JPH0618146Y2 - LPG constant pressure liquid sending device - Google Patents

LPG constant pressure liquid sending device

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Publication number
JPH0618146Y2
JPH0618146Y2 JP1987185184U JP18518487U JPH0618146Y2 JP H0618146 Y2 JPH0618146 Y2 JP H0618146Y2 JP 1987185184 U JP1987185184 U JP 1987185184U JP 18518487 U JP18518487 U JP 18518487U JP H0618146 Y2 JPH0618146 Y2 JP H0618146Y2
Authority
JP
Japan
Prior art keywords
pressure
lpg
room temperature
liquid
pump
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 - Lifetime
Application number
JP1987185184U
Other languages
Japanese (ja)
Other versions
JPH0189699U (en
Inventor
弘將 扇
Original Assignee
石川島播磨重工業株式会社
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.)
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Application filed by 石川島播磨重工業株式会社 filed Critical 石川島播磨重工業株式会社
Priority to JP1987185184U priority Critical patent/JPH0618146Y2/en
Publication of JPH0189699U publication Critical patent/JPH0189699U/ja
Application granted granted Critical
Publication of JPH0618146Y2 publication Critical patent/JPH0618146Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【考案の詳細な説明】 〔産業上の利用分野〕 この考案はLPG(液化石油ガス)の常温タンクから圧
力を一定として供給先に送液する装置に関し、外気温に
よって変化する常温タンクの圧力に応じてポンプ動力を
最少とするようにしたものである。
[Detailed Description of the Invention] [Industrial field of application] The present invention relates to a device for sending a liquid from a room temperature tank of LPG (liquefied petroleum gas) to a supply destination with a constant pressure. Accordingly, the pump power is minimized.

〔従来の技術〕[Conventional technology]

プロパンやブタン等のLPG(液化石油ガス)を貯蔵す
るタンクのひとつに球形タンク等の常温タンクがあり、
これら常温タンクから常に一定圧力で消費先等に供給し
なければならない場合も多い。
One of the tanks that stores LPG (liquefied petroleum gas) such as propane and butane is a room temperature tank such as a spherical tank,
In many cases, it is necessary to always supply a constant pressure from these room temperature tanks to consumers.

このためLPG送液装置として圧力の常温タンクに送液
ポンプを付設し、送液ポンプで所定の圧力に加圧して供
給先に送るようにしている。
Therefore, as the LPG liquid sending device, a liquid sending pump is attached to a normal temperature tank, and the liquid sending pump pressurizes the liquid to a predetermined pressure and sends it to the supply destination.

〔考案が解決しようとする問題点〕[Problems to be solved by the invention]

ところが、このようなLPGの貯蔵設備では、プロパン
やブタン等のLPGを常温タンクに貯蔵するため、外気
温によって内部の圧力が変化し、例えばプロパンでは、
夏期に12kg/cm2程度となる一方、冬期は4kg/cm2程度
になり、ブタンでは、夏期に5kg/cm2程度となる一方、
冬期では0kg/cm2程度になってしまう(いずれもゲージ
圧)。
However, in such an LPG storage facility, LPG such as propane and butane is stored in a room temperature tank, so the internal pressure changes depending on the outside temperature.
In summer it is about 12kg / cm 2 , while in winter it is about 4kg / cm 2 , and in Butane it is about 5kg / cm 2 in the summer,
It becomes 0kg / cm 2 in winter (both gauge pressure).

このため送液ポンプの容量を一方圧力で圧送する供給先
との圧力差が最大となる冬期を基準に決定しなければな
らず、夏期には送液ポンプの容量が過大となってしま
う。
For this reason, the capacity of the liquid feed pump must be determined on the basis of the winter season when the pressure difference with the destination to which one-side pressure is fed is maximum, and the capacity of the liquid feed pump becomes excessive in the summer.

そこで、夏期には、送液ポンプの吐出側に弁を設けて絞
ることで調整しており、送液ポンプのポンプ動力が無駄
になっている。
Therefore, in the summer, a valve is provided on the discharge side of the liquid feed pump to adjust the valve, and the pump power of the liquid feed pump is wasted.

