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EP 3 271 546 B1 |
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EUROPEAN PATENT SPECIFICATION |
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Mention of the grant of the patent: |
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05.06.2019 Bulletin 2019/23 |
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Date of filing: 16.03.2015 |
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International Patent Classification (IPC):
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International application number: |
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PCT/IB2015/051920 |
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International publication number: |
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WO 2016/147029 (22.09.2016 Gazette 2016/38) |
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METHOD FOR CONDUCTING ON-GOING ANALYSIS OF THE CURRENT TECHNICAL CONDITION OF A SUBMERSIBLE
PUMP SYSTEM AND A PROBE USED FOR EMPLOYING THIS METHOD
VERFAHREN ZUR DURCHFÜHRUNG EINER LAUFENDEN ANALYSE DES AKTUELLEN TECHNISCHEN ZUSTANDS
EINES TAUCHPUMPENSYSTEMS UND EINE ZUM EINSATZ DES VERFAHREN VERWENDETE SONDE
PROCÉDÉ POUR EFFECTUER UNE ANALYSE CONTINUE DE L'ÉTAT TECHNIQUE ACTUEL D'UN SYSTÈME
DE POMPE SUBMERSIBLE ET SONDE UTILISÉE POUR EMPLOYER CE PROCÉDÉ
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Designated Contracting States: |
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AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL
NO PL PT RO RS SE SI SK SM TR |
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Date of publication of application: |
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24.01.2018 Bulletin 2018/04 |
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Proprietors: |
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- Aplisens S.A.
03-192 Warszawa (PL)
- Mast Dr Straczynski, Marian
97-0400 Belchatów (PL)
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Inventor: |
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- MAST Dr Straczynski, Marian
97-0400 Belchatów (PL)
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Representative: Adamczyk, Piotr |
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Kancelaria Patentowa Piotr Adamczyk
Ul. Wilcza 70/8 00-670 Warszawa 00-670 Warszawa (PL) |
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References cited: :
WO-A2-98/05848 US-A1- 2015 052 989
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US-A- 5 634 522
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| Note: Within nine months from the publication of the mention of the grant of the European
patent, any person may give notice to the European Patent Office of opposition to
the European patent
granted. Notice of opposition shall be filed in a written reasoned statement. It shall
not be deemed to
have been filed until the opposition fee has been paid. (Art. 99(1) European Patent
Convention).
|
Technical Field
[0001] The invention relates to method for conducting on-going analysis of the current technical
condition of a submersible pump system installed in a deep well and to a probe to
survey of the current technical condition of such system.
Background Art
[0002] The basic operating parameters of any submersible pump include its capacity (Q),
which is the volume of liquid pumped out within a specific time unit, and lift (H),
which is the pressure of pumped liquid provided in metres water column. The relationship
between a pump's lift and its capacity is defined by the well-known pump flow characteristic
H=f(Q). The submersible pump operating parameters (Q,H) facilitate determination of
other parameters, such as efficiency and power consumption of the pump. The existing
method for conducting on-going analysis of the current technical condition of a submersible
pump system with known capacity value (Q) involves approximate determination of pump
lift (H
R) by adding the water surface height in the well to the pressure value measured upstream
of the damper gate in a horizontal run of the pipeline which terminates the pump system.
Such a system can be found for example in
US 2015/052989. Since it is impossible to determine the linear flow loss in a vertical pressure
line of a submersible pump, its estimate value is sometimes added, and in each such
instance the actual pump lift of the pump system was estimated. The lack of a known
actual lift of a submersible pump (H
R), operated in a pump set with a known capacity value (Q), precluded determination
of actual distortions to the actual characteristic H
R=f(Q) during operation of the pump against the reference H=f(Q), determined on a test
stand. This prevents exact diagnosis of the technical condition of a submersible pump
system and of the actual pump. The reference characteristics H=f(Q) determined on
a test stand is evaluated by reference to the pump technical data sheet according
to the approved standards, e.g. PN-EN ISO 9906:2012. Before installing the pump into
the pumping system, the submersible pump is fully diagnosed, as well as it is in good
technical condition and it is energy-efficient.
