP2001056097 A JP 2001056097A JP 11230256 A JP11230256 A JP 11230256A JP 23025699 A JP23025699 A JP 23025699A JP 2001056097 A JP2001056097 A JP 2001056097A
- Authority
- JP
- Japan
- Prior art keywords
- heat
- vaporization
- cutouts
- finned
- fins
- 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.)
- Pending
Links
Landscapes
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は、大気中の熱エネ
ルギーを効率よく吸収して液化ガス燃料を気化させる装
置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for efficiently absorbing thermal energy in the atmosphere and vaporizing a liquefied gas fuel.
【0002】[0002]
【従来の技術】一般に使用されている燃料ガスは、都市
ガスと液化ガスであり、液化ガスの多くは液化石油ガス
(以下、LPGという)である。2. Description of the Related Art Fuel gas generally used is city gas and liquefied gas, and most of liquefied gas is liquefied petroleum gas (hereinafter referred to as LPG).
【0003】一般家庭で使用されるLPGは、シリンダ
型ボンベに充填されて宅配され、ボンベに充填されたL
PGがなくなると、LPGを充填したボンベと交換する
方式で供給されている。[0003] LPG used in ordinary households is packed in a cylinder-type cylinder and delivered to the home, and the LPG filled in the cylinder is delivered.
When the PG runs out, it is supplied in such a way that it is replaced with a cylinder filled with LPG.
【0004】LPGボンベからのガス供給は、ボンベ表
面から大気中の熱エネルギーを気化熱として吸収してL
PGを気化させてガス消費機器に供給されるが、その
際、プロパンにあっては、1kgを気化させるのに約4
27キロジュール(kJ)の気化熱を必要とし、ボンベ
の表面のみからの気化熱の吸収ではガスの発生量に限界
がある。The gas supply from the LPG cylinder absorbs thermal energy in the atmosphere from the cylinder surface as heat of vaporization, and
PG is vaporized and supplied to a gas consuming device. In this case, in the case of propane, about 4 kg is required to vaporize 1 kg.
It requires 27 kilojoules (kJ) of heat of vaporization, and there is a limit to the amount of gas generated by the absorption of heat of vaporization only from the surface of the cylinder.
【0005】ところで、近年、人件費などの配送コスト
の高騰により、配送経費の低減を目的として、従来大口
の顧客向けに採用されていたバルク容器が中・小口の顧
客にも採用されるようになってきている。[0005] In recent years, bulk containers, which have been conventionally used for large customers, have been adopted by medium and small customers in order to reduce delivery costs due to soaring delivery costs such as labor costs. It has become to.
【0006】上記バルク容器の場合、ガスの消費量に対
する容器の表面積が小さくなるため一般家庭用として使
用されているボンベのように、大気中の熱エネルギーを
気化熱として吸収するだけでは、充分LPGを気化させ
ることができない。In the case of the above-mentioned bulk container, since the surface area of the container with respect to the gas consumption is small, it is not enough to absorb the heat energy in the atmosphere as heat of vaporization as in a cylinder used for general households. Can not be vaporized.
【0007】従って、バルク容器を採用する場合、図5
に示すようにバルク容器1の液相から抽出したLPGを
気化器9に導き、ここで電気あるいは蒸気などにより気
化熱を与えて気化させるか、図6に示すように、バルク
容器1の液相内に熱交換器10を配置して気化熱を与え
て気化させるかのいずれかの方法が採用されてきた。な
お、図5、図6において2はガス充填弁、3はガス取り
出し弁、4は一次調整弁、5は二次調整弁、6はメータ
ー、7は安全弁、8は液面計、11は給湯器、12は外
気センサー、13は圧力センサー、14は温度センサ
ー、15は制御器である。Therefore, when a bulk container is used, FIG.
The LPG extracted from the liquid phase of the bulk container 1 is guided to a vaporizer 9 as shown in FIG. 6, where it is vaporized by applying heat of vaporization by electricity or steam, or as shown in FIG. Either a method of arranging the heat exchanger 10 therein and applying heat of vaporization to vaporize the heat has been adopted. 5 and 6, 2 is a gas filling valve, 3 is a gas takeoff valve, 4 is a primary regulating valve, 5 is a secondary regulating valve, 6 is a meter, 7 is a safety valve, 8 is a liquid level gauge, and 11 is hot water supply. , 12 is an outside air sensor, 13 is a pressure sensor, 14 is a temperature sensor, and 15 is a controller.