すなわち、送液ポンプの性能曲線を表わす第2図に示す
ように、吸込圧力が低い冬期の実揚程がhの場合には、
例えば管路等の抵抗曲線Rと揚程Hとの交点Aに対応す
る水量Qが送液でき、そのときの軸馬力は線図S上のa
点となるのに対し、夏期のように吸込圧力が高くなって
実揚程h′に低下する場合には、弁で絞るため管路等の
抵抗が増加して抵抗曲線がR″となり、冬期と同一水量
Qを確保すると、送液ポンプの軸馬力は線S上のaのま
まとなってしまい、図中、斜線で示す分だけポンプ動力
が無駄となっている。
That is, as shown in FIG. 2 which shows the performance curve of the liquid delivery pump, when the actual lift in winter when the suction pressure is low is h,
For example, the amount Q of water corresponding to the intersection A of the resistance curve R of the pipeline or the like and the head H can be sent, and the axial horsepower at that time is a on the diagram S.
On the other hand, when the suction pressure is high and drops to the actual pump head h ′ as in the summer, the resistance of the pipeline increases because the valve is throttled and the resistance curve becomes R ″. If the same amount of water Q is secured, the axial horsepower of the liquid delivery pump remains a on the line S, and the pump power is wasted by the amount shown by the diagonal lines in the figure.

特に、プロパンとブタンとを弁の切替えで1台の送液ポ
ンプで送液する設備では、夏期と冬期の圧力差が大きく
なって、一層ポンプ動力の無駄が多く、運転経費の増大
を招いてしまう。
In particular, in a facility that supplies propane and butane with a single liquid feed pump by switching valves, the pressure difference between summer and winter becomes large, resulting in much waste of pump power and an increase in operating costs. I will end up.

この考案はかかる従来技術を問題点に鑑みてなされたも
ので、吸込圧力の変化に応じてポンプ動力の無駄が発生
せず、運転経費を減少することができるLPG定圧送液
装置を提供しようとするものである。
The present invention has been made in view of the above problems in the prior art, and it is an object of the present invention to provide an LPG constant pressure liquid-feeding device that does not waste pump power according to a change in suction pressure and can reduce operating costs. To do.

〔問題点を解決するための手段〕[Means for solving problems]

上記問題点を解決するためこの考案は、LPGを常温状
態で貯蔵する複数の常温タンクから供給先に一定圧力で
送液する装置において、常温タンクからLPGを吸引し
て供給先に圧送する送液ポンプと、この送液ポンプから
の送出量を検出する流量検出器と、この送液ポンプと複
数の常温タンクとの間に設けられてLPGを送液する常
温タンクを切り換える弁および開閉状態の検出器と、各
常温タンク内の圧力をそれぞれ検出する圧力検出器と、
これら圧力検出器のうちLPGを送出する常温タンクか
らの検出信号を切り換える切換スイッチと、この切換ス
イッチを介して入力される吸引圧力の検出信号および流
量検出信号とで送液ポンプの回転数を制御して吐出圧を
一定にする回転数制御器とからなることを特徴とするも
のである。
In order to solve the above problems, the present invention is directed to an apparatus for feeding LPG from a plurality of room temperature tanks that store LPG at room temperature to a supply destination at a constant pressure, and a method for sucking LPG from the room temperature tank and pumping the LPG to the supply destination. A pump, a flow rate detector for detecting a delivery amount from the liquid delivery pump, a valve provided between the liquid delivery pump and a plurality of room temperature tanks for switching a room temperature tank for delivering LPG, and detection of an open / closed state And a pressure detector that detects the pressure in each room temperature tank,
Among these pressure detectors, the changeover switch that changes over the detection signal from the room temperature tank that sends out the LPG, and the suction pressure detection signal and the flow rate detection signal that are input via this changeover switch control the rotation speed of the liquid delivery pump. And a rotation speed controller for keeping the discharge pressure constant.

〔作用〕[Action]

LPGが貯蔵された常温タンク内の圧力を圧力検出器で
検出し、回転数制御器で必要な吐出圧力に見合うよう送
液ポンプの回転数を制御するようにしており、送液ポン
プを必要最小限のポンプ動力で運転するようにして無駄
を省き、運転経費の節約をはかっている。
The pressure in the room temperature tank where LPG is stored is detected by the pressure detector, and the rotation speed of the liquid feed pump is controlled by the rotation speed controller to match the required discharge pressure. By operating with limited pump power, waste is saved and operating costs are saved.

また、複数の常温タンクに異なる貯蔵液が貯蔵されてい
る場合でも、1台の送液ポンプで、その送出量を検出し
て回転数を制御するようにして一定圧力を保持して圧送
できるようになる。
Further, even when different storage liquids are stored in a plurality of room temperature tanks, one liquid feed pump detects the amount of the liquid feed and controls the number of rotations so that a constant pressure can be maintained and pressure fed. become.