Disclosure of Invention
[0003] The purpose of the invention was to develop a method for conducting on-going analysis
of the current technical condition of an assembled (integrated) and commissioned submersible
pump system.
The purpose meets a method by which, for a given capacity of the pump system measured
at its downstream end, differential pressure is determined between the liquid pressure
in the pipeline near the pump pressure port and the hydrostatic pressure of the same
liquid outside of the pump and near the pump pressure port. The differential pressure
determined in this way is compared against the lift, which results from the known
lift as a function of capacity, for the capacity value being the given capacity of
the pump system for which the differential pressure has been determined.
In one of variants of the method according to the invention, comparison of the determined
differential pressure to lift involves calculating the ratio of that differential
pressure to that lift.
Another variant of the method according to the invention involves determining the
differential pressure for pressure values measured at a distance to the pump pressure
port equal or less than 0.15% of the pump installation depth but also equal or less
than 4 meters.
Another variant of the method according to the invention involves determining the
differential pressure by measuring the liquid pressure in the pipeline and the liquid
hydrostatic pressure outside of the pump in two separate measurements in which two
separate liquid electrical pressure transducers are applied and then determining the
difference between the two obtained electric signals.
[0004] In another variant of the method according to the invention the pressure transducers
feature piezo-resistive silicon sensors, isolated from the liquid being measured by
a separating membrane enclosing a manometer liquid. Another variant of the method
according to the invention involves measuring the liquid pressure in the pipeline
by connecting a pressure transducer to a port located in an intermediate ring installed
in line of the pipeline, advantageously between the pump pressure port and the pipeline
start section.
Yet another variant of the method according to the invention involves determining
the liquid differential pressure with a measurement probe which houses both of the
said pressure transducers connected with each other by one common body. The common
body is installed on the pipeline and the pressure transducer of the liquid hydrostatic
pressure outside of the pump is oriented perpendicularly to flow direction in the
pipeline.
[0005] A probe according to the invention consists of two liquid electrical pressure transducers.
One of the pressure transducers measures the pressure of liquid forced by the pump
into the pipeline connected to the pump pressure port. The other pressure transducer
measures hydrostatic pressure of the liquid in which the pump is immersed. Each of
the two pressure transducers is housed in a separate body which features a metering
orifice on one end. The pressure transducer bodies are installed substantially in
perpendicular against each other in a common coupling body.
In one of variants of the probe according to the invention both pressure transducers
feature piezo-resistive silicon sensors isolated from the measured liquid with a separating
membrane and a manometer liquid.
In another variant of the probe according to the invention, the probe also features
an intermediate ring designed to be fastened between the pump pressure port and the
starting section of the pipeline. The intermediate ring features a port connected
by a line with the metering orifice of the pump-forced liquid pressure transducer
In yet another variant of the probe according to the invention, the probe also features
a fixture for fastening the probe to the pipeline.
[0006] The advantage of the invention is that it facilitates conducting on-going analysis
of the current technical condition of a submersible pump system, i.e. the actual submersible
pump, its pressure pipeline, and its fittings. This fact considerably improves the
quality of operation of submersible pumps and submersible pump systems. Only if damage
to a pump operating in a deeply submerged assembly is detected soon enough, is it
possible to predict and prevent problems which are always expensive to fix. According
to the invention, the technical condition diagnosis allows the pump user to remove
the damaged submersible pump immediately or stop leaks in the pressure pipeline. As
a result, significant savings in electrical power consumption are made. The invention
effectively optimises the use of submersible pump systems.
Brief Description of Drawings
[0007] Embodiment exemplifying the invention is described below and presented on the drawings.
Fig. 1 shows schematically cross-section of a deep well with installed submersible
pump and the probe according to the invention. Fig. 2 shows a magnification of vertical
cross-section of the pipeline starting section which is provided with the probe according
to the invention, and admits water from the pump. Fig. 3 shows a partial cross-section
of a part of the first pressure transducer (the pipeline liquid pressure transducer)
being a component of the probe according to the invention. Fig. 4 shows, in the same
cross-section as provided in Fig. 3, a part of the second pressure transducer which
is a component of the probe and measures hydrostatic pressure. Fig. 5 shows a diagram
presenting the lift vs. capacity of the pump, which is implemented in the invention
embodiment.
Mode for Carrying out Invention
[0008] The submersible pump (1) type GCA.6.12 manufactured by HYDRO VACUUM S.A., with nominal
capacity of 1.42 m
3/min and nominal lift of 219 meters was installed on a known test stand. Further,
lift H was determined as a function of capacity Q, as shown in the diagram on Fig.
5. Next, the pump 1 was placed in a deep well 2 bored in an aquifer. The deep well
2 depth Ls was 250 meters and the deep well diameter was 16" (ca. 406 mm). The structural
design of the deep well in question 2 resembled the well-known design of S5 submersibles
and it included, among others, the filter 3. The pump 1 was installed in the deep
well 2 at the depth Lp of 223 m. The pump 1 pressure port 4 was connected to the pipeline
5 with a diameter of 150 mm, featuring a throttle valve 6 installed on the pipeline
surface and two pressure gauges 7 and 8 located on both sides of the throttle valve
6. The end of the pipeline 5 was located over a surface reservoir 9 into which the
water from the deep well 2 was pumped. The water surface 10 in static conditions (10'),
i.e. with non-operating submersible pump 1 was at the depth Lw' of 167 m. When the
pump 1 was operating, the water surface depth was reduced (10") to Lw" of 199 m.
[0009] The measurement probe enabling the invention to be embodied was made of two measurement
probes manufactured by APLISENS S.A. Smart depth probe type SG-25 Smart was used as
hydrostatic pressure transducer 11. The probe had two metering orifices 12 made in
the head 13, which closed the probe body 14 on one end. PC28 pressure transducer was
used as the pressure transducer 15 for water forced by the pump 1 into the pipeline
5. The body 16 of the said pressure transducer 15 had a threaded head 17 with a metering
orifice 18. Both pressure transducers 11 and 15 featured piezo-resistive silicon sensors
19 isolated from the measured liquid by a separating membrane 20 and a manometer liquid
21. The above-mentioned transducers 11 and 15 featured also digital electronic circuits
(not shown) working with the sensors 18. The body 14 and 16 ends of the pressure transducers
11 and 15 were installed inside a common body 22 with a watertight seal. The common
body 22 features known fixing assemblies 23 which facilitated fastening of the probe
(11,15,22) to the pipeline 5 at the depth Hs of 228 m. A cable 24 was fed out of the
common body 22 in order to transmit electrical outputs from the transducers 19 to
a measurement instrument assembly 25. Between the pump 1 pressure port 4 and the pipeline
5 start section 5' there was an intermediate ring 26 installed with a port 27 on the
side, which allows a user to use a tube 28 to connect the pipeline 5 interior to the
metering orifice 18 of the pressure transducer 15. A water meter (not shown in the
drawing) was also installed in line of the pipeline 5 in order to measure the actual
water output from the pump 1. The water meter enabled the actual output of the pump
1 to be recorded at 1.36 m
3/min. During the use of the pump 1 the pressure transducer 15 recorded pipeline internal
pressure of 256 m H
2O. At the same time, the pressure transducer 11 recorded hydrostatic pressure of 29
m H
2O inside the well 2. The measurement instrument assembly 25 recorded the differential
pressure of 227 m H
2O, which corresponded to the actual ongoing lift HR of the pump system. With the Q
R capacity of 1.36 m
3/m as established on the test stand, the pump 1 achieved the lift H of 228 m (Fig.
5), i.e. only 1 metre above the reference value. This results in drawing the conclusion
that the pump 1 is in good technical condition and the entire pump system is leak-free.
Due to determining, according to the above-mentioned procedure, the actual lift HR
for a submersible pump in a pump system it is possible to accurately track the current
changes (run distortions) of the pump characteristics at any measured capacity Q.
It is also possible to evaluate the optimum energy efficiency of the pump system.
