IPC classes for russian patent Method of examining wells. RU patent 2244105. (RU 2244105):
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Method of examining wells / 2244105
Invention can be used in case of gas-lift operation of wells equipped by free piston-type installations. Invention envisages stopping well, connecting tube space and annular space in wellhead, recording bottom zone and wellhead pressures in tube and annular spaces, and computing well operation parameters using inflow curve plotted according to differences of bottom zone and wellhead pressures. Volume of produced fluid is found from potential output of formation and from condition of output of free piston. When comparing these volumes, parameters of well are computed in the base of minimum volume value.
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Foam-forming compound for shutting wells / 2245441
Foam-forming compound for shutting wells contains hydrocarbon liquid, mixture of surfactants, one of components thereof is water solution of lignosulphonate reagent of 25% concentration, herbal filling agent and 20% water solution of calcium chloride, as lignosulphonate agent reagent it contains powder-like technical lignosulphonate, and as other component of surfactant mixture - hexamethylentetramine, and as herbal filling agent - peat or grass flour with following ratio of components in percents of mass: hydrocarbon liquid 12-14, said water solution of technical powder-like lignosulphonate 17-21, hexamethylentetramine 0.17-0.63, peat or grass flour 3-6, said calcium chloride solution - the rest, while relation of mass portions between said water solution of technical powder-like lignosulphonate and hexamethylentetramine is 1: 0.01-0.03 respectively, as grass flour it contains pulverized herbal waste of grain bread production or similar substance.
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Compound for blocking and shutting wells / 2245996
Compound includes water and inhibiting salt, as inhibiting salt contains processed electrolyte - side product during production of magnesium via electrolysis from carnallite, and additionally as reducer of filtering and thickener - carbooximethylcellulose polymer, and as colmatation agent - magnesium oxide with following relation of components in percents of mass: processed electrolyte - side product of magnesium production via electrolysis from carnallite 10.0-15.0, carbooximethylcellulose 2.5-3.0; magnesium oxide 1.0-2.0, water 80.0-86.5.
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Well killing polysaccharide gel composition and method for producing the same / 2246609
Claimed polysaccharide gel contains sweet or mineralized water, polysaccharide gelling agent, boron cross-linking agent, diethanolamine, quaternary ammonium compounds, and mixture of non-ionic and anionic surfactant (complex surfactant). Mixture of water soluble oxyethilated alkylphenols and their sulphoethoxylates in form of sodium salts or salts with triethanolamine is used as complex surfactant in amount of 0.1-0.5 kg on 1000 l of water being the gel base. Polysaccharide gel is obtained by dissolution and hydration of polysaccharide gelling agent in sweet or mineralized water (preferably monovalent ion solution) followed by treatment of obtained polysaccharide solution with aqueous solution including boron cross-linking agent, diethanolamine, quaternary ammonium compounds, and complex surfactant.
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Method for extraction of hydrocarbon deposit with sole water and extraction of hydrocarbon by sucker-rod compressor pump with separated intake of hydrocarbon and water / 2247228
Method includes mounting compressor pump in such a way, that input aperture of tail piece was positioned below bed sole. Prior to that water cone in face-adjacent zone is destroyed by draining water through tail piece, connected to lower suck-in valve of compressor pump cylinder, and along behind-pipe space through side suck-in valve of compressor pump cylinder. In case of increase of hydrocarbon contained in drained liquid beginning of water cone destruction is assumed. Draining is continued until destruction of emulsion in water cone, formed in non-homogenous porous environment of bed at limits of hydrocarbon-water and water-hydrocarbon, separation of water and hydrocarbon streams and bringing current water-hydrocarbon contact to initial position. Then during extraction water is drained through tail piece, and hydrocarbon - along behind-pipe space.
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Well stopping method / 2250360
Method includes preparation of technological liquid - water solution of sylvinite ore mixture with chlorine calcium by solving a mixture of components in hot fresh technical water, drained from oil and water preparation plants or bed water. During solution of sylvinite ore mixture with chlorine calcium in bed water the latter is drained from the well at temperature 60-90°C. Technological liquid is produced with solution density 1.23-1.37 t/m3. Then prepared technological liquid is fed into well shaft a bit lower, oppositely to zone and above ceiling of productive bed with forming of hydraulic column above the latter. Then well shaft to the mouth is filled with water. Value of technological liquid hydraulic column of high density on basis of said mixture, fed into well shaft above ceiling of productive column of technological liquid is taken in amount, necessary and enough from well stopping conditions.
