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JPH07103871B2 - Water pressure control method - Google Patents
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JPH07103871B2 - Water pressure control method - Google Patents

Water pressure control method

Info

Publication number
JPH07103871B2
JPH07103871B2 JP2008785A JP2008785A JPH07103871B2 JP H07103871 B2 JPH07103871 B2 JP H07103871B2 JP 2008785 A JP2008785 A JP 2008785A JP 2008785 A JP2008785 A JP 2008785A JP H07103871 B2 JPH07103871 B2 JP H07103871B2
Authority
JP
Japan
Prior art keywords
pump
pumps
parallel
bypass valve
pressure
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
JP2008785A
Other languages
Japanese (ja)
Other versions
JPS61180315A (en
Inventor
潤一 上野
一幸 神村
Original Assignee
山武ハネウエル株式会社
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.)
Filing date
Publication date
Application filed by 山武ハネウエル株式会社 filed Critical 山武ハネウエル株式会社
Priority to JP2008785A priority Critical patent/JPH07103871B2/en
Publication of JPS61180315A publication Critical patent/JPS61180315A/en
Publication of JPH07103871B2 publication Critical patent/JPH07103871B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B49/00Control, e.g. of pump delivery, or pump pressure of, or safety measures for, machines, pumps, or pumping installations, not otherwise provided for, or of interest apart from, groups F04B1/00 - F04B47/00
    • F04B49/10Other safety measures
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B49/00Control, e.g. of pump delivery, or pump pressure of, or safety measures for, machines, pumps, or pumping installations, not otherwise provided for, or of interest apart from, groups F04B1/00 - F04B47/00
    • F04B49/22Control, e.g. of pump delivery, or pump pressure of, or safety measures for, machines, pumps, or pumping installations, not otherwise provided for, or of interest apart from, groups F04B1/00 - F04B47/00 by means of valves
    • F04B49/24Bypassing

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Control Of Non-Positive-Displacement Pumps (AREA)
  • Control Of Positive-Displacement Pumps (AREA)
  • Feedback Control In General (AREA)
  • Control Of Fluid Pressure (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、空調制御装置等において用いられるポンプ群
からの送水圧力(吐出圧力)を制御する方法に関するも
のである。
TECHNICAL FIELD The present invention relates to a method for controlling a water supply pressure (discharge pressure) from a pump group used in an air conditioning control device or the like.

〔従来の技術〕[Conventional technology]

空調制御装置においては、空調用の給水を送水するため
ポンプを用いているが、空調負荷の変動に対処する目的
上、複数台のポンプを並列に接続し、このうちの例えば
1台を可変回転数としたうえ、一定範囲の負荷変動に応
じて回転数を制御すると共に、これによる対処範囲を超
える負荷変動に対しては、他のポンプの列運転台数を制
御するものとなっている。
In the air-conditioning control device, a pump is used to feed the water supply for air-conditioning, but in order to cope with fluctuations in the air-conditioning load, multiple pumps are connected in parallel, and for example, one of them can be variably rotated. The number of rotations is controlled according to the load fluctuation within a certain range, and the number of other pumps operating in a row is controlled when the load fluctuation exceeds the coping range.

第4図は、従来の空調装置におけるポンプ群を示す計装
図であり、可変回転数のポンプ11および固定回転数のポ
ンプ12〜1nがヘッダ21および22を介して並列に接続さ
れ、入力側の管路3からの還水をもどし、出力側の管路
4を介して図上省略した空調器へ圧送する。
Figure 4 is a instrumentation diagram showing a pump unit of the conventional air conditioning system, the pump 1 2 to 1 n of the variable rotational speed of the pump 1 1 and the fixed speed in parallel through a header 2 1 and 2 2 It is connected and returns the return water from the input side pipe 3 and pressure-feeds it to the air conditioner (not shown) via the output side pipe 4.