【0008】また、上記LPGの気化方法では別途熱エ
ネルギーを必要とし、ランニングコストが嵩むため、鰭
付き管を多数林立させ、この鰭付き管にバルク容器の液
相から抽出したLPGを導き、大気中の熱エネルギーを
気化熱として吸収するものが採用されている。Further, since the above-mentioned LPG vaporization method requires additional heat energy and increases running costs, a large number of finned tubes are established, and LPG extracted from the liquid phase of the bulk container is introduced into the finned tubes, and the air is introduced into the atmosphere. One that absorbs heat energy inside as vaporization heat is employed.
【0009】上記のように大気中の熱エネルギーを気化
熱として吸収するタイプの気化装置の一形態を図4によ
り説明する。An embodiment of a vaporizer of the type that absorbs thermal energy in the atmosphere as heat of vaporization as described above will be described with reference to FIG.
【0010】正常時は、図4(a)のようにバルク容器
の液相から抽出されたLPGは、液用調節弁31でLP
Gの供給が制御され、蒸発器本体(鰭付き管)32が気
化熱を吸収してガス化し、温度感知筒33を経てガス消
費管路(以下、ラインという)34に供給される。温度
感知筒33には温度センサー35が取り付けられてい
る。Under normal conditions, the LPG extracted from the liquid phase of the bulk container as shown in FIG.
The supply of G is controlled, the evaporator body (tube with fins) 32 absorbs heat of vaporization and gasifies, and is supplied to a gas consuming pipe (hereinafter, referred to as a line) 34 via a temperature sensing cylinder 33. A temperature sensor 35 is attached to the temperature sensing cylinder 33.
【0011】鰭付き管32でLPGが順当に気化してい
るときは、ライン34の気化ガスの一部が取り込まれて
遮断弁36を経て上記液用調整弁31のダイヤフラム室
37に入り、LPG側の圧力とバランスして順当にLP
Gが供給される。When the LPG is vaporized properly in the finned tube 32, a part of the vaporized gas in the line 34 is taken in, enters the diaphragm chamber 37 of the liquid regulating valve 31 through the shut-off valve 36, and enters the LPG. LP properly balanced with the side pressure
G is supplied.
【0012】ここで、鰭付き管32での気化熱の吸収が
不十分、即ち、気化が不十分になると図4(b)のよう
に温度感知筒33の温度が低下し、温度センサー35が
作動して遮断弁36が作動して取り込まれていた気化ガ
スの流入が遮断され、遮断用ガス38が流入して液用調
節弁31が閉じ、LPGの供給も遮断されるようになっ
ている。上記遮断弁36は、非可逆構造になっているの
で、気化ガスの状態が正常に戻れば、リセットボタン3
9を押すことにより元の状態でLPGを気化させること
ができる。Here, when the heat of vaporization in the finned tube 32 is insufficiently absorbed, that is, when the vaporization becomes insufficient, the temperature of the temperature sensing tube 33 decreases as shown in FIG. When activated, the shutoff valve 36 is activated to shut off the inflow of the vaporized gas taken in, the shutoff gas 38 flows in, the liquid control valve 31 is closed, and the supply of LPG is also shut off. . Since the shut-off valve 36 has an irreversible structure, when the state of the vaporized gas returns to normal, the reset button 3
By pressing 9, the LPG can be vaporized in the original state.
【0013】[0013]
【発明が解決しようとする課題】上記方式は、太陽の輻
射熱、気温、風量によって気化熱の吸収量が左右され、
とくに気温と風量との関係で見ると、林立した鰭付き管
の風上側あるいは外側では大気の入れ替わりがあって気
化熱が充分に吸収できるが、風下あるいは内側は風通し
が悪く気化熱を充分吸収できない状態になる。In the above-mentioned method, the amount of vaporized heat absorbed depends on the radiant heat of the sun, temperature, and air volume.
Looking at the relationship between air temperature and air volume in particular, the air is exchanged on the windward or outer side of the finned tube with forests, so that the heat of vaporization can be sufficiently absorbed, but the leeward or inner side is poorly ventilated and cannot absorb the heat of vaporization sufficiently. State.