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Well killing composition / 2254454
Water-based composition that can be used for killing of well during pullout of hole and well remedial work as well as for temporary abandonment of well contains, wt %: carboxymethylcellulose3.5-4.5, sodium hydroxide1.5-2.0, copper sulfate 0.3-0.4, and methanol 4.0-16.0.
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Method for shutting a well / 2255209
Method includes serial pumping into well of buffer, blocking and pressing liquid, blocking liquid contains hydrocarbon base, acyclic acid, caustic soda and mineral filler with following relation of components in percents of mass: hydrocarbon base 41-72, acyclic acid 6.1-14.4, caustic soda 4.9-13.0, mineral filler the rest. Hydrocarbon base of blocking liquid is oil or oil processing products. As mineral filler blocking liquid has calcium carbonate with diameter of particles no less than 2 micrometers.
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Method for operating gas-lifting oil well, gas-lifting oil well and method for controlling flow of multi-phase flowing substance in gas-lift oil well / 2256067
At least one acoustic dynamic is mounted immediately on product pipe in oil well and acoustic characteristic of flowing environment flow is determined in product pipe. It is sent into surface controller, using product pipe. Using surface controller flowing substance flowing mode is determined, on basis of which working parameters of oil well are adjusted. Working parameters of oil well can be adjusted to detect Taylor mode of flow. For adjustment of working parameters throttle is used and/or controlled valve of oil well, controlling amount of gas, forces into product pipe. For determining mode of flow of flowing environment artificial neuron net can be used. It is possible is provide energy for acoustic sensor through product pipe. It is possible to determine additional physical characteristics of flowing substance, for example pressure and temperature.
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System for controlling connections and feeding of electric current, oil well for extracting oil products (variants) and method for extracting oil product from oil well / 2256074
System has first induction throttle, second induction throttle and controlled switch. Second induction throttle is positioned near second branch of pipeline structure. Controlled switch has two outputs. First switch output is electrically connected to pipeline structure on the side of induction throttles connection, where first and second branches of pipeline structure intersect. Second output of switch is electrically connected to pipeline structure on other side of at least one induction throttle. Pipeline structure can be positioned inside oil well, and can have casing string and operation tubing column. Also described is method for extracting oil products from oil well using said system.
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Method of examining wells / 2244105
Invention can be used in case of gas-lift operation of wells equipped by free piston-type installations. Invention envisages stopping well, connecting tube space and annular space in wellhead, recording bottom zone and wellhead pressures in tube and annular spaces, and computing well operation parameters using inflow curve plotted according to differences of bottom zone and wellhead pressures. Volume of produced fluid is found from potential output of formation and from condition of output of free piston. When comparing these volumes, parameters of well are computed in the base of minimum volume value.
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Functional insert for well stream plant / 2244118
Device has body placed in body of stream pump and has locking valve and axial channel for logging cable with fixed logging device. Device also has discharge valve. Device body has ports in middle portion, which connect middle hollow portion of device to displacement chamber for stream pump. In upper and lower portions of body of device upper and lower compactors are placed, limited by support elements on each side of the latter, respectively. Locking valve is mounted in lower portion of device and mated with inner space of tubing string and logging device. Axial channels of valves are eccentric and parallel to first channel of device, while discharge valve is provided with rod with its end prominent relatively to body of device.
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Method for delivering devices into well and device for realization of said method / 2244119
Method includes selection of cable of required rigidity and fixing devices on it. Transporting of devices into well is performed under effect from weight of cable and devices. Cable also contains inner hermetic pipe, which is plugged on both sides prior to lowering cable into well. Liquid is pumped into pipe under pressure through locking valve in upper plug and is kept in pipe under constant pressure during operation. After that cable is lowered with devices fixed to it. Value of pressure of liquid in pipe is determined from formula Ppipe≥ Pwell(Scable/Spipe-1)-QcablexLcable/Spipe<Ptear, where Ppipe - pressure of fluid in pipe, kg-wt/sm2; Scable - cross-section of cable with pipe, sm2; Pwell - hydrostatic pressure of well liquid column at depth of planned delivery of devices on cable, kg-wt/sm2; Spipe - cross-section area of pipe aperture and plug area equal to it in contact with liquid in pipe, sm; Qcable - weight of 1 km of cable with pipe, kg-wt; Lcable - length of cable to depth of planned delivery of devices, km; Ptear - pressure of liquid in pipe leading to tear of cable, kg-wt/sm2, determined from formula: Ptear=Ftear/Spipe, where Ftear - tear force for cable according to documentation, kg-wt.