ポンプ11の最大能力はポンプ12〜1nと同能力となってお
り、すなわちポンプ11の最大回転数とポンプ12〜1nの固
定回転数とは等しく設定されており、制御装置9が、図
上省略した経路により与えられる空調状況のデータ(吐
出圧力値や補正データ)に応じて制御演算を行ない、こ
の結果も加味して、制御盤10を介しポンプ11の回転数を
制御すると共に、ポンプ12〜1nに対しては起動および停
止の指令を送出し、これらに対する並列運転の台数制御
を行なう。
Maximum capacity of pump 1 1 is a pump 1 2 to 1 n the same capacity, that is, is set equal to the maximum rotation speed and the pump 1 2 to 1 n fixed rotational speed of the pump 1 1, the control device 9 may perform the control operation according to the data of the air conditioning status provided by routes drawing omitted (discharge pressure value and correction data), this results in consideration, the rotational speed of the pump 1 1 via the control panel 10 and controls, for the pump 1 2 to 1 n transmits a command for start and stop, performs controlling the number of parallel operations for these.

すなわち、今、ポンプ11のみの運転により給水を行って
いるものとした場合、ポンプ11のみの運転では増大する
空調負荷に対処できないと判断すると、ポンプ11に加え
てポンプ12を運転(増設)する。例えば、空調負荷に対
応する量として現在の必要流量Fを求め、この必要流量
Fがポンプ11を最大能力(最大回転数)で回転させた場
合に供給可能な最大流量F1を越えていれば、ポンプ11
加えてポンプ12を運転する。
That is, the operation now, when it is assumed that is performing the water supply by the operation of only the pump 1 1, when the operation of only the pump 1 1 determines that it is unable to cope with the air conditioning load increases, the pump 1 2 In addition to the pump 1 1 (Add). For example, determine the current required flow rate F as an amount corresponding to the air-conditioning load, if it exceeds the maximum flow F1 can be supplied when the required flow rate F rotates the pump 1 1 at maximum capacity (maximum rotation speed) , to operate the pump 1 2 in addition to the pump 1 1.

これに対し、ポンプ11とポンプ12および13(図示せず)
との並列運転では減少する空調負荷に対し不経済となる
と判断すると、ポンプ13の運転を停止(減段)する。例
えば、空調負荷に対応する量として現在の必要流量Fを
求め、この必要流量Fがポンプ11と12とを最大能力で回
転させた場合に供給可能な最大流量F2を下回っていれ
ば、ポンプ13の運転を停止する。
In contrast, pump 1 1 and pumps 1 2 and 1 3 (not shown)
If it is determined that uneconomical to decrease the air-conditioning load in parallel operation with, stops the operation of the pump 1 3 (reduction stages) to. For example, determine the current required flow rate F as an amount corresponding to the air-conditioning load, if it is below the maximum flow F2 can be supplied when the required flow rate F rotates the pump 1 1 and 1 2 at maximum capacity, Stop operation of pump 1 3 .

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

しかしながら、このような台数制御方法によると、例え
ばポンプ11とポンプ12との並列運転の際、ポンプ12の出
口の送水圧力P12に対してポンプ11の出口の送水圧力P11
が大きく低下した場合、すなわちポンプ11の回転数が低
回転制御されその送水圧力P11がP12に対して大きく低下
した場合、ポンプ11からのヘッダ22への送水が抑圧され
て滞留し、この滞留する水の運動エネルギーが熱エネル
ギーに変わって配管121が破損したり、最悪の条件では
ポンプ11が破損する等の問題を生ずる。
However, according to such a unit count control method, such as a pump 1 1 and when parallel operation of the pumps 1 2, pump 1 1 of the outlet of the water supply pressure P1 1 against water pressure P1 2 of the pump 1 second outlet
If drops significantly, that is, when the rotational speed of the pump 1 1 is the water supply pressure P1 1 is low rotation control is greatly reduced relative to P1 2, water is suppressed retention of the header 2 2 from the pump 1 1 However, the kinetic energy of the accumulated water is changed to thermal energy, and the pipe 12 1 is damaged, or the pump 11 is damaged under the worst conditions.

このため、並列運転の際は、ポンプ11に回転数の下限値
を定め、ヘッダ22への送水を滞留させないようにするこ
とが考えられている。
Therefore, when the parallel operation is established a lower limit value of the rotational speed to the pump 1 1, it is considered so as not to stay the water to the header 2 2.