〔実施例〕〔Example〕

以下、この考案の一実施例を図面に基づき詳細に説明す
る。
An embodiment of the present invention will be described below in detail with reference to the drawings.

第1図はこの考案のLPG定圧送液装置の一実施例にか
かる概略構成図である。
FIG. 1 is a schematic configuration diagram of an embodiment of the LPG constant pressure liquid feeding device of the present invention.

このLPG定圧送液装置10は、プロパンとブタンとを
それぞれ貯蔵する2つの常温タンク11,12から2つ
の弁13,14を切替えることで1台の送液ポンプ15
で供給先16に圧送するものである。
This LPG constant-pressure liquid-sending device 10 has a single liquid-sending pump 15 by switching two valves 13 and 14 from two room-temperature tanks 11 and 12 that store propane and butane, respectively.
The pressure is fed to the supply destination 16.

常温タンク11,12としては、例えば球形タンクが使
用され、常温状態で貯蔵できるよう耐圧容器としてあ
る。
As the room temperature tanks 11 and 12, for example, spherical tanks are used, which are pressure resistant containers that can be stored at room temperature.

これら常温タンク11,12の払出管にそれぞれ弁1
3,14が取付けられて送液ポンプ15の吸込側と連結
されており、これらの弁13,14には、弁の開閉状態
を検出する検出器が取付けられ、回転数制御器17に入
力されるようにしてある。
Valves 1 are provided on the pay-out pipes of these room temperature tanks 11 and 12, respectively.
3, 14 are attached and connected to the suction side of the liquid feed pump 15, and detectors for detecting the open / closed state of the valves are attached to these valves 13 and 14, and input to the rotation speed controller 17. I am doing it.

また、各常温タンク11,12には、内部の圧力を検出
する圧力検出器18,19が取付けてあり、検出信号が
切替スイッチ20を介して回転数制御器17に入力され
るようにしてある。
Further, pressure detectors 18 and 19 for detecting the internal pressure are attached to the room temperature tanks 11 and 12, respectively, and a detection signal is input to the rotation speed controller 17 via a changeover switch 20. .

さらに、送液ポンプ15の吐出側には、供給先16への
送液量を検出するための流量検出器21が介装してあ
り、回転数制御器17に検出信号が入力されるととも
に、供給先16にも圧力検出器22が取付けられ回転数
制御器17に検出信号が入力されるようになっている。
Further, on the discharge side of the liquid feed pump 15, a flow rate detector 21 for detecting the amount of liquid fed to the supply destination 16 is provided, and a detection signal is input to the rotation speed controller 17, and A pressure detector 22 is also attached to the supply destination 16 and a detection signal is input to the rotation speed controller 17.

この回転数制御器17では、常温タンク11,12の送
液に使用している方の圧力検出器18,19を切替スイ
ッチ20で選択して検出信号を入力させ、この圧力信号
から必要な吐出圧力に見合う送液ポンプ15の回転数を
演算し、送液ポンプ15に制御信号を出力して送液ポン
プ15の回転数を制御する。
In the rotation speed controller 17, the pressure detectors 18 and 19 used for liquid transfer to the room temperature tanks 11 and 12 are selected by the changeover switch 20 to input a detection signal, and the required discharge is made from this pressure signal. The number of rotations of the liquid feed pump 15 corresponding to the pressure is calculated, and a control signal is output to the liquid feed pump 15 to control the number of rotations of the liquid feed pump 15.

また、供給先16の圧力検出器22の検出信号に基づき
一定にすべき圧力に変動が生じた場合にも回転数制御器
17で送液ポンプ15の回転数を制御して一定にするよ
うにする。
Further, even when the pressure that should be made constant based on the detection signal of the pressure detector 22 of the supply destination 16 changes, the rotation speed controller 17 controls the rotation speed of the liquid feed pump 15 to keep it constant. To do.

かように構成したLPG定圧送液装置10によれば、2
つの常温タンク11,12のうち圧送すべき一方の常温
タンク、例えば常温タンク11の圧力を検出するよう切
替スイッチ20を切替えるとともに、送液ポンプ15に
通じる弁13を開いた状態とすると、回転数制御器17
で供給先16に必要な吐出圧力に見合う送液ポンプ15
の回転数が演算され、送液ポンプ15の駆動用電動機の
電源装置のインバータ等に制御信号が出力されて送液ポ
ンプ15が運転される。
According to the LPG constant pressure liquid-feeding device 10 configured as described above, 2
If one of the two room temperature tanks 11 and 12 to be pressure-fed, for example, the changeover switch 20 is switched to detect the pressure of the room temperature tank 11 and the valve 13 leading to the liquid supply pump 15 is opened, Controller 17
And the liquid delivery pump 15 that matches the discharge pressure required for the supply destination 16
Is calculated, and a control signal is output to an inverter or the like of the power supply device of the driving motor of the liquid feed pump 15 to operate the liquid feed pump 15.