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Profile meter / 2244120
Device has body, spring-loaded levers jointly connected to it, levers position indicator, made in form of constant magnet mounted at joint connection end of each measuring lever, and signal converter, mounted in body in protective chamber. Constant magnet is made in form of washer and is mounted in circular groove on rotation axis of each lever, and as signal converter magnetic-resistive sensor is used in form of resistive bridge circuit sensitive to direction of magnetic field and non-sensitive to its intensity, while magnetic axis of constant magnet is in plane of washer and is directed perpendicularly to sensitivity axis of magnetic-resistive sensor.
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Device for detecting obstruction positions in operation column / 2244121
Device has body with ports in lower and upper ends, main sensitive elements in form of turbines and packing elements, placed in pairs at body ends, side port made in body between main sensitive elements and converter, connected to surface equipment. In side pipe, mounted inside the body between main sensitive elements, additional sensitive element is placed in form of turbine and thermal sensor. Lower end of side pipe is connected to side port. Diameter of turbine of additional sensitive element is less than diameter of turbines of main sensitive elements. Converter is a control block mounted above body including sleeves locator and electronic microprocessor device.
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Method of measuring liquid flow in gas-liquid mixtures / 2244122
Invention relates to gas-liquid systems coming from oil production wells. Mixture is separated into liquid and gas in separator. Liquid is periodically accumulated in separator container and then displaced with gas. During this operation, differential pressure for liquid reaching its lower and upper recorded levels and time required for filling recorded volumes are measured as well as absolute pressure and temperature of gas in container. Liquid flow value expressed in weight is calculated using special mathematical dependence. At oil field, liquid and gas enter separator from preliminary gas intake installation or from the first separation step.
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Device for metering pressure / 2244779
Device comprises probe (working tip), control-rod, pipeline, communication line, loading jig and measuring station. Probe includes hollow cylindrical body with bottom and cap filled with working liquid, elastic shell sealed from body bottom and top. Formed in non-fixed elastic shell area are perforations. Piston with rod is installed in upper part of hollow body above working liquid. Rod passes through cap in sealed manner. Rod is connected with control rod so that piston may move in axial direction. Formed above piston is cavity connected to pipeline. Hollow body has bottom in which air-tight plug is installed. Measuring device is made as linear piston displacement transducer. Through orifices are formed in hollow body wall near body bottom. Arranged from body outside are vertical or inclined grooves aligned with through orifices by lower ends thereof. Air-tight plug is provided with adjustable rest for restricting piston stroke.
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Method for monitoring underground placement of liquid industrial waste in deep water-bearing horizons / 2244823
Method includes performing a test pumping of liquid waste into absorbing well before operational pumping, while changing flow step-by-step. From equation of absorption base hydrodynamic parameters are determined for calculation of predicted coefficients of operation characteristics of absorbing well and reserve well. During operational pumping of liquid waste together with thermometry along absorbing well shaft, registration of actual pressures and flow on pump devices, actual pressures on mouth in tubing pipes of absorbing well, actual pressures on face are additionally registered in absorbing well as well as pressures on mouth in behind-pipe space, actual loss at mouth in behind-pipe space, actual loss of waste on mouth, actual positions of face well, upper and lower limits of absorption range from well mouth. In reserve well actual pressures on face are registered, as well as actual positions of liquid level from reserve well mouth, upper and lower limits of absorption range. Prediction coefficients are compared for operation characteristics of absorbing well and reserve well to actual coefficients. 9 conditions of hydrodynamic bed conditions at reserve well and absorbing well are considered during pumping of waste. Specific actions of operator on each condition are described.
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Method for examining horizontal wells / 2244824
Method includes lowering protective container to the well to portion of intensive curvature of shaft, which container is fixed at end of drilling pipes, lowering of geophysical device into protective container on lower portion of logging cable, delivery of protective container with geophysical device to pit-face by consecutive extending of drilling pipes column, lowering of upper portion of logging cable through remote-controlled compactor of logging cable fixed on branch of swivel, into drilling pipes, until electric contact to free end of lower portion of logging cable via detachable connecting sleeve, geophysical examining of shaft during raising of geophysical device together with drilling pipes with appropriate connection-disconnection of fixing ends of lower and upper portions of logging cable when screwing away each following drill stand. When examining wells having extensive steeply slanted portion of well shaft with zenith angle of 50°-90°, where lowering of upper portion of logging cable to electrical contact with free end of lower portion of logging cable via detachable connecting sleeve under its own weight is difficult due to friction at drilling column wall, forced lowering of detachable connecting sleeve is performed by feeding washing liquid under pressure into drilling pipes and concurrent adjustment of pressure in chamber of remote-controlled compactor of logging cable. Pressure in chamber of remote-controlled logging cable compactor is achieved to be close to pressure of washing liquid in drilling pipes, to provide for optimal speed of cable lowering and its pressurization, and after connection of detachable connecting sleeve to lower portion of logging cable during raising and lowering of drilling pipes, examinations of well are performed.
