KR20130022193A - Water treatment apparatus and method for enhancing oil recovery - Google Patents
Water treatment apparatus and method for enhancing oil recovery Download PDFInfo
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- KR20130022193A KR20130022193A KR1020110085024A KR20110085024A KR20130022193A KR 20130022193 A KR20130022193 A KR 20130022193A KR 1020110085024 A KR1020110085024 A KR 1020110085024A KR 20110085024 A KR20110085024 A KR 20110085024A KR 20130022193 A KR20130022193 A KR 20130022193A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 172
- 238000000034 method Methods 0.000 title claims abstract description 53
- 238000011084 recovery Methods 0.000 title claims description 89
- 230000002708 enhancing effect Effects 0.000 title abstract description 7
- 239000003129 oil well Substances 0.000 claims abstract description 57
- 239000002918 waste heat Substances 0.000 claims abstract description 43
- 238000001914 filtration Methods 0.000 claims abstract description 12
- 239000010779 crude oil Substances 0.000 claims description 64
- 239000003921 oil Substances 0.000 claims description 46
- 239000012530 fluid Substances 0.000 claims description 18
- 230000001678 irradiating effect Effects 0.000 claims description 9
- 238000002347 injection Methods 0.000 claims description 8
- 239000007924 injection Substances 0.000 claims description 8
- 238000012546 transfer Methods 0.000 claims description 5
- 239000008400 supply water Substances 0.000 claims description 4
- 238000009281 ultraviolet germicidal irradiation Methods 0.000 claims description 3
- 239000002244 precipitate Substances 0.000 claims description 2
- 239000013535 sea water Substances 0.000 abstract description 11
- 238000012423 maintenance Methods 0.000 abstract description 4
- 244000005700 microbiome Species 0.000 description 17
- 238000004519 manufacturing process Methods 0.000 description 16
- 239000007789 gas Substances 0.000 description 14
- 239000000126 substance Substances 0.000 description 14
- 239000003208 petroleum Substances 0.000 description 11
- 230000001965 increasing effect Effects 0.000 description 9
- 238000005553 drilling Methods 0.000 description 8
- 241000196324 Embryophyta Species 0.000 description 7
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- 230000007423 decrease Effects 0.000 description 5
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- 239000001569 carbon dioxide Substances 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 230000001954 sterilising effect Effects 0.000 description 3
- 238000004659 sterilization and disinfection Methods 0.000 description 3
- 241000195493 Cryptophyta Species 0.000 description 2
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- 230000008439 repair process Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000011343 solid material Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 241000191291 Abies alba Species 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
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- 230000015572 biosynthetic process Effects 0.000 description 1
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- 238000000605 extraction Methods 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
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- 230000002588 toxic effect Effects 0.000 description 1
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/12—Methods or apparatus for controlling the flow of the obtained fluid to or in wells
- E21B43/121—Lifting well fluids
- E21B43/124—Adaptation of jet-pump systems
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/34—Arrangements for separating materials produced by the well
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/32—Details relating to UV-irradiation devices
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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Mining & Mineral Resources (AREA)
- Geology (AREA)
- