JPH0411758B2 - - Google Patents
Info
- Publication number
- JPH0411758B2 JPH0411758B2 JP13808983A JP13808983A JPH0411758B2 JP H0411758 B2 JPH0411758 B2 JP H0411758B2 JP 13808983 A JP13808983 A JP 13808983A JP 13808983 A JP13808983 A JP 13808983A JP H0411758 B2 JPH0411758 B2 JP H0411758B2
- Authority
- JP
- Japan
- Prior art keywords
- hot water
- pump
- temperature
- well
- downhole 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 82
- 239000012071 phase Substances 0.000 claims description 22
- 239000007791 liquid phase Substances 0.000 claims description 15
- 229920006395 saturated elastomer Polymers 0.000 claims description 8
- 238000005086 pumping Methods 0.000 claims description 5
- 238000011017 operating method Methods 0.000 claims 1
- 239000007788 liquid Substances 0.000 description 11
- 238000010586 diagram Methods 0.000 description 5
- 230000000630 rising effect Effects 0.000 description 4
- 230000017525 heat dissipation Effects 0.000 description 2
- 238000010795 Steam Flooding Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Landscapes
- Structures Of Non-Positive Displacement Pumps (AREA)
- Control Of Non-Positive-Displacement Pumps (AREA)
- Reciprocating Pumps (AREA)
Description
【発明の詳細な説明】
「産業上の利用分野」
本発明は地下熱水汲み上げ用のダウンホールポ
ンプの初期運転に関する。DETAILED DESCRIPTION OF THE INVENTION "Field of Industrial Application" The present invention relates to the initial operation of a downhole pump for pumping underground hot water.
「従来の技術と発明が解決しようとする課題」
密閉した熱水井戸の定常運転状態においては熱
水井戸内の液相部の温度は総て湧出する熱水の温
度となつており、一様であり、気相部は上下方向
に長大なため、周囲の岩盤へ放熱し、液相部より
も平均温度がわずかに低い値となつている。"Problems to be solved by the conventional technology and the invention" In the steady operation of a closed hot water well, the temperature of the liquid phase inside the well is the same as the temperature of the gushing hot water, and is uniform. Since the gas phase is long in the vertical direction, heat is radiated to the surrounding rock, and the average temperature is slightly lower than that of the liquid phase.
長期間停止された熱水井戸においては、大気や
岩盤への熱放散のため坑底温度に比べ上層部に行
くに従つて低温になる。第1図はポンプの停止時
の密閉した熱水井戸の温度分布を示す線図であつ
て垂直な座標Y−Yから水平方向にその位置の温
度をとり、温度分布線1を示すもので図のOが地
上である。熱水井戸2中の液相部3中にダウンホ
ールポンプ(以下単にポンプと称す)4が設置さ
れ、ポンプ4に連結した吐出管5により地上へ送
液される。 In hot water wells that have been shut down for long periods of time, the temperature at the top becomes lower than the bottom temperature due to heat dissipation into the atmosphere and bedrock. Figure 1 is a diagram showing the temperature distribution of a closed hot water well when the pump is stopped.The temperature at that position is taken in the horizontal direction from the vertical coordinate Y-Y, and the diagram shows temperature distribution line 1. O is on the ground. A downhole pump (hereinafter simply referred to as a pump) 4 is installed in the liquid phase portion 3 of the hot water well 2, and the liquid is sent to the ground through a discharge pipe 5 connected to the pump 4.
例えば図に示すごとく坑底7では熱水は200℃
になつているが上層部に行くに従つて温度が下
り、気相部6では飽和蒸気状態のため温度はどこ
でも一定で100℃になる様な場合もある。この様
な場合上記温度の違いを考慮せずポンプ4を運転
すると坑底7の200℃の熱水が急激に上昇するた
めポンプ4に吸込まれる熱水の温度は急激に上昇
する。この熱水の温度上昇は数分間と短かい。ポ
ンプ4の運転が続行されるためにはキヤビテーシ
ヨンを無視して考えると、ポンプ4の吸込口を取
囲む液体の圧力はポンプ4が吸込む熱水の温度に
相当した飽和蒸気圧以上の圧力が必要である。処
が気相部6の飽和蒸気圧とポンプ4よりも上部の
液相部3のヘツドに相当する圧力の和が前記のポ
ンプ4が吸込む熱水の温度以上の飽和蒸気圧より
大でなければならないが気相部6や液上層は吐出
管5をとおる熱水により加熱されるものの、温度
上昇はおくれ低温のままのため十分なポンプ吸込
圧力が確保できない。この様なことからポンプが
運転不能になる場合がある。如何なる熱水量でポ
ンプ4を運転すれば如何なる温度変化が生じるか
は、その井戸固有の問題があり、井戸の直径、液
相部3の深さ、熱水の温度、ポンプ4の設置深
さ、ポンプ4上部の液相部深さ、吐水管5の直
径、長さ等があり、井1の湧水量、地上の熱交換
負荷等を考慮して予測するが予測困難である。従
つて、運転不能となつた場合に予かじめ備える必
要がある。 For example, as shown in the figure, the hot water at bottom 7 is 200℃.
However, the temperature decreases as you go to the upper layer, and in the gas phase 6, the temperature is constant everywhere and may reach 100°C because it is in a saturated vapor state. In such a case, if the pump 4 is operated without considering the above-mentioned temperature difference, the temperature of the hot water sucked into the pump 4 will rise rapidly because the 200° C. hot water at the bottom of the well 7 will rise rapidly. The temperature rise of this hot water is short, lasting only a few minutes. In order for the pump 4 to continue operating, ignoring cavitation, the pressure of the liquid surrounding the suction port of the pump 4 must be higher than the saturated vapor pressure corresponding to the temperature of the hot water sucked into the pump 4. It is. However, unless the sum of the saturated vapor pressure of the gas phase section 6 and the pressure corresponding to the head of the liquid phase section 3 above the pump 4 is greater than the saturated vapor pressure above the temperature of the hot water sucked by the pump 4, However, although the gas phase portion 6 and the upper liquid layer are heated by the hot water passing through the discharge pipe 5, the temperature rises slowly and remains at a low temperature, making it impossible to ensure sufficient pump suction pressure. Due to this, the pump may become inoperable. What kind of temperature change will occur if the pump 4 is operated with what amount of hot water depends on the problems specific to the well, and includes the diameter of the well, the depth of the liquid phase part 3, the temperature of the hot water, the installation depth of the pump 4, The depth of the liquid phase in the upper part of the pump 4, the diameter and length of the water discharge pipe 5, etc. are involved, and it is difficult to predict, although it takes into consideration the amount of spring water in the well 1, the heat exchange load on the ground, etc. Therefore, it is necessary to prepare in advance in case the vehicle becomes inoperable.
本発明は熱水井戸に設置されたダウンホールポ
ンプ始動時においてポンプ吸込圧力を確保して該
ポンプの始動を円滑にする運転手段を提供するこ
とを目的とする。 SUMMARY OF THE INVENTION An object of the present invention is to provide an operating means that ensures pump suction pressure at the time of starting a downhole pump installed in a hot water well to ensure smooth startup of the pump.
「課題を解決するための手段」
本発明の第1の発明は地下熱水を汲上げるダウ
ンホールポンプの初期運転において、地下装置へ
吐出される熱水量を少なくして地下熱水の湧き上
がる速度を遅くすると同時にダウンホールポンプ
の吐出された熱水の一部を地上もしくは地上近傍
にて取り出しもしくは他の熱水源から導いて井戸
に入れることによりダウンホールポンプに吸込ま
れる熱水の温度変化を小さくし、ダウンホールポ
ンプに吸込まれる熱水の温度に相当する飽和蒸気
圧よりも気相部の温度に相当する飽和蒸気圧とポ
ンプより上層の液相部ヘツドに相当する圧力の和
が大となるように維持して十分なポンプ吸込圧力
を確保しダウンホールポンプを安全に運転する地
下熱水汲上げ用ダウンホールポンプの初期運転方
法である。``Means for Solving the Problems'' The first aspect of the present invention is to reduce the amount of hot water discharged to underground equipment during the initial operation of a downhole pump that pumps up underground hot water, thereby increasing the speed at which hot water rises underground. At the same time, some of the hot water discharged from the downhole pump is taken out at or near the ground or guided from another hot water source and introduced into the well, thereby reducing the temperature change of the hot water sucked into the downhole pump. The sum of the saturated vapor pressure corresponding to the temperature of the gas phase and the pressure corresponding to the head of the liquid phase above the pump is greater than the saturated vapor pressure corresponding to the temperature of the hot water sucked into the downhole pump. This is an initial operation method for a downhole pump for pumping up underground hot water, which maintains sufficient pump suction pressure to operate the downhole pump safely.