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Method and device for measuring gas loss in gas-liquid mixtures / 2244825
Mixture is separated on liquid and gas in separator. Liquid is periodically collected and forced away by gas while measuring absolute pressure and gas temperature in separator tank near upper and lower fixed liquid levels, and times of forcing away of fixed liquid volume. Additionally measured are absolute pressure and temperature in moment when liquid reaches intermediate fixed level. Then liquid is forced from intermediate fixed level to lower fixed level separator is switched off from well, and mass loss of gas is calculated from provided relation. Device for realization of method consists of separator with feeding pipe, in which a three-drive valve is mounted, and draining pipe, which through said valve is connected to liquid outlet channel and to gas outlet channel. Separator is provided with sensors of temperature and pressure and sensors of upper, intermediate and lower levels, mounted in such a manner, that they separate fixed volumes between each other in separator tank, in case of equality of which calculations are simplified.
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FIELD: mining industry.
SUBSTANCE: invention can be used in case of gas-lift operation of wells equipped by free piston-type installations. Invention envisages stopping well, connecting tube space and annular space in wellhead, recording bottom zone and wellhead pressures in tube and annular spaces, and computing well operation parameters using inflow curve plotted according to differences of bottom zone and wellhead pressures. Volume of produced fluid is found from potential output of formation and from condition of output of free piston. When comparing these volumes, parameters of well are computed in the base of minimum volume value.
EFFECT: optimized well operation.
2 dwg
The present invention relates to mining, in particular to the study of drilling wells, and can be used in gas-lift well operation, equipped with a plunger lift installations.
The known method for wells to be converted for operation of plunger lift, which stopped at the mouth of the well record the difference of the pressures in the annulus and Elevator pipes. Taking into account the density of the formation fluid to determine the volume of the liquid and the height of her post in the lift pipe. The equation of the balance of pressures in the receipt of fluid and plunger head count of the working gas pressure in the annulus, and the assumption that the plunger is constantly in motion, set the number of cycles plunger lift (see “Plunger Lift: Introduction, Applications, Equipment, Equations, Operations”, the company's catalog Production Control Services, copyright, 1996, p.5-6).
The disadvantage of this method is that the design works well lead without taking into account the real characteristics of the reservoir, working in conditions of variable depression. In addition, the location of the anchor Shoe lift pipes justified for depleted wells and may not be applicable to wells with relatively high formation pressure, where there are restrictions on the amount of depression on the formation.
There is a method of research oil wells copyright certificate №653385, E 21 In 47/00, 1979, including the recovery of downhole pressure to the reservoir with the dimension in the process of further short-term selection of fluid falling downhole pressure, closing wells on the mouth and termination of the selection of the fluid by measuring the change of pressure with time at the bottom, in the annulus and on the buffer. While the magnitude of the flow are calculated according to equation depending on the sectional area of the borehole, the increment in time pressure recovery at the pit's mouth, in the annulus and on the buffer, and the density of the oil at reservoir conditions.
The disadvantages of the above method include the uncertainty in time of sampling fluid, without which it is impossible to predict a decrease in bottomhole pressure and, consequently, the depression on the layer. The working value of the depression defines the performance of the well and in General is in the range between the maximum and minimum values, due to the requirements of sustainable exploitation.
Closest to the proposed method is a method of research wells equipped with a plunger lift installations, RF patent No. 2165519, E 21 In 43/12, 47/00, 2001, including the well shutdown, reducing the liquid to a valid value, the registration bottomhole and wellhead pressures in reported on the mouth of the pipe and the annular spaces and calculation of parameters of the wells, which use the curve flow of the liquid from the difference graphs bottomhole and wellhead pressures, and on it, asking the depression on the layer, calculate the depth of the location of the working holes and the volume of liquid raised for the cycle of operation of plunger lift.
The disadvantages of the prototype should include the inability to design a technological regime of the well based on a comparative analysis of the performance of the reservoir at a variable depression and performance of the lift.
The aim of the invention is to optimize the life of the well.
This is achieved by the fact that in the proposed method of research is well equipped with installing plunger lift, including a stop well, the message pipe and annular spaces on the mouth, registration bottomhole and wellhead pressures in the pipe and annulus spaces and calculation of the parameters of the well along the curve of inflow, based on the difference between the graphs bottomhole and wellhead pressures, calculate the volume of the produced fluid in the potential productivity of the reservoir and the performance condition plunger lift, compare the volume and the lower volume calculate the parameters of a well.
The proposed method is as follows:
- well prepared for the descent of underlying instruments, if necessary, conduct a heat treatment (FACT) and sweeping-up;
- reduce the liquid level in the well to the depth permitted by condition for the establishment of maximum depression of the reservoir;
- lower depth gauge on the bottom of a well; the preferred type of device is nanothermometer AMT, account settings, which is carried out in real time;
- set the second recording gauge buffer wells;
- report on the mouth between the ring and tube space;
simultaneously hermetically isolated from commercial communications and atmospheric pressure;
- conduct simultaneous registration of change of pressure at the bottom hole and wellhead within 24-36 hours with periodic control by measuring the gas pressure in the buffer according to an exemplary gauge every 4-6 hours;
- write down the gradient curve pressure gas-liquid mixture in the tubing when lifting pressure gauge with bottom-hole with periodic stops (step 250 m), or with a uniform continuous movement gauge to check the depth of the device and the time from the beginning of the ascent.
The method is illustrated in the drawings. Figure 1 shows a synchronous changes of pressure in the study wells with a closed mouth, figure 2 - graphs of pressure changes in the research process well # 24226.
For the interpretation of research results in the coordinate system p=f(t) synchronize readings downhole and wellhead pressure gauges and build time dependency downhole R Zab (line I) and wellhead R u (line II) pressure, and graph the difference between these two pressures (line III), which represents a curve of flow of fluid R W back-pressure at the mouth (figure 1). In the right part of the graph mark the formation pressure (point 1), which lay down the minimum depression in the reservoir (point 2). From the obtained point spend a horizontal line to the intersection with the line R Zab (point 3) and drop the perpendicular line which intersects the line R W at the point 4 and the x-axis at point 5. Segment between points 3-4 determines the gas pressure p g on the mouth in the annulus in the research process and during operation of plunger lift. Cut between 4-5 points is determined by the pressure of the liquid column p W on the bottom. A similar construction is performed in the left part of the graph (point 1’-5’), while the segment 1’-2’ corresponds to the maximum depression of the reservoir.
The depth of the arrangement of the working openings are calculated according to equation:
where L p.o - depth location of a work entry opening of the gas, m;
N the middle of the perforation interval, m;
R W - fluid pressure downhole in the annulus is determined by the value of the segment 4-5 (figure 1), PA;
ρ W is the density of the fluid in the downhole conditions, kg/m;
g - free fall acceleration, m/2 .
The density of the fluid with regard to water in wells expect:
p W =(1-k )· R n +k in · ρ;
where k is the moisture content, the proportion of the units;
ρ n and ρ accordingly, the density of oil and water, kg/m 3 .
Time (in minutes) work well when lifting fluid (plunger) with an average speed of 5 m/s and given a ten-minute purge wells to determine:
and stop time well:
Θ =(3,7-5,5)· t
The number of produced fluid expect:
a) the potential productivity of the reservoir
where Q’ C - volume of fluid flow at a variable depression, m 3 ;
the current differential pressure at the well bottom, MPa;
k is the permeability, cm 2 ;
h is the effective thickness of the reservoir, cm;
μ - viscosity, SP;
In the volume ratio of the reservoir fluid;
b) the performance condition plunger lift:
where Q C is the volume of liquid raised to the surface for one cycle when the pressure p ZM , m 3 ;
p sm - pressure gas in the annulus, doing the work of lifting the liquid to the surface, MPa, is determined by the value of the segment 3-4, (1);
R b - pressure buffer well (in the train), MPa;
0,3 - constant characterizing the total loss of pressure on the lifting of the plunger, MPa;
K - coefficient taking into account the pressure losses by friction gas;
p q is the pressure required for lifting to the surface of a unit volume of fluid, MPa/m 3 ;
R m W - pressure drop on the fluid friction when raising the volume units MPa/m 3 .
Comparing volumes of liquids Q’ q u Q C , for the project taking the minimum value, which denote Q C .