【0014】このような状態になるとLPGの気化とガ
スの消費とのバランスが崩れてLPGの供給が度々遮断
されてしまう問題が生ずる。In such a state, there arises a problem that the balance between the vaporization of LPG and the consumption of gas is lost, and the supply of LPG is frequently cut off.
【0015】この発明は上記従来技術問題に鑑み、鰭付
き管を林立させて大気中から気化熱を吸収する液化ガス
燃料の気化装置を効率よく稼働させるようにした液化ガ
ス燃料の気化装置を提供することを課題とする。The present invention has been made in view of the above-mentioned problems in the prior art, and provides a liquefied gas fuel vaporizer in which a finned tube is established to efficiently operate a liquefied gas fuel vaporizer that absorbs heat of vaporization from the atmosphere. The task is to
【0016】[0016]
【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、林立させた鰭付き管により大気中から気
化熱を吸収する液化ガス燃料の気化装置において、上記
鰭付き管の鰭を、その長さ方向で間欠的に切り欠きを設
けてなる構成としたものである。SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention relates to a liquefied gas fuel vaporizer for absorbing heat of vaporization from the atmosphere by means of a forest of finned tubes. , In which a notch is provided intermittently in the length direction.
【0017】上記の如く構成するこの発明にあっては、
鰭付き管の鰭を間欠的に切り欠くことによって、林立し
た鰭付き管の風下あるいは内部にも風通しが良くなり、
全ての鰭付き管から気化熱を吸収できるようになり、L
PGを効率よく気化させることができるようになる。In the present invention configured as described above,
By intermittently cutting out the fins of the finned tube, ventilation becomes better downwind or inside the forested finned tube,
The heat of vaporization can be absorbed from all finned tubes.
PG can be efficiently vaporized.
【0018】[0018]
【発明の実施の形態】次にこの発明の実施形態を図面を
参照しながら説明する。図1(a)はこの発明の一実施
例の正面図で、林立している鰭付き管21の鰭22を、
その長さ方向で一定間隔に切り欠き23している。切り
欠き23の寸法は、風通しの効果と鰭22の熱吸収効果
を考慮して実験的に決定される。Embodiments of the present invention will now be described with reference to the drawings. FIG. 1A is a front view of an embodiment of the present invention, in which a fin 22 of a finned tube 21 in a forest is shown.
Notches 23 are provided at regular intervals in the length direction. The size of the notch 23 is experimentally determined in consideration of the ventilation effect and the heat absorption effect of the fin 22.
【0019】図1(b)は平面図で鰭付き管1が林立し
ている状態が理解できる。このように鰭付き管21の鰭
22を間欠的に切り欠くことにより、そり切り欠き23
を通してX、Y、Zのいずれの方向でも空気が流通する
ようになり気化熱が充分吸収できるようになる。FIG. 1B is a plan view showing a state in which the finned tube 1 stands. By intermittently notching the fin 22 of the finned tube 21 in this manner, the sled notch 23
Through which air can flow in any of the X, Y, and Z directions, and the heat of vaporization can be sufficiently absorbed.
【0020】また、図3に示すように林立設置する鰭付
き管21を、傾斜させて設置することにより、吹き込ん
だ風の一部が矢印のように鰭22の切り欠き23の端に
当たって分流し、軸方向に流れを変えるので気化熱の吸
収効率を一層向上させることができる。Also, as shown in FIG. 3, the finned pipe 21 to be set up in a forest is installed at an angle so that a part of the blown wind hits the end of the notch 23 of the fin 22 as shown by the arrow and is diverted. Since the flow is changed in the axial direction, the efficiency of absorbing the heat of vaporization can be further improved.
【0021】[0021]
【発明の効果】以上説明したようにこの発明によれば、
林立させた鰭付き管全体に大気が入れ替わるようになっ
て気化熱の吸収効率が良くなり順当に気化ガスの供給が
行われる。As described above, according to the present invention,
The atmosphere is exchanged with the entire finned tube, thereby increasing the efficiency of absorbing the heat of vaporization and supplying the vaporized gas properly.
【図1】この発明に係る林立鰭付き管の(a)正面図、
(b)平面図FIG. 1A is a front view of a forest finned tube according to the present invention,
(B) Plan view
【図2】鰭付き管の拡大図Fig. 2 Enlarged view of finned tube
【図3】鰭付き管の傾斜配置図FIG. 3 is an oblique view of a finned tube
【図4】(a)LPGの気化制御系統図(正常時) (b)LPGの気化制御系統図(遮断時)FIG. 4 (a) LPG vaporization control system diagram (when normal) (b) LPG vaporization control system diagram (when shut off)
【図5】気化器を使用したガス発生設備の概略図(その
1)FIG. 5 is a schematic diagram of a gas generation facility using a vaporizer (part 1).
