JPS6318071B2 - - Google Patents

Info

Publication number
JPS6318071B2
JPS6318071B2 JP54118802A JP11880279A JPS6318071B2 JP S6318071 B2 JPS6318071 B2 JP S6318071B2 JP 54118802 A JP54118802 A JP 54118802A JP 11880279 A JP11880279 A JP 11880279A JP S6318071 B2 JPS6318071 B2 JP S6318071B2
Authority
JP
Japan
Prior art keywords
gas
pressure
air
raw material
mixer
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
Application number
JP54118802A
Other languages
Japanese (ja)
Other versions
JPS5642799A (en
Inventor
Satoo Akyama
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BUYO GASU KK
Original Assignee
BUYO GASU KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by BUYO GASU KK filed Critical BUYO GASU KK
Priority to JP11880279A priority Critical patent/JPS5642799A/en
Publication of JPS5642799A publication Critical patent/JPS5642799A/en
Publication of JPS6318071B2 publication Critical patent/JPS6318071B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 (産業上の利用分野) この発明は、ブタンその他の液化ガスを原料と
して一般需要家にガスを低圧供給する方法に関す
るものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for supplying gas to general consumers at low pressure using butane or other liquefied gas as a raw material.

(従来技術とその問題点) 従来のガス供給は、第1図に示すような装置に
よつて行なわれている。
(Prior art and its problems) Conventional gas supply is carried out by a device as shown in FIG.

即ち、ブタン等の液化燃料は、貯槽1からポン
プ2によつてベーパーライザーミキサー3に供給
され温水加熱式ガス発生機4によつてガス化され
て原料ガスとされ、圧力調整弁5で調圧されてベ
ンチユリー管6で所容量の空気と混合されて有水
式低圧ガスホルダー7に貯められる。
That is, liquefied fuel such as butane is supplied from a storage tank 1 to a vapor riser mixer 3 by a pump 2, is gasified by a hot water heating type gas generator 4, and is made into a raw material gas, and the pressure is regulated by a pressure regulating valve 5. The gas is mixed with a predetermined amount of air in a ventilator tube 6 and stored in a water-type low-pressure gas holder 7.

而して、この貯留ガスを需要家に供給するには
ブロワー8によつて加圧し、圧力調整弁9によつ
て所定のガス圧として供給するのである。
In order to supply this stored gas to consumers, it is pressurized by a blower 8 and supplied at a predetermined gas pressure by a pressure regulating valve 9.

この方法では原料ガスと空気の混合比即ち発熱
量を正確に規定するのが困難である。
In this method, it is difficult to accurately define the mixing ratio of raw material gas and air, that is, the calorific value.

ブロワー8は常時最大能力で運転されており需
要量の少ないときは余分の加圧ガスをガスホルダ
ー7に環流させる方式であるから多大の電力を要
する他、加圧供給であるから導管10の途中に設
けられる水取器11内に溜る水量が多くなり採水
作業を頻繁に行う必要がある。
The blower 8 is always operated at maximum capacity, and when the demand is low, excess pressurized gas is circulated to the gas holder 7, which requires a large amount of electric power. The amount of water that accumulates in the water collector 11 installed in the tank increases, and it is necessary to perform water sampling work frequently.

また、停電時に備えてブロワー運転用その他の
電源用発電機として大容量のジーゼル発電機等が
必要になり電力施設が大型にならざるを得ないの
みならずガスを圧縮するため安全対策に多額の費
用を要する。
In addition, large-capacity diesel generators are required to operate blowers and other power sources in case of power outages, which not only forces the power facilities to become larger, but also requires a large amount of money for safety measures because the gas is compressed. It costs money.

(目 的) 本発明は、比較的簡単な装置によつて所望する
正確な混合比が得られる他、混合ガス中の水分含
量が少なくなりしかも従来必要であつたガス供給
用ブロワーを不要にして電力を節減できるガス供
給方法を提供するものであり、ブロワーを不要に
したことに伴つてこれに付属する予備的電力設備
も不要にできるのである。
(Purpose) The present invention not only allows a desired accurate mixing ratio to be obtained using a relatively simple device, but also reduces the water content in the mixed gas, and eliminates the need for a gas supply blower, which was conventionally required. This provides a gas supply method that can save electricity, and since the blower is not needed, the backup power equipment attached to it can also be made unnecessary.