しかし、この方法では、ポンプ11が下限値の回転数に達
した状態で、微少な空調負荷の軽減に応じて図示せぬ別
途の制御装置により空調器2方弁の開度が絞られると、
還水の流量が減少し、ヘッダ22において吐出圧力PTが上
昇する。吐出圧力PTが過剰に上昇すると、これに抑圧さ
れてポンプ11からのヘッダ22への送水が滞留し、配管12
1が破損したり、ポンプ11が破損する等の問題が生ず
る。
However, in this method, in a state in which the pump 1 1 has reached a rotational speed lower limit value, when the air conditioner 2-way valve opening is restricted by a separate controller (not shown) in accordance with the reduction of fine air conditioning load ,
Flow rate of Kaemizu is reduced, the discharge pressure P T is increased in the header 2 2. When the discharge pressure P T rises excessively, it is suppressed and the water sent from the pump 1 1 to the header 2 2 accumulates, and the pipe 12
1 is damaged, problems arise such as the pump 1 1 may be damaged.

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

前述の問題を解決するため、本発明はつぎの手段により
構成するものとなっている。
In order to solve the above-mentioned problems, the present invention comprises the following means.

すなわち、上述のポンプ群において、このポンプ群の出
力側と入力側との間へバイパス弁を設け、かつ、可変回
転数のポンプの回転数に固定回転数のポンプの並列運転
台数の増加に従って上昇する下限値を定め、ポンプ群の
出力側と入力側との差圧に応じてバイパス弁の開度を制
御すると共に、バイパス弁が開き始める差圧を固定回転
数のポンプの並列運転台数が増加するに従って小さくす
るようにしている。
That is, in the above-mentioned pump group, a bypass valve is provided between the output side and the input side of this pump group, and the number of rotations of the variable rotation speed pump increases as the number of parallel operation pumps of fixed rotation speed increases. The lower limit value is set and the opening of the bypass valve is controlled according to the pressure difference between the output side and the input side of the pump group, and the differential pressure at which the bypass valve starts to open increases the number of parallel pumps operating at fixed speed. I try to make it smaller as I do.

〔作用〕[Action]

したがって、この発明によれば、固定回転数のポンプの
並列運転台数が増加するに従って可変回転数のポンプの
回転数の下限値が上昇し、また固定回転数のポンプの並
列運転台数が増加するに従ってバイパス弁が開き始める
差圧が小さくなり、ポンプ群からの吐出圧力の過剰上昇
分が固定回転数のポンプの並列運転台数が多い程早期に
バイパス弁によって側路されるものとなり、これにより
可変回転数ポンプが下限値の回転数に達した状態で吐出
圧力が過剰に上昇することがなくなり、可変回転数のポ
ンプからの送水の滞留が生じないものとなる。
Therefore, according to the present invention, the lower limit value of the rotational speed of the variable speed pump increases as the number of parallel operating pumps of the fixed rotational speed increases, and as the number of parallel operating pumps of the fixed rotational speed increases. The differential pressure at which the bypass valve starts to open becomes small, and the excessive increase in the discharge pressure from the pump group is bypassed by the bypass valve as soon as the number of parallel operating pumps with a fixed rotational speed increases. The discharge pressure will not excessively rise in the state where several pumps have reached the lower limit rotation speed, and the retention of the water supply from the pumps of variable rotation speed will not occur.

〔実施例〕〔Example〕

以下、実施例を示す図によって本発明の詳細を説明す
る。
Hereinafter, the present invention will be described in detail with reference to the drawings showing examples.

第1図はポンプ群を示す計装図である。同図において、
第4図と同一符号は同一あるいは同等構成要素を示し、
その説明は省略する。
FIG. 1 is an instrumentation diagram showing a pump group. In the figure,
The same reference numerals as those in FIG. 4 denote the same or equivalent components,
The description is omitted.

本実施例においては、出力側と入力側との各管路4,3の
間に、分岐管路5,6を介してバイパス弁7を設けてお
り、この両端の差圧P′を差圧センサ8によって検出
し、これの検出出力に応じて制御装置9がバイパス弁7
の開度を制御するものとなっている。
In the present embodiment, a bypass valve 7 is provided between the output-side and input-side pipes 4 and 3 via the branch pipes 5 and 6, and the differential pressure P'at both ends is set to the differential pressure P '. The control device 9 detects by the sensor 8 and the bypass valve 7 detects the detected output.
Is to control the opening degree of.

流量Fを流すために必要な吐出圧力PTの最低圧力(必要
最低圧力)は、システムとして定められた流量圧力特製
により定まり、流量Fの増大に従って上昇する。
The minimum pressure (required minimum pressure) of the discharge pressure P T required to flow the flow rate F is determined by the flow rate pressure specially set as the system, and increases as the flow rate F increases.