本発明の第2の発明は井戸から地下熱水を汲み
上げるダウンホールポンプの吐出管から井戸の気
相部に流量調整手段を介して連通させた初期運転
用のバイパス配管を設けると共にポンプ吐出量を
可変とする手段を備えてなる地下熱水汲み上げ用
ダウンホールポンプの初期運転装置である。 The second aspect of the present invention is to provide a bypass pipe for initial operation that communicates from the discharge pipe of a downhole pump that pumps up underground hot water from a well to the gas phase part of the well via a flow rate adjustment means, and to adjust the pump discharge amount. This is an initial operating device for a downhole pump for pumping up underground hot water, which is equipped with variable means.
「実施例」
以下、図面に従つて本発明の実施例について説
明する。第2図は熱水井戸の縦断面を示すと共に
併せて熱水井戸の温度分布を示す線図を表示して
あり、温度分布を示す線図は第1図と同じ手法で
示されており、Y−Yが垂直方向の座標で原点0
は地上を示す。"Embodiments" Examples of the present invention will be described below with reference to the drawings. Figure 2 shows a longitudinal section of a hot water well and also shows a diagram showing the temperature distribution of the hot water well, and the diagram showing the temperature distribution is shown in the same manner as in Figure 1. Y-Y is the vertical coordinate and the origin is 0
indicates the ground.
ポンプ4の吐出管5は地上にて井戸2の蓋8を
密封挿通している。そして地上施設側へは流量調
整も可能な仕切弁9を介して連結されている。 The discharge pipe 5 of the pump 4 is hermetically inserted through the cover 8 of the well 2 above ground. It is connected to the ground facility side via a gate valve 9 that can also adjust the flow rate.
地上施設側は熱水井戸(以下井戸と称す)2か
ら供給された熱水を熱交換器に導いて熱媒体を過
熱蒸気として過熱蒸気により蒸気タービンを駆動
して蒸気タービンにより発電機を駆動するもの
で、熱交換器を出た一次側の熱水は還元井へ送り
込まれるものである。 On the ground facility side, hot water supplied from a hot water well (hereinafter referred to as well) 2 is guided to a heat exchanger, the heat medium is used as superheated steam, the superheated steam drives a steam turbine, and the steam turbine drives a generator. The primary hot water that exits the heat exchanger is sent to the reinjection well.
吐出管5の仕切弁9の上流側と井戸2の気相部
6との間を連通する初期運転用バイパス配管11
が設けてあり、バイパス配管11にはバイパス配
管11内の液体の温度を計る温度計12、始動し
て運転初期に開く仕切弁14、バイパス配管11
を流れる液体の流量を調整する流量調整弁13が
介在している。尚、バイパス配管11は他の熱源
例えば他の熱水井戸から井戸2内に連通するよう
にしてもよい。 Bypass piping 11 for initial operation that communicates between the upstream side of the gate valve 9 of the discharge pipe 5 and the gas phase part 6 of the well 2
The bypass piping 11 is equipped with a thermometer 12 that measures the temperature of the liquid in the bypass piping 11, a gate valve 14 that opens at the beginning of operation after startup, and a bypass piping 11.
A flow rate adjustment valve 13 is interposed to adjust the flow rate of liquid flowing through the tube. Note that the bypass pipe 11 may communicate with the well 2 from another heat source, for example, another hot water well.
始動時仕切弁14は開放され仕切弁9は絞られ
る。そしてポンプ4が付勢されると吐出管5を通
じて地上施設へ熱水を送るバイパス配管11を通
じて井戸2の気相部6へ一部戻される。 At startup, the gate valve 14 is opened and the gate valve 9 is throttled. Then, when the pump 4 is energized, a portion of the hot water is returned to the gas phase section 6 of the well 2 through the bypass pipe 11 that sends the hot water to the above-ground facility through the discharge pipe 5.
ポンプ4から吐出された熱水の内地上装置側へ
吐出される熱水量をQとし、初期運転用バイパス
配管11から井戸2内へ戻される熱水量をqとす
る。この場合ポンプ4より吐出される流量はQ+
qであり坑底7から上昇する熱水量Q′は地上装
置側へ吐出される熱水量Qに等しいとして扱つて
よい。即ち、井戸は数千メートル〜数百メートル
の深さがあり、液相部3の液面変動はポンプ4の
全揚程に比して小さいからである。 Let Q be the amount of hot water discharged from the pump 4 to the inland equipment side, and let q be the amount of hot water returned from the bypass piping 11 for initial operation into the well 2. In this case, the flow rate discharged from pump 4 is Q+
q, and the amount of hot water Q' rising from the bottom 7 may be treated as equal to the amount of hot water Q discharged to the ground equipment side. That is, the well has a depth of several thousand meters to several hundred meters, and the liquid level fluctuation in the liquid phase portion 3 is small compared to the total head of the pump 4.
ポンプ4の運転初期においては仕切弁9で地上
装置側へ吐出される熱水量Qを絞り、Q′を小さ
くすることにより、坑底7からの熱水の上昇を緩
やかにする。このことにより運転初期にポンプ4
内に吸込まれる熱水量は定常運転時におけるポン
プ4の吐出量よりも小さく、吸込む熱水の温度の
上昇は緩やかである。 At the beginning of the operation of the pump 4, the amount of hot water Q discharged to the ground equipment side is throttled by the gate valve 9, and by reducing Q', the rise of the hot water from the bottom 7 is made gradual. As a result, pump 4
The amount of hot water sucked into the pump 4 is smaller than the discharge amount of the pump 4 during steady operation, and the temperature of the hot water sucked in increases slowly.
またこの時に前記の初期運転用バイパス配管1
1から吐出された熱水の一部qを井戸2へ戻す。
この際qを出来るだけ大きくすることによりポン
プ4より上の井戸内温度を均一に近い状態にする
ことができる。このようにするとポンプ4の起動
直後はポンプ4に吸込まれる熱水の温度と気相部
6の温度差は小さく、わずかにポンプ4の吸込む
熱水温度の方が高い場合は大量に井戸1へ戻す。
即ち、Qをきわめて小としてもよい。これによつ
て気相部6と液相部3の上部はポンプ4における
吸込液体の温度との温度差が小さい状態を保ち乍
ら共に温度上昇する。 Also, at this time, the above-mentioned bypass piping 1 for initial operation
A portion q of the hot water discharged from 1 is returned to well 2.
At this time, by making q as large as possible, the temperature in the well above the pump 4 can be made nearly uniform. In this way, immediately after the pump 4 is started, the difference in temperature between the temperature of the hot water sucked into the pump 4 and the gas phase part 6 is small, and if the temperature of the hot water sucked into the pump 4 is slightly higher than the temperature of the hot water sucked into the well 1 Return to.
That is, Q may be made extremely small. As a result, the temperatures of the upper portions of the gas phase portion 6 and the liquid phase portion 3 both rise while the temperature difference between the temperature of the liquid sucked into the pump 4 remains small.
従つてQ′(=Q)を小さくしqを大きくするこ
とによつて抗底7から上昇してくる熱水による温
度変化を緩やかにし、かつポンプ4近傍およびそ
れより上層部の温度を均一に近い状態にし十分な
ポンプ4の吸込圧力を確保し、ポンプ4を安全に
運動することができる。 Therefore, by reducing Q' (=Q) and increasing q, the temperature change caused by the hot water rising from the bottom of the shaft 7 can be made gradual, and the temperature near the pump 4 and above it can be made uniform. It is possible to maintain sufficient suction pressure of the pump 4 in a similar state and safely operate the pump 4.
さてかかるポンプ4の初期運転によるポンプ4
の吸込口入口の温度tpを求めてみる。ポンプ4を
始動してある時間運転すると地底7からポンプ4
までの井戸2内の熱水は上昇し、抗底7にあつた
熱水は位置15まで上昇して抗底7から位置15
までは一定温度T゜となり、位置15を基準に第
1図の温度分布線1を重ねたようになよたポンプ
4の位置では上昇した熱水の温度はTとなる。一
方バイパス配管11から気相部6に戻される熱水
の一部の流量はqであり、符号17の線で示すよ
うに気相部6において気相部6の飽和温度t′(気
相部6中では一定)まで降下して液相部3の液面
に到る。そして液面16で液化して次第に温度
t′からtに下りポンプ4に吸込まれる。吸込液体
は抗底7側から上昇する熱水と気相部6を通じて
戻される熱水の混合されるものであるから、ポン
プ4の吸込口入口の温度tpは
tp=QT+qt/Q+q
となる。T、t、tpは時間と共に大きくなるがポ
ンプ4の始動時は仕切弁9を絞るかポンプが可変
吐出量の形式のポンプの場合はポンプ4の吐出量
を少なくして地上施設への送液量Qを小さくし戻
し量qを大きくすることによつてTの変化を小さ
くT、t、tpの温度差を小さくする。かくして気
相部6の圧力は高められポンプ4の吸込圧を確保
できる。ポンプ4で吸込まれた熱水は符号18の
点線で示すように吐出管5内で次第にやや気相部
6の気体により熱を奪われて地上で温度t′となる
と均衡されるがポンプ4よりも上部に液相部3が
あり、そのヘツドにより、ポンプ4の吸込は続行
される。処がポンプ4の吸込みが続行すると液相
部3は上昇し、温度Tは上昇し、温度t、tp、T
は共に高くなつて行き接近して行くので、地上に
吐出される熱水の温度は気相部6の温度より、わ
ずかに大きく、気相部6は戻した熱水と吐出管5
をおそくされた速度で上昇する熱水の放熱によ
り、ポンプ4の吸込む熱水の温度との差が大とな
らない状態でゆるやかに昇温する。かくして、こ
の作動を続行すると気相部6、液相部3は一様な
温度T゜となるものである。 Now, the pump 4 according to the initial operation of the pump 4
Let's find the temperature tp at the inlet of the suction port. When pump 4 is started and operated for a certain period of time, pump 4 will be pumped from underground 7.