(構 成) 本発明は、原料ガスとこれに混合すべき除湿加
圧空気を同圧力としてこれらを所望する混合比に
比例した口径比を有するオリフイスを通してミキ
サーに供給して一挙に所定熱量を有する加圧混合
ガスとしてタンクに貯蔵し、この混合ガスをガバ
ナーによつて0.02〜1.0Kg/cm2の圧力に減圧して
末端需要家に供給するものであつて、ガスタンク
と工場出口の間にはブロワーその他のガス加圧圧
送設備を必要としない特長を有するものである。
(Structure) The present invention supplies raw material gas and dehumidified pressurized air to be mixed with the same pressure to a mixer through an orifice having an aperture ratio proportional to a desired mixing ratio, thereby generating a predetermined amount of heat all at once. This system stores a pressurized mixed gas in a tank, reduces the pressure to 0.02 to 1.0 Kg/cm 2 using a governor, and supplies it to end users. It has the advantage of not requiring a blower or other gas pressurization and pressure feeding equipment.

(実施装置及び作用) 本発明の実施に適用される装置は第2図に示す
ようであつて、原料はポンプ20及びリリーフ弁
21により5〜6Kg/cm2に調整されてガス発生装
置22に導入されてガス化される。23は温水加
熱式ガス発生器、24は圧力調整弁であつて発生
ガスは3.0Kg/cm2に整圧される。
(Implementation equipment and operation) The equipment applied to the implementation of the present invention is as shown in FIG . introduced and gasified. 23 is a hot water heating type gas generator, 24 is a pressure regulating valve, and the pressure of the generated gas is regulated to 3.0 kg/cm 2 .

一方、混合用加圧空気は圧縮機又はブロワー2
5により7Kg/cm2程度に圧縮され冷却器26で冷
却されて除湿され、この除湿加圧空気(ドライエ
アー)はタンク27に溜められる。このドライエ
アーは供給管Bに設けた均圧弁28によつてその
二次側においてガス供給管A内の圧力P1と等し
い圧力に減圧される。
On the other hand, the pressurized air for mixing is supplied by the compressor or blower 2.
5 to about 7 kg/cm 2 , cooled and dehumidified by a cooler 26 , and this dehumidified pressurized air (dry air) is stored in a tank 27 . This dry air is reduced in pressure to a pressure equal to the pressure P 1 in the gas supply pipe A on its secondary side by a pressure equalizing valve 28 provided in the supply pipe B.

即ち、均圧弁28のダイヤフラムには導管29
によつてP1の圧力が印加されこの圧力によつて
均圧弁28の弁開度がカウンタスプリングに抗し
て可変され均圧弁28の二次側圧力P2は常にP1
と等しくなるように調節されている。
That is, the diaphragm of the pressure equalizing valve 28 is connected to the conduit 29.
, a pressure P 1 is applied, and this pressure changes the opening degree of the pressure equalizing valve 28 against the counter spring, so that the secondary side pressure P 2 of the pressure equalizing valve 28 is always P 1
is adjusted to be equal to

ガス用オリフイスOfaとエアーオリフイスOfb
は所望の混合比、例えば、24:76に比例した口径
比に設定された固定オリフイスである。ガス圧力
P1とエア圧力P2はP1=P2であるからミキサー3
0では上記設定比率で混合が行なわれタンク31
に貯められる。而して、各需要家へはガバナー3
2により0.02〜1.0Kg/cm2として導管10を通じ
て供給する。
Gas orifice Ofa and air orifice Ofb
is a fixed orifice set to a diameter ratio proportional to the desired mixing ratio, e.g. 24:76. gas pressure
Since P 1 and air pressure P 2 are P 1 = P 2 , mixer 3
At 0, mixing is performed at the above set ratio and the tank 31
can be stored in Therefore, governor 3 is sent to each consumer.
2 is supplied through conduit 10 as 0.02 to 1.0 Kg/cm 2 .

(効 果) 上記した如く本発明方法によれば、ガスとエア
ーの混合量が混合比に比例して設定した口径を有
する2ケのオリフイスのみで決定されるので安定
性が高い他、それらの圧力調節に複雑な制御系を
導入せずに1個の均圧弁で簡単に達成できるので
ある。なお圧力調節手段として公知の圧力調節器
を使用できること勿論である。
(Effects) As described above, according to the method of the present invention, the mixing amount of gas and air is determined only by two orifices whose diameters are set in proportion to the mixing ratio, so it is highly stable and This can be easily achieved with a single pressure equalization valve without introducing a complicated control system for pressure regulation. It goes without saying that a known pressure regulator can be used as the pressure regulating means.