これを第2図に示す送液ポンプ15の性能曲線で説明す
る。
This will be described with reference to the performance curve of the liquid delivery pump 15 shown in FIG.

まず、冬期等で常温タンク11内の圧力が低い場合に
は、供給先16への吐出圧力を高くする必要があり、そ
の実揚程がhであるとすると、配管系などから抵抗曲線
Rが得られる。
First, when the pressure in the room temperature tank 11 is low in winter or the like, it is necessary to increase the discharge pressure to the supply destination 16, and assuming that the actual head is h, the resistance curve R is obtained from the piping system or the like. .

また、送液ポンプ15の回転数をNとした場合の揚程曲
線Hと軸馬力の線図Sも図のようになり、揚水量がQと
なるとともに、軸馬力は線図S上のa点となる。
Further, when the number of rotations of the liquid feed pump 15 is N, the lift curve H and the shaft horsepower diagram S are also as shown in the figure, and the pumping amount is Q and the shaft horsepower is point a on the diagram S. Becomes

次に、夏期等で常温タンク11内の圧力が上昇した場合
には、送液ポンプ15の吸込圧力が上昇することになっ
て実揚程がh′に低下する一方、配管系などの抵抗は変
化しないことから抵抗曲線Rを平行移動した抵抗曲線
R′(破線)になる。
Next, when the pressure in the room temperature tank 11 rises in the summer or the like, the suction pressure of the liquid feed pump 15 rises and the actual lift decreases to h ', while the resistance of the piping system changes. Since this is not done, the resistance curve R is translated into a resistance curve R '(broken line).

そして、この場合にも冬期等と同一の揚水量Qを確保す
るとすれば、揚水量Qと抵抗曲線R′との交点Xが求め
られる。
Also in this case, if the same pumping amount Q as in the winter season is secured, the intersection X between the pumping amount Q and the resistance curve R'is obtained.

そこで、送液ポンプ15の回転数を低くして点Xを通る
揚程曲線H′(破線)が得られる回転数N′を回転数制
御器17で演算し、この回転数N′で送液ポンプ15を
運転する。
Therefore, the rotation speed controller 17 calculates the rotation speed N ′ at which the rotation speed of the liquid feed pump 15 is lowered to obtain a lift curve H ′ (broken line) passing through the point X, and the liquid feed pump is operated at this rotation speed N ′. Drive 15

この回転数をN′とした場合の揚程曲線H′に対応する
軸馬力は直線S′(破線)となり、揚水量Qとした場合
に必要な軸馬力は線図S′上の点bとなり、ポンプ動力
が低下することがわかる。
The shaft horsepower corresponding to the lift curve H'when the number of revolutions is N'is a straight line S '(broken line), and the shaft horsepower required when the pumping amount is Q is a point b on the diagram S'. It can be seen that the pump power decreases.

このように、常温タンク11,12内の圧力を圧力検出
器18,19で検出し、供給先16で必要な吐出圧に見
合う送液ポンプ15の回転数N,N′を求めて運転する
ので、ポンプ動力の無駄がなく、効率的に運転できる。
In this way, the pressures in the room temperature tanks 11 and 12 are detected by the pressure detectors 18 and 19, and the number of rotations N and N'of the liquid feed pump 15 corresponding to the discharge pressure required at the supply destination 16 is obtained to operate. The pump can be operated efficiently without waste of power.

なお、上記実施例では、1台の送液ポンプで2つの常温
タンクを切替えて使用する場合で説明したが、さらに複
数の常温タンクを切替えて使用する場合にも適用でき
る。また、LPGもプロパンとブタンに限定するもので
ない。
In the above embodiment, the case where two normal temperature tanks are switched and used by one liquid feed pump has been described, but it is also applicable when a plurality of normal temperature tanks are switched and used. Also, LPG is not limited to propane and butane.

〔考案の効果〕[Effect of device]

以上、一実施例とともに具体的に説明したようにこの考
案のLPG定圧送液装置によれば、LPGが貯蔵された
常温タンク内の圧力を圧力検出器で検出し、回転数制御
器で必要な吐出圧力に見合うよう送液ポンプの回転数を
制御するようにしたので、送液ポンプを常に必要最小限
のポンプ動力で運転することができ、運転経費の節約が
できる。また、複数の常温タンクに異なる貯蔵液が貯蔵
されている場合でも、1台の送液ポンプで、その送出量
を検出して回転数を制御することで、一定圧力を保持し
て圧送することができる。
As described above in detail with reference to the embodiment, according to the LPG constant-pressure liquid-feeding device of the present invention, the pressure in the room temperature tank storing LPG is detected by the pressure detector and required by the rotation speed controller. Since the rotation speed of the liquid feed pump is controlled so as to match the discharge pressure, the liquid feed pump can always be operated with the minimum required pump power, and operating costs can be saved. Further, even when different storage liquids are stored in a plurality of room temperature tanks, a single liquid feed pump detects the delivery amount and controls the number of revolutions to maintain a constant pressure for pressure delivery. You can

【図面の簡単な説明】[Brief description of drawings]

第1図および第2図はこの考案のLPG定圧送液装置の
一実施例にかかる概略構成図および性能曲線の説明図で
ある。 10…LPG定圧送液装置、11,12…常温タンク、
13,14…弁、15…送液ポンプ、16…供給先、1
7…回転数制御器、18,19,22…圧力検出器、2
0…切替スイッチ、21…流量検出器。
FIG. 1 and FIG. 2 are a schematic configuration diagram and an explanatory diagram of a performance curve according to an embodiment of the LPG constant pressure liquid sending device of the present invention. 10 ... LPG constant pressure liquid sending device, 11, 12 ... Room temperature tank,
13, 14 ... Valve, 15 ... Liquid feed pump, 16 ... Supply destination, 1
7 ... Revolution speed controller, 18, 19, 22 ... Pressure detector, 2
0 ... Changeover switch, 21 ... Flow rate detector.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】LPGを常温状態で貯蔵する複数の常温タ
ンクから供給先に一定圧力で送液する装置において、常
温タンクからLPGを吸引して供給先に圧送する送液ポ
ンプと、この送液ポンプからの送出量を検出する流量検
出器と、この送液ポンプと複数の常温タンクとの間に設
けられてLPGを送液する常温タンクを切り換える弁お
よび開閉状態の検出器と、各常温タンク内の圧力をそれ
ぞれ検出する圧力検出器と、これら圧力検出器のうちL
PGを送出する常温タンクからの検出信号を切り換える
切換スイッチと、この切換スイッチを介して入力される
吸引圧力の検出信号および流量検出信号とで送液ポンプ
の回転数を制御して吐出圧を一定にする回転数制御器と
からなることを特徴とするLPG定圧送液装置。
1. An apparatus for feeding LPG from a plurality of room temperature tanks that store LPG in a room temperature state to a supply destination at a constant pressure, and a liquid supply pump that sucks LPG from the room temperature tank and pressure-transmits the LPG to the supply destination. A flow rate detector for detecting the amount delivered from the pump, a valve provided between the liquid delivery pump and a plurality of room temperature tanks for switching the room temperature tank for delivering the LPG and a detector for opening / closing state, and each room temperature tank The pressure detectors that detect the internal pressure, respectively, and L of these pressure detectors
The changeover switch that switches the detection signal from the room temperature tank that sends out PG, and the suction pressure detection signal and the flow rate detection signal that are input via this changeover switch are used to control the number of revolutions of the liquid feed pump to keep the discharge pressure constant. The LPG constant pressure liquid-feeding device, comprising:
JP1987185184U 1987-12-04 1987-12-04 LPG constant pressure liquid sending device Expired - Lifetime JPH0618146Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1987185184U JPH0618146Y2 (en) 1987-12-04 1987-12-04 LPG constant pressure liquid sending device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1987185184U JPH0618146Y2 (en) 1987-12-04 1987-12-04 LPG constant pressure liquid sending device

Publications (2)

Publication Number Publication Date
JPH0189699U JPH0189699U (en) 1989-06-13
JPH0618146Y2 true JPH0618146Y2 (en) 1994-05-11

Family

ID=31476511

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1987185184U Expired - Lifetime JPH0618146Y2 (en) 1987-12-04 1987-12-04 LPG constant pressure liquid sending device

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001004096A (en) * 1999-06-23 2001-01-09 Nippon Sanso Corp Gas supply method and device therefor

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59107400U (en) * 1983-01-10 1984-07-19 石川島播磨重工業株式会社 Liquefied natural gas delivery pressure control device

Also Published As

Publication number Publication date
JPH0189699U (en) 1989-06-13

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