今、ポンプ11のみを最大能力で運転したときこれに応ず
る最大流量F1を流すための必要最低圧力をP1、ポンプ11
と他の1台とを最大能力で並列運転したときこれに応ず
る最大流量F2を流すための必要最低圧力をP2、・・・、
ポンプ11とポンプ12〜1nとを最大能力で並列運転したと
きこれに応ずる最大流量Fnを流すための必要最低圧力を
Pnとし、必要最低圧力P1をポンプ11のみの運転時におけ
る設定吐出圧力とし、必要最低圧力P2をポンプ11と他の
1台との並列運転時における設定吐出圧力とし、・・
・、必要最低圧力Pnをポンプ11とポンプ12〜1nとの並列
運転時における設定吐出圧力とする。
Now, P 1 the minimum required pressure for passing the maximum flow rate F1 to comply with this when operating the only pump 1 1 at full capacity, the pump 1 1
And the other one are operated in parallel at maximum capacity, the minimum pressure required to flow the maximum flow rate F2 corresponding to this is P 2 , ...,
When the pump 1 1 and the pumps 1 2 to 1 n are operated in parallel at maximum capacity, the minimum pressure required to flow the maximum flow rate Fn
And P n, the required minimum pressure P 1 and set discharge pressure during operation of only the pump 1 1, and set ejection pressure required minimum pressure P 2 at the time of parallel operation of the 1 1 and the other one pump, ...
·, And set ejection pressure required minimum pressure P n at the parallel operation of the pump 1 1 and the pump 1 2 to 1 n.

第2図にポンプ11〜1nの運転台数(又は運転機器の能
力)に応じた設定吐出圧力P1〜Pnとその時のポンプ11
下限回転数R1〜Rnとの関係を示す。すなわち、本実施例
においては、設定吐出圧力Pの上昇に応じ、ポンプ11
下限回転数Rも上昇するものとして定められ、ポンプ11
の回転数Rを制御するに当たり、この各下限値よりも回
転数Rが低下しないものとなっている。
The relationship between the second figure pump 1 1 to 1 n the number of operating units (or operating capacity of the apparatus) corresponding to the set discharge pressure of P 1 to P n and the lower limit rotation speed of the pump 1 1 at that R 1 to R n Show. That is, in this embodiment, with the increase of the set discharge pressure P, the lower limit rotational speed R of the pump 1 1 is also defined as being raised, the pump 1 1
In controlling the rotation speed R of, the rotation speed R does not decrease below the respective lower limit values.

ここで、ポンプ11が下限回転数に達した状態で、空調負
荷の軽減に応じて空調器の2方弁の開度が絞られ、給水
の流量Fが減少し、吐出圧力PTが上昇する場合について
考えてみる。
Here, in a state in which the pump 1 1 has reached the lower limit revolution speed, 2-way valve opening degree of the air conditioner in accordance with the reduction of air conditioning load is squeezed, the feed water flow rate F is reduced, the discharge pressure P T is increased Think about when you do.

この場合、差圧センサ8により検出される差圧P′に応
じ、バイパス弁7の開度が制御される。
In this case, the opening degree of the bypass valve 7 is controlled according to the differential pressure P ′ detected by the differential pressure sensor 8.

第3図は、差圧P′に応ずるバイパス弁7の開度調整特
性であり、設定吐出圧力P1〜Pnに応じて設定差圧PS1〜P
Snが定められている。すなわち、設定吐出圧力Pの上昇
に応じバイパス弁7を開き始める設定差圧PSが小さくな
るものとして定められている。そして、この設定差圧P
S1〜PSnを基準とし設定差圧PS0へ向けて、ポンプ11のみ
の運転時はl1、ポンプ12〜ln中のいずれか1台の並列運
転時はl2、全ポンプ12〜lnの並列運転時にはlnとして、
バイパス弁7の開度Dの調整特性が各個に定められてい
る。
FIG. 3 shows the opening adjustment characteristic of the bypass valve 7 depending on the differential pressure P ′, and the set differential pressures P S1 to P n according to the set discharge pressures P 1 to P n.
Sn is defined. That is, it is set that the set differential pressure P S at which the bypass valve 7 starts to open decreases as the set discharge pressure P increases. And this set differential pressure P
Toward S1 to P Sn was used as a reference set pressure differential P S0, during operation of only the pump 1 1 l 1, pump 1 2 to l parallel during operation either one of n is l 2, all pumps 1 as l n during parallel operation of 2 to l n,
The adjustment characteristic of the opening degree D of the bypass valve 7 is set individually.