更に、工場出口に圧送機を全然必要としないか
ら電力を要せずしかも混合空気が一度加圧されて
ドライエアーとされているので導管内に凝縮する
水分は極めて少量になる。
Furthermore, since there is no need for a pressure feeder at the factory outlet, no electricity is required, and since the mixed air is once pressurized to become dry air, the amount of moisture that condenses in the conduit is extremely small.

また、停電の場合も短時間であればガスタンク
31の容量により供給を継続できるのでポンプ2
0及びエアーコンプレツサー25を駆動する僅か
の電力でよいから発電装置が小規模で済む。
In addition, even in the event of a power outage, the pump 2 can continue supplying the gas tank 31 for a short time.
Since only a small amount of electric power is required to drive the air compressor 25 and the air compressor 25, the power generation device can be small-scale.

この場合において、コンプレツサー25の被圧
縮物はエアーであるからコンプレツサーの原動力
としてガスエンジン等を直結しておいても安全で
あり、発電機を介在しないから効率もよい。叙上
の如く本発明ガス供給方法は従来のガス供給方法
に較べ消費電力は格段に少なくて済みこれだけで
も経済的であるのに加えて、停電時の電源確保も
容易且つ安価にできるので装置全体の経済性は頗
る向上する。
In this case, since the material to be compressed by the compressor 25 is air, it is safe to directly connect a gas engine or the like as the motive force for the compressor, and efficiency is also good because no generator is involved. As mentioned above, the gas supply method of the present invention consumes much less power than the conventional gas supply method, which is not only economical, but also makes it easy and inexpensive to secure power during a power outage, so the entire device can be The economic efficiency of the system will be significantly improved.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来法によるガス供給その概要図、第
2図は本発明方法に適用する装置の概要図であ
る。
FIG. 1 is a schematic diagram of gas supply according to a conventional method, and FIG. 2 is a schematic diagram of an apparatus applied to the method of the present invention.

Claims (1)

【特許請求の範囲】[Claims] 1 液化ガスを原料としてガスを低圧供給する方
法において、ガス化された原料ガスと、このガス
圧力と等圧にした混合用除湿加圧空気を、夫々所
定の混合比に比例した口径比を有するオリフイス
を通してミキサーに導入し、該ミキサー内で混合
された混合ガスをその圧力のままガスタンクに貯
蔵しガバナーを通して各需要家に減圧供給するこ
とを特徴とするガス供給方法。
1 In a method of supplying gas at low pressure using liquefied gas as a raw material, the gasified raw material gas and the dehumidified pressurized air for mixing, which is made equal to the gas pressure, each have an aperture ratio proportional to a predetermined mixing ratio. A gas supply method characterized by introducing the mixed gas into a mixer through an orifice, storing the mixed gas in the mixer at that pressure in a gas tank, and supplying the gas to each customer under reduced pressure through a governor.
JP11880279A 1979-09-18 1979-09-18 Gas feed system Granted JPS5642799A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11880279A JPS5642799A (en) 1979-09-18 1979-09-18 Gas feed system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11880279A JPS5642799A (en) 1979-09-18 1979-09-18 Gas feed system

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP15336179A Division JPS5644035A (en) 1979-11-26 1979-11-26 Fluid mixing device

Publications (2)

Publication Number Publication Date
JPS5642799A JPS5642799A (en) 1981-04-21
JPS6318071B2 true JPS6318071B2 (en) 1988-04-16

Family

ID=14745475

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11880279A Granted JPS5642799A (en) 1979-09-18 1979-09-18 Gas feed system

Country Status (1)

Country Link
JP (1) JPS5642799A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH035367U (en) * 1989-06-09 1991-01-18
US9062372B2 (en) 2002-08-01 2015-06-23 Applied Materials, Inc. Self-ionized and capacitively-coupled plasma for sputtering and resputtering

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0121222Y2 (en) * 1985-06-25 1989-06-26
CN107261874A (en) * 2017-08-18 2017-10-20 云南省环境科学研究院(中国昆明高原湖泊国际研究中心) A kind of high-precision volatile materials air distribution system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH035367U (en) * 1989-06-09 1991-01-18
US9062372B2 (en) 2002-08-01 2015-06-23 Applied Materials, Inc. Self-ionized and capacitively-coupled plasma for sputtering and resputtering

Also Published As

Publication number Publication date
JPS5642799A (en) 1981-04-21

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