【図6】気化器を使用したガス発生設備の概略図(その
2)FIG. 6 is a schematic diagram of a gas generation facility using a vaporizer (part 2).
21 鰭付き管 22 鰭 23 切り欠き 21 Finned tube 22 Fin 23 Notch
Claims (1)
化熱を吸収する液化ガス燃料の気化装置において、上記
鰭付き管の鰭を、その長さ方向で間欠的に切り欠きを設
けてなることを特徴とする液化ガス燃料の気化装置。1. A liquefied gaseous fuel vaporizer that absorbs heat of vaporization from the atmosphere by means of a forest of finned tubes, wherein the fins of the finned tubes are provided with intermittent cutouts in the length direction thereof. A vaporizer for liquefied gas fuel, characterized in that:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11230256A JP2001056097A (en) | 1999-08-17 | 1999-08-17 | Carburetor for liquefied gas fuel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11230256A JP2001056097A (en) | 1999-08-17 | 1999-08-17 | Carburetor for liquefied gas fuel |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2001056097A true JP2001056097A (en) | 2001-02-27 |
Family
ID=16904962
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11230256A Pending JP2001056097A (en) | 1999-08-17 | 1999-08-17 | Carburetor for liquefied gas fuel |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2001056097A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003065860A (en) * | 2001-08-29 | 2003-03-05 | Ito Koki Kk | Temperature sensor for liquefied gas vaporizing device |
CN112503974A (en) * | 2020-11-06 | 2021-03-16 | 涡阳县华夏气体有限公司 | Gasifier for liquid oxygen |
-
1999
- 1999-08-17 JP JP11230256A patent/JP2001056097A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003065860A (en) * | 2001-08-29 | 2003-03-05 | Ito Koki Kk | Temperature sensor for liquefied gas vaporizing device |
CN112503974A (en) * | 2020-11-06 | 2021-03-16 | 涡阳县华夏气体有限公司 | Gasifier for liquid oxygen |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN2883869Y (en) | Liquefied natural gas gasifier | |
US10502368B2 (en) | Indirect fluid heater | |
US3724426A (en) | Hydrothermal liquefied petroleum gas vaporization system | |
US20160195116A1 (en) | Pressure management system for storage tank containing liquefied natural gas | |
WO2009124345A1 (en) | A heat pipe and a water heater using a heat pipe | |
US4203300A (en) | Horizontal direct fired water bath propane vaporizer | |
JP2001056097A (en) | Carburetor for liquefied gas fuel | |
KR101910530B1 (en) | Liquid natural gas vaporization | |
CN112924489B (en) | Low-temperature dangerous liquid accident leakage jet experiment device | |
CN208983341U (en) | Evaporation combustion device | |
JP2004309039A (en) | Integral liquefied gas vaporizer | |
JPS6216557Y2 (en) | ||
JP2907745B2 (en) | Line heater for city gas | |
JP2013119942A (en) | Vaporization system for liquefied gas | |
CN208123900U (en) | A kind of independently supplying system of light-hydrocarbon gas | |
CN217082170U (en) | Low-temperature liquid air-temperature type vaporization system | |
CN207270731U (en) | A kind of flammable liquid gas generator | |
JP2000039098A (en) | Evaporating device for bulk container | |
CN207280240U (en) | A kind of methyl alcohol vaporizing device | |
CN208169994U (en) | A kind of LNG vaporization device | |
CN208171077U (en) | A kind of NG temperature control device | |
KR970701336A (en) | SYSTEM AND METHOD FOR EVAPORATING MOISTURE FROM A GAP DEFINED BETWEEN AND REPAIR SLEEVE AND A SURROUNDING HEAT TRANSFER TUBE IN A NUCLEAR STEAM GENERATOR ) | |
CN201246988Y (en) | Vacuum phase-change heat exchanger | |
CN206958956U (en) | A kind of direct-fired liquified natural gas vaporizer | |
JPS60233444A (en) | Hot water supplier |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20060502 |
|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20090511 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20090519 |
|
A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 20091006 |