したがって、本実施例によれば、並列運転台数の増加に
応じ、差圧P′の低い点からバイパス弁7の開放が開始
され、バイパス弁7による側流効果が並列運転の台数が
多い程早期に生じ、吐出圧力PTが低下して平衡するた
め、ポンプ11が下限回転数に達した状態での吐出圧力PT
の過剰な上昇が阻止され、ポンプ11からのヘッダ22への
送水の滞留が生じないものとなる。
Therefore, according to the present embodiment, the opening of the bypass valve 7 is started from the point where the differential pressure P'is low according to the increase in the number of parallel-operated machines, and the side flow effect of the bypass valve 7 is earlier as the number of parallel-operated machines is larger. to occur because the discharge pressure P T is balanced lowered, the discharge pressure P T in the state in which the pump 1 1 has reached the lower limit engine speed
Is an excessive increase of blocking, retention of water to the header 2 2 from the pump 1 1 is assumed to not occur.

なお、第2図(第3図)の特性は、状況に応じて定まる
ものであり、曲線状(直線状)のみならず直線状(曲線
状)としても設定される。
The characteristics shown in FIG. 2 (FIG. 3) are determined depending on the situation, and are set not only in a curved shape (straight line shape) but also in a straight line shape (curve shape).

また、第3図の調整特性は、制御装置9のメモリ中へ格
納しておき、プロセッサ等により運転台数を判断して所
定の特性を読み出し、差圧P′に応じてバイパス弁7を
制御するものとすればよく、第2図の制御特性および下
限値R1〜Rnも同様である。
The adjustment characteristic of FIG. 3 is stored in the memory of the control unit 9, the number of operating units is judged by a processor or the like to read out a predetermined characteristic, and the bypass valve 7 is controlled according to the differential pressure P ′. The same applies to the control characteristics and the lower limit values R 1 to R n in FIG.

ただし、可変回転数のポンプを複数台としてもよく、第
2図および第3図の特性は状況に応じて定めればよいと
共に、空調装置のみならず、同様の構成を有する各種用
途のポンプ群へ適用することができる等、種々の変形が
自在である。
However, a plurality of pumps with variable rotation speeds may be provided, and the characteristics of FIGS. 2 and 3 may be determined according to the situation, and not only the air conditioner but also a group of pumps having a similar configuration for various purposes. It can be applied to various modifications such as being applicable to.

〔発明の効果〕〔The invention's effect〕

以上説明したことから明らかなように本発明によれば、
固定回転数のポンプの並列運転台数が増加するに従って
可変回転数のポンプの回転数の下限値が上昇し、また固
定回転数のポンプの並列運転台数が増加するに従ってバ
イパス弁が開き始める差圧が小さくなり、ポンプ群から
の吐出圧力の過剰上昇分が固定回転数のポンプの並列運
転台数が多い程早期にバイパス弁によって側路されるも
のとなり、これにより可変回転数のポンプが下限値の回
転数に達した状態で吐出圧力が過剰に上昇することがな
くなり、可変回転数のポンプからの送水の滞留が生じな
いものとなり、配管や可変回転数のポンプに破損等が生
じず、可変回転数のポンプを含むポンプ群の制御におい
て顕著な効果が得られる。
As is clear from the above description, according to the present invention,
The lower limit of the rotational speed of the variable speed pump increases as the number of fixed speed pumps operating in parallel increases, and the differential pressure at which the bypass valve begins to open increases as the number of parallel operating pumps of fixed speed increases. As the number of pumps with fixed rotation speed increases in parallel, the excess increase in discharge pressure from the pump group is bypassed earlier by the bypass valve, which causes the pump with variable rotation speed to rotate at the lower limit value. The discharge pressure does not rise excessively when the number of pumps reaches the maximum number, the accumulated water is not accumulated from the variable speed pump, and the pipes and variable speed pump are not damaged. A remarkable effect can be obtained in the control of the pump group including the pumps.