The hot water in well 2 rises up to the bottom, and the hot water in well 7 rises to position 15, and the hot water in well 2 rises to position 15 from bottom well 7.
Until then, the temperature is constant T°, and the temperature of the increased hot water becomes T at the position of the pump 4 where the temperature distribution line 1 in FIG. 1 is overlapped with the position 15 as a reference. On the other hand, the flow rate of a part of the hot water returned from the bypass pipe 11 to the gas phase section 6 is q, and as shown by the line 17, the saturation temperature t' of the gas phase section 6 (gas phase section 6) and reaches the liquid level in the liquid phase section 3. Then, it liquefies at the liquid level 16 and the temperature gradually increases.
From t' to t, it is sucked into the pump 4. Since the suction liquid is a mixture of hot water rising from the bottom 7 side and hot water returning through the gas phase section 6, the temperature tp at the inlet of the suction port of the pump 4 is tp=QT+qt/Q+q. T, t, and tp increase with time, but when starting the pump 4, either throttle the gate valve 9 or, if the pump is a variable discharge type pump, reduce the discharge volume of the pump 4 to send liquid to the ground facility. By reducing the amount Q and increasing the return amount q, the change in T is reduced and the temperature difference between T, t, and tp is reduced. In this way, the pressure in the gas phase section 6 is increased, and the suction pressure of the pump 4 can be ensured. As shown by the dotted line 18, the hot water sucked in by the pump 4 gradually loses heat in the discharge pipe 5 by the gas in the gas phase 6, and when it reaches the temperature t' on the ground, it is balanced. There is also a liquid phase section 3 at the top, and the suction of the pump 4 is continued by its head. However, as the suction of the pump 4 continues, the liquid phase portion 3 rises, the temperature T rises, and the temperatures t, tp, T
As both become higher and closer together, the temperature of the hot water discharged to the ground is slightly higher than the temperature of the gas phase part 6, and the gas phase part 6 collects the returned hot water and the discharge pipe 5.
Due to the heat dissipation of the hot water, which rises at a slow rate, the temperature of the hot water is gradually raised without becoming large in temperature difference from the temperature of the hot water sucked by the pump 4. Thus, if this operation is continued, the gas phase portion 6 and liquid phase portion 3 will have a uniform temperature T°.
本発明は井戸内温度の不均一な運転初期状態に
おいてダウンホールポンプの運転について吐出管
から井戸中へ吐出熱水の一部を流量調整して戻す
ようにバイパス配管もしくは他の熱水源から井戸
中へ熱水を導く配管を備え運転初期においては地
上装置側へ送る熱水量を絞り、坑底から上昇して
くる熱水による温度変化を緩やかにし、かつ、地
上吐出部に設けられた初期運転用バイパス配管か
ら井戸内へ吐出された熱水を戻すか他の熱水源か
ら井戸中へ熱水を送り込むようにしたから、ポン
プに吸込まれる熱水の温度変化を小さくすると同
時に十分なポンプ吸込圧力を確保し、ポンプを安
全に初期運転するることを可能にした。
The present invention is designed to adjust the flow rate and return a portion of the hot water discharged from the discharge pipe into the well from a bypass pipe or other hot water source into the well during operation of a downhole pump in an initial operation state where the temperature inside the well is uneven. In the early stages of operation, the amount of hot water sent to the ground equipment is reduced, and temperature changes due to hot water rising from the bottom of the well are moderated. By returning the hot water discharged into the well from the bypass piping or sending hot water into the well from another hot water source, the temperature change of the hot water sucked into the pump is minimized, and at the same time sufficient pump suction pressure is maintained. This enabled safe initial operation of the pump.
従つて本発明により、井戸内温度差の大きい停
止状態から定常状態(井戸内温度が一定の状態)
に至るまでポンプを安全に運転することが出来
る。 Therefore, according to the present invention, it is possible to change from a stopped state with a large temperature difference in the well to a steady state (state where the temperature in the well is constant).
The pump can be operated safely up to
第1図は井戸のポンプ停止時における温度分布
を示す線図、第2図は本発明の実施例の縦断面図
である。
1……温度分布線、2……熱水井戸、3……液
相部、4……ポンプ、5……吐出管、6……気相
部、7……坑底、8……蓋、9……仕切弁、11
……初期運転用バイパス配管、12……温度計、
13……流量調整弁、14……仕切弁、15……
位置。
FIG. 1 is a diagram showing the temperature distribution when the well pump is stopped, and FIG. 2 is a longitudinal sectional view of an embodiment of the present invention. 1...Temperature distribution line, 2...Hot water well, 3...Liquid phase section, 4...Pump, 5...Discharge pipe, 6...Gas phase section, 7...Bottom hole, 8...Lid, 9...Gate valve, 11
...Bypass piping for initial operation, 12...Thermometer,
13...Flow rate adjustment valve, 14...Gate valve, 15...
position.
Claims (1)
期運転において、地上装置へ吐出される熱水量を
少なくして地下熱水の湧き上がる速度を遅くする
と同時にダウンホールポンプの吐出された熱水の
一部を地上もしくは地上近傍にて取り出しもしく
は他の熱水源から導いて井戸に入れることにより
ダウンホールポンプに吸込まれる熱水の温度変化
を小さくし、ダウンホールポンプに吸込まれる熱
水の温度に相当する飽和蒸気圧よりも気相部の温
度に相当する飽和蒸気圧とポンプより上層の液相
部ヘツドに相当する圧力の和が大となるように維
持して十分なポンプ吸込圧力を確保しダウンホー
ルポンプを安全に運転する地下熱水汲上げ用ダウ
ンホールポンプの初期運転方法。 2 井戸から地下熱水を汲み上げるダウンホール
ポンプの吐出管から井戸の気相部に流量調整手段
を介して連通させた初期運転用のバイパス配管を
設けると共にポンプ吐出量を可変とする手段を備
えてなる地下熱水汲上げ用ダウンホールポンプの
初期運転装置。[Scope of Claims] 1. In the initial operation of a downhole pump that pumps up underground hot water, the amount of hot water discharged to above-ground equipment is reduced to slow down the speed at which underground hot water rises, and at the same time the downhole pump is discharged. By extracting some of the hot water above ground or near the ground, or guiding it from another hot water source and introducing it into the well, the temperature change of the hot water sucked into the downhole pump is reduced, and the temperature change of the hot water sucked into the downhole pump is reduced. A pump that is sufficient to maintain the sum of the saturated vapor pressure corresponding to the temperature of the gas phase and the pressure corresponding to the head of the liquid phase above the pump is greater than the saturated vapor pressure corresponding to the temperature of the hot water. An initial operating method for a downhole pump for pumping up underground hot water to secure suction pressure and operate the downhole pump safely. 2. Provide bypass piping for initial operation that communicates from the discharge pipe of the downhole pump that pumps underground hot water from the well to the gas phase part of the well via a flow rate adjustment means, and also includes means for making the pump discharge rate variable. Initial operation equipment for a downhole pump for pumping up underground hot water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13808983A JPS6030497A (en) | 1983-07-28 | 1983-07-28 | Method and device for initial operation of downhole pump for pumping up underground hot water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13808983A JPS6030497A (en) | 1983-07-28 | 1983-07-28 | Method and device for initial operation of downhole pump for pumping up underground hot water |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6030497A JPS6030497A (en) | 1985-02-16 |
| JPH0411758B2 true JPH0411758B2 (en) | 1992-03-02 |
Family
ID=15213693
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13808983A Granted JPS6030497A (en) | 1983-07-28 | 1983-07-28 | Method and device for initial operation of downhole pump for pumping up underground hot water |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6030497A (en) |
-
1983
- 1983-07-28 JP JP13808983A patent/JPS6030497A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6030497A (en) | 1985-02-16 |
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