If we know the actual water pressure in the pipeline 5 upstream and downstream of
the throttle valve 6 which is read e.g. from the pressure gauges 7 and 8, and if we
know the actual lift as determined by the method according to the invention, it is
possible to precisely evaluate pressure loss across the entire pipeline. The determination
of actual lift with the electrical outputs from the pressure transducers 11 and 15
can be easily automated with any computer. This will greatly simplify remote monitoring
of the submersible pump performance. One of ways of defining the technical condition
of a pump system is calculating the ratio of a determined differential pressure to
pump lift read from the pump characteristics and provided in percentage. This facilitates
easy visualisation of the technical condition, with 100% being a brand-new pump system.
[0010] According to the invention, the internal pressure in the pipeline 5 can be measured
with the probe also at the pump pressure port 4, provided that the pressure port 4
is provided with a suitable metering orifice similar to the aforementioned orifice
27 of the intermediate ring 26, or at the pipeline 5 start section, provided that
the pumped liquid can access the pressure transducer 15 in a similar way. It is essential
to take measurement within the following distance from the pump pressure port: equal
to or less than 0.15% of the pump installation depth and also equal to or less than
4 meters.
1. A method for conducting on-going analysis of the current technical condition of a
submersible pump system consisting of a submersible pump with a known lift as a function
of capacity determined on a test stand, with the submersible pump immersed in a liquid
contained in a deep well, and of a pressure pipeline complete with fittings to discharge
the pumped liquid and connected to the pressure port of the same submersible pump,
characterised in that for a given pump system capacity measured at its discharge end, a differential pressure
is determined between the liquid in the pipeline (5) close to the pump (1) pressure
port (4) and the hydrostatic pressure outside of the pump (1) measured in close proximity
to the pressure port (4), and then the acquired value of the determined differential
pressure is compared against the lift (H) resulting from its known value as a function
of capacity (Q), being the given capacity of the pump system, for which that differential
pressure is determined.
2. The method according to claim 1, characterised in that the comparing of the determined differential pressure to the lift involves calculating
the ratio of that differential pressure to that lift.
3. The method according to claim 1 or 2, characterised in that the differential pressure is determined for the pressure values measured at a distance
to the pump pressure port equal to or less than 0.15% of the pump installation depth
(Lp) but also equal to or less than 4 meters.
4. The method according to claim 1 or 2 or, 3, characterised in that the differential pressure is determined by measuring the liquid pressure in the pipeline
(5) and the liquid hydrostatic pressure outside of the pump (1) with two separate
liquid electrical pressure transducers (11,15) separately, and then determining the
difference between the two obtained electric signals.
5. The method according to claim 4, characterised in that the pressure transducers (11,15) feature piezo-resistive silicon sensors (19) isolated
from the measured liquid by a separating membrane (20) and manometer liquid (21).
6. The method according to claim 4 or 5, characterised in that the liquid pressure in the pipeline (5) is measured by connecting the pressure transducer
(15) to a port (27) located in an intermediate ring (26) installed in line of the
pipeline (5), advantageously between the pump (1) pressure port (4) and the pipeline
(5) starting section (5').
7. The method according to claim 4 or 5 or 6, characterised in that the liquid differential pressure is determined with a measurement probe, housing
both of the said pressure transducers (11, 15) within the same common body (22) and
where the common body (22) is installed on the pipeline (2), whereas the pressure
transducer (11) of the liquid hydrostatic pressure outside of the pump (1) is oriented
in perpendicular to the pipeline (5) liquid direction of flow.
8. A probe for conducting on-going analysis of the current technical condition of a submersible
pump system comprising a submersible pump immersed in a deep well and a pressure pipeline
discharging the pumped liquid and connected to the pressure port of the same submersible
pump, characterised in that the probe comprises two pressure transducers (11,15) of the forced liquid pressure
provided with electrical outputs, where one of the pressure transducers (15) measures
the pressure of the liquid forced by the pump (1) to the pipeline (5) connected to
its pressure port (4), whereas the other pressure transducer (11) measures hydrostatic
pressure of the liquid the pump (1) is immersed in, each of the pressure transducers
(11, 15) features a separate body (14,16) and on one end of each body (14, 16) there
is a metering orifice (12, 18), while the pressure transducer (11, 15) bodies (14,
16) are installed substantially perpendicular to each other in a common coupling body
(22).
9. The probe according to claim 8, is characterised in that the pressure transducers (11, 15) feature piezo-resistive silicon sensors (19) isolated
from the measured liquid by a separating membrane (20) and manometer liquid (21).
10. The probe according to claim 8 or 9 is characterised in that it additionally features an intermediate ring (26), which is to be placed between
the pump (1) pressure port (4) and the pipeline (5) starting section (5'), and the
intermediate ring (26) is provided with a port (27) connected by a line (28) to the
metering orifice (18) of the pressure transducer (15) of the liquid forced by the
pump (1).
11. The probe according to claim 8 or 9 or 10, characterised in that it additionally features a fixture (23) for fastening the probe to the pipeline.
1. Eine Methode zum Diagnostizieren des aktuellen technischen Zustands eines Tauchpumpsystems,
bestehend aus einer Tauchpumpe mit bekanntem Verlauf der Förderhöhe als Funktion der
Förderleistung, der an einem Prüfstand ermittelt wurde, wobei die Tauchpumpe in der
in einem Tiefbrunnen enthaltenen Flüssigkeit getaucht war, und einer Druckrohrleitung
samt Armaturen zur Ableitung der gepumpten Flüssigkeit, angeschlossen an den Druckstutzen
dieser Tauchpumpe, dadurch gekennzeichnet, dass für eine bestimmte Förderleistung des Pumpsystem, gemessen an dessen Auslauf, die
Druckdifferenz zwischen der Flüssigkeit in der Rohrleitung (5) in der Nähe des Druckstutzens
(4) der Pumpe (1) und dem hydrostatischem Druck außerhalb der Pumpe (1) in der Nähe
des Druckstutzens (4) gemessen wird, und der erhaltene Wert des Druckunterschieds
mit der Förderhöhe (H) verglichen wird, die sich aus dem bekannten Wert als Funktion
der Förderleistung (Q) ergibt, die eine festgelegte Förderleistung des Pumpsystems
ist, für die der Druckunterschied ermittelt wurde.
2. Die Methode nach Anspruch 1 dadurch gekennzeichnet, dass der Vergleich des ermittelten Druckunterschieds mit der Förderhöhe die Berechnung
des Verhältnisses des Druckunterschied zu dieser Förderhöhe umfasst.
3. Die Methode nach Anspruch 1 oder 2 dadurch gekennzeichnet, dass der Druckunterschied für Druckwerte ermittelt wird, die nicht weiter als bei 0,15%
der Installationstiefe (Lp) der Pumpe (1) und nicht weiter als 4 Meter vom Druckstutzen
entfernt gemessen wurden.
4. Die Methode nach Anspruch 1 oder 2 oder 3 dadurch gekennzeichnet, dass der Druckunterschied durch die Messung des Flüssigkeitsdrucks in der Rohrleitung
(5) und des hydrostatischen Druck der Flüssigkeit außerhalb der Pumpe (1) ermittelt
wird, und zwar unter Verwendung zweier separater elektrischer Hydrodruckwandler (11,15),
wobei der Unterschied zwischen den beiden erhaltenen Elektrosignalen bestimmt wird.
5. Die Methode nach Anspruch 4 dadurch gekennzeichnet, dass die Druckwandler (11,15) piezo-resistive Siliziumsensoren (19) enthalten, getrennt
von der Flüssigkeit durch eine Membrane (20) und die Manometer-Flüssigkeit (21).
6. Die Methode nach Anspruch 4 oder 5 dadurch gekennzeichnet, dass die Flüssigkeitsdruckmessung in der Rohrleitung (5) auf dem Wege der Verbindung des
Druckwandlers (15) mit der Öffnung (27) im Zwischenring (26) erfolgt, der in der Linie
mit der Rohrleitung (5) installiert ist, vorzugsweise zwischen dem Druckstutzen (4)
der Pumpe (1) und dem Anfangsabschnitt (5') der Rohrleitung (5).