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

第1図は本発明の適用された空調装置におけるポンプ群
の計装図、第2図は設定吐出圧力とポンプの下限回転数
との関係を示す図、第3図は差圧に応ずるバイパス弁の
開度調整特性を示す図、第4図は従来の空調装置におけ
るポンプ群を示す計装図である。 11……ポンプ(回転数の制御されるポンプ)、12〜1n
…ポンプ(並列運転の台数が制御されるポンプ)、21,2
2……ヘッダ、3,4……管路、5,6……分岐管路、7……
バイパス弁、8……差圧センサ、9……制御装置、R1
Rn……下限値、P1〜Pn……設定吐出圧力、PS0〜PSn……
設定差圧。
FIG. 1 is an instrumentation diagram of a pump group in an air conditioner to which the present invention is applied, FIG. 2 is a diagram showing a relationship between a set discharge pressure and a lower limit rotation speed of the pump, and FIG. 3 is a bypass valve depending on a differential pressure. FIG. 4 is a diagram showing the opening adjustment characteristic of FIG. 4, and FIG. 4 is an instrumentation diagram showing a pump group in a conventional air conditioner. 1 1 …… Pump (pump whose rotation speed is controlled), 1 2 to 1 n
… Pumps (pumps whose number is controlled in parallel), 2 1 , 2
2 …… Header, 3,4 …… Pipeline, 5,6 …… Branch line, 7 ……
Bypass valve, 8 ... Differential pressure sensor, 9 ... Control device, R 1 ~
R n …… Lower limit value, P 1 to P n …… Set discharge pressure, P S0 to P Sn ……
Set differential pressure.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】可変回転数のポンプとこの可変回転数のポ
ンプにヘッダを介して並列接続された複数台の固定回転
数のポンプとを備え、前記可変回転数のポンプの回転数
が負荷変動に応じて制御される一方、この可変回転数の
ポンプの回転数制御ではその負荷変動に対処できない場
合、前記固定回転数のポンプの運転台数が制御されるポ
ンプ群において、 このポンプ群の出力側と入力側との間へバイパス弁を設
け、 かつ、前記可変回転数のポンプの回転数に前記固定回転
数のポンプの並列運転台数の増加に従って上昇する下限
値を定め、 前記ポンプ群の出力側と入力側との差圧に応じて前記バ
イパス弁の開度を制御すると共に、 前記バイパス弁が開き始める差圧を前記固定回転数のポ
ンプの並列運転台数が増加するに従って小さくするよう
にした ことを特徴とする送水圧力制御方法。
1. A variable speed pump and a plurality of fixed speed pumps connected in parallel to the variable speed pump via a header, wherein the variable speed pump has a variable speed. On the other hand, when the load fluctuation cannot be dealt with by the rotation speed control of the variable rotation speed pump, in the pump group in which the number of operating pumps of the fixed rotation speed is controlled, the output side of this pump group is controlled. A bypass valve is provided between the pump group and the input side, and the lower limit of the number of rotations of the variable speed pump is increased as the number of parallel-operated pumps of the fixed number of rotations increases. The opening degree of the bypass valve according to the differential pressure between the input side and the input side, and the differential pressure at which the bypass valve starts to open is reduced as the number of parallel operating pumps with the fixed rotation speed increases. The water supply pressure control method characterized in that
JP2008785A 1985-02-06 1985-02-06 Water pressure control method Expired - Lifetime JPH07103871B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2008785A JPH07103871B2 (en) 1985-02-06 1985-02-06 Water pressure control method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2008785A JPH07103871B2 (en) 1985-02-06 1985-02-06 Water pressure control method

Publications (2)

Publication Number Publication Date
JPS61180315A JPS61180315A (en) 1986-08-13
JPH07103871B2 true JPH07103871B2 (en) 1995-11-08

Family

ID=12017322

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2008785A Expired - Lifetime JPH07103871B2 (en) 1985-02-06 1985-02-06 Water pressure control method

Country Status (1)

Country Link
JP (1) JPH07103871B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5299064B2 (en) * 2009-04-27 2013-09-25 アイシン精機株式会社 Waste heat recovery device and fuel cell system
JP5313848B2 (en) * 2009-11-26 2013-10-09 アズビル株式会社 Water supply pressure control system and method
CN110886693B (en) * 2018-09-10 2021-02-19 濮阳市百福瑞德石油科技有限公司 Method for preventing error operation of drilling pump in petroleum drilling engineering and pumping pressure protection system thereof

Also Published As

Publication number Publication date
JPS61180315A (en) 1986-08-13

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