The maximum pressure p ZM . max gas in the annulus with the amount of filling of the production string when lifting the plunger to the surface is determined by the ratio:
where F KP and F m, respectively, the area of the ring and the tube space, m 2 .
The increase in pressure of the liquid column in the well bottom, corresponding to the volume Q” C , the assumption that fills all available space well, is equal to:
where Δ R W is the increase in pressure of the liquid column, MPa.
The amount of gas necessary to perform a single operation by lifting the plunger to the surface, calculated according to equation:
V g =16,5·· L po · p SSR ;
where V g is the quantity of gas per cycle, thousand m 3 /cycle;
With - empirical constant;
P SMS - arithmetic mean value of the gas pressure in the annulus, MPa.
Specific gas consumption:
The number of cycles of operation per day:
As an example, consider an updated calculation of the mode of operation of well No. 20226 Urengoy field in the periodic plunger of the gas lift. Figure 2 shows a synchronous time-based downhole (line I) and wellhead (line II) pressures, as well as schedule their difference (line III). Initial data for calculation:
- static reservoir pressure of 17.5 MPa;
- downhole pressure: maximum of 10.5 MPa; minimum of 7.5 MPa;
average 9 MPa;
the flow rate of formation fluids 7.2 m 3 /day (by 115.7 cm 3 /s);
- permeability of 5 MD (5· 10-11 cm 2 );
the dynamic viscosity of the reservoir oil 0,5 SP (0,5· 10 2 kgf· s/cm);
is the density of the oil at reservoir conditions, 640 kg/m 3 ;
- the volume ratio of oil to 1.2;
is the effective thickness of the reservoir 5 m (5· 10 2 cm);
- depth of descent of the tubing (the middle of the perforated interval) 2978 m;
- the area of the annular space -130· 10 -4 m 2 ;
- the area of the inner channel tubing 30· 10 -4 m 2 ;
- pressure gas-lift gas in the annular space of 5.0-7.5 MPa;
- pressure on the buffer (the train) 2.5 MPa;
- gas factor oil formation conditions 185 m 3 /m 3 ;
- empirical constant for pipes 73 mm tubing
- (pν +p MF )=102, K=45000,=0,2904· 10 -5
By construction, we find that the pressure of liquid and gas in the annulus at a minimum depression are respectively equal to: p W =6,1 MPa (cut 4-5), p ZM =4,4 MPa (cut 3-4). The ordinates of the points 4 and 4’ are of 6.1 and 4.7 MPa, and the time points 5 and 5’ - 1225 and 570 min, respectively.
The depth of the location of the working hole:
Open period:
The time of the open period of the curved accept t=15 minutes
The stop time well:
Θ =(3,7-5,5)· t=(3,7-5,5)· 15=55-83 minutes;
accept Θ =75 minutes (4500 s).
The volume of formation fluid per cycle by the condition of the fluid flowing from the reservoir:
The volume of liquid raised by the installation of one cycle for the performance of a plunger lift:
Q” p =0,23 m 3
From the comparison it is seen that Q’ C >Q” C , but at well # 20226 possible supply of gas-lift gas with an operating pressure up to 7.5 MPa, the conversion result for p ZM =5.0 MPa obtained Q” C =0.35 m 3 . For this case, the volume of liquid is practically equal to the volume of inflow and in the further calculation, Q p =0,41 m 3 .
The maximum required operating pressure of the gas in the annulus:
The increase in pressure of the liquid column in the tubing of the working hole (pressure difference across the mouth between the annular space and the buffer in the layout without starting clutch):
The required amount of gas for the cycle:
Specific gas consumption:
less gas the oil factor in the formation conditions, therefore, require additional supply of the working gas;
the number of cycles of operation per day
A method of testing and interpretation of results are implemented in commercial practice in the translation of twenty-three wells Urengoi oil and gas work gas lift plunger. Implementation of the proposed method provided reliable data for the design of modes of operation of the plunger lift installations in Novy Urengoy. The effectiveness of the method is confirmed by comparing the actual and estimated production rate of the well, with the relative difference does not exceed 7%.
The method of research wells equipped with installing plunger lift, including a stop well, the message pipe and annular spaces on the mouth, registration bottomhole and wellhead pressures in the pipe and annulus spaces and calculation of the parameters of the well along the curve of inflow, based on the difference between the graphs bottomhole and wellhead pressures, characterized in that the calculated volume of the produced fluid in the potential productivity of the reservoir and the performance condition plunger lift, compare the volume and the lower volume calculate the parameters of a well.
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