7. Die Methode nach Anspruch 4 oder 5 oder 6 dadurch gekennzeichnet, dass der Flüssigkeits-Druckunterschied mit einer Messsonde ermittelt wird, in der sich
die beiden besagten Druckwandler (11, 15) befinden und die im gleichen gemeinsamen
Gehäuse (22) untergebracht ist, wobei das Gehäuse (22) an der Rohrleitung (2) installiert
ist, während der Druckwandler (11) zur Messung des hydrostatischen Drucks der Flüssigkeit
außerhalb der Pumpe (1) rechtwinklig zur Flussrichtung der Flüssigkeit in der Rohrleitung
(5) angeordnet ist.
8. Eine Sonde zur laufenden Prüfung des technischen Zustands des Tauchpumpsystems, bestehend
aus der im Tiefbrunnen getauchten Tauchpumpe und einer Druckrohrleitung zur Ableitung
der gepumpten Flüssigkeit, angeschlossen an den Druckstutzen dieser Tauchpumpe, dadurch gekennzeichnet, dass die Sonde zwei Druckwandler (11,15) zur Druckmessung der geförderten Flüssigkeit
enthält, ausgestattet mit elektrischen Ausgängen, wo einer der Druckwandler (15) den
Druck der durch die Pumpe (1) in die an den Pumpen-Druckstutzen (4) angeschlossene
Rohrleitung (5) geförderten Flüssigkeit, während der andere Druckwandler (11) den
hydrostatischen Druck der Flüssigkeit misst, in der die Pumpe (1) getaucht ist, wobei
jeder der Druckwandler (11, 15) ein separates Gehäuse (14,16) aufweist, an dessen
Ende sich eine Messöffnung (12, 18) befindet, wobei die Gehäuse (14, 16) der Druckwandler
(11, 15) grundsätzlich rechtwinklig zueinander in einem gemeinsamen Verbindungsgehäuse
(22) montiert sind.
9. Die Sonde nach Anspruch dadurch gekennzeichnet, dass die Druckwandler (11, 15) piezo-resistive Siliziumsensoren (19) enthalten, getrennt
von der Flüssigkeit durch eine Membrane (20) und die Manometer-Flüssigkeit (21).
10. Die Sonde nach Anspruch 8 oder 9 dadurch gekennzeichnet, dass sie zusätzlich einen Zwischenring (26) enthält, der zwischen dem Druckstutzen (4)
der Pumpe (1) und dem Anfangsabschnitt (5') der Rohrleitung (5) montiert wird, und
der Zwischenring (26) die Öffnung (27) aufweist, verbunden durch eine Leitung (28)
mit der Messöffnung (18) des Druckwandlers (15) zur Messung des Drucks der durch die
Pumpe (1) geförderten Flüssigkeit.
11. Die Sonde nach Anspruch 8 oder 9 oder 10 dadurch gekennzeichnet, dass sie zusätzlich eine Vorrichtung (23) zu ihrer Befestigung an der Rohrleitung enthält.
1. Procédé d'analyse continue de l'état technique actuel d'un système de pompe submersible
constitué d'une pompe submersible ayant une levée connue en tant que fonction d'une
capacité déterminée sur un banc d'essai, la pompe submersible étant immergée dans
un liquide contenu dans un puits profond, et d'une conduite sous pression munie de
raccords pour évacuer le liquide pompé et reliée au raccord de pression de la même
pompe submersible, caractérisé en ce que pour la capacité de la pompe donnée mesurée à son extrémité de sortie, une pression
différentielle est déterminée entre le liquide dans la tuyauterie (5) à proximité
du raccord de pression (4) de la pompe (1) et la pression hydrostatique à l'extérieur
de la pompe (1) mesurée à proximité immédiate du raccord de pression (4), puis la
valeur acquise de la pression différentielle déterminée est comparée à la levée (H)
résultant de sa valeur connue en tant que fonction du débit (Q), qui est la capacité
donnée du système de pompage, pour laquelle cette pression différentielle est déterminée.
2. Procédé selon la revendication 1, caractérisé en ce que la comparaison de la pression différentielle déterminée à la levée consiste à calculer
le rapport de cette pression différentielle à cette levée.
3. Procédé selon la revendication 1 ou 2, caractérisé en ce que la pression différentielle est déterminée pour les valeurs de pression mesurées à
une distance du raccord de pression de la pompe égale ou inférieure à 0,15 % de la
profondeur (Lp) de l'installation de la pompe mais également égale ou inférieure à
4 mètres.
4. Procédé selon la revendication 1 ou 2 ou 3, caractérisé en ce que la pression différentielle est déterminée en mesurant la pression du liquide dans
la tuyauterie (5) et la pression hydrostatique du liquide à l'extérieur de la pompe
(1) par deux capteurs de pression de liquide électriques séparés (11, 15) séparément,
puis en déterminant la différence entre les deux signaux électriques obtenus.
5. Procédé selon la revendication 4, caractérisé en ce que les capteurs de pression (11, 15) comportent des capteurs piézorésistifs en silicium
(19) isolés du liquide mesuré par une membrane de séparation (20) et un liquide manométrique
(21).
6. Procédé selon la revendication 4 ou 5, caractérisé en ce que la pression du liquide dans la conduite (5) est mesurée en raccordant le capteur
de pression (15) à un raccord (27) situé dans un anneau intermédiaire (26) installé
en ligne de la conduite (5), avantageusement entre le raccord de pression (4) de la
pompe (1) et la section initiale (5') de la conduite (5)
7. Procédé selon la revendication 4 ou 5 ou 6, caractérisé en ce que la pression différentielle du liquide est déterminée à l'aide d'une sonde de mesure,
logeant les deux capteurs de pression (11, 15) dans le même corps commun (22) et où
le corps commun (22) est installé sur la conduite (2), le capteur de pression (11)
de la pression hydrostatique du liquide en dehors de la pompe (1) étant orienté perpendiculairement
à la direction du flux du liquide dans la conduite (5).
8. Sonde pour effectuer une analyse continue de l'état technique actuel d'un système
de pompe submersible comprenant une pompe submersible immergée dans un puits profond
et une conduite sous pression déchargeant le liquide pompé et connectée au raccord
de pression de la même pompe submersible, caractérisée en ce que la sonde comprend deux capteurs de pression (11, 15) de la pression du liquide forcée
pourvus de sorties électriques, où l'un des capteurs de pression (15) mesure la pression
du liquide forcé par la pompe (1) à la conduite (5) reliée à son raccord de pression
(4), tandis que l'autre capteur de pression (11) mesure la pression hydrostatique
du liquide dans lequel la pompe (1) est plongée, chacun des capteurs de pression (11,
15) comporte un corps séparé (14, 16) et à une extrémité de chaque corps (14, 16)
il y a un orifice de mesure (12, 18), tandis que les corps (14, 16) des capteurs de
pression (11, 15) sont installés sensiblement perpendiculairement les uns aux autres
dans un corps d'accouplement commun (22).
9. Sonde selon la revendication 8, est caractérisée en ce que les capteurs de pression (11, 15) comportent des capteurs piézorésistifs en silicium
(19) isolés du liquide mesuré par une membrane de séparation (20) et un liquide manométrique
(21).
10. Sonde selon la revendication 8 ou 9 est caractérisée en ce qu'elle comporte en outre un anneau intermédiaire (26) qui doit être placé entre le raccord
de pression (4) de la pompe (1) et la section de départ (5') de la conduite (5), et
l'anneau intermédiaire (26) est muni d'un raccord (27) relié par une conduite (28)
à l'orifice de mesure (18) du capteur de pression (15) du liquide forcé par la pompe
(1).
11. Sonde selon la revendication 8 ou 9 ou 10, caractérisée en ce qu'elle présente en outre un dispositif de fixation (23) pour la fixation de la sonde
sur la conduite.
REFERENCES CITED IN THE DESCRIPTION
This list of references cited by the applicant is for the reader's convenience only.
It does not form part of the European patent document. Even though great care has
been taken in compiling the references, errors or omissions cannot be excluded and
the EPO disclaims all liability in this regard.
Patent documents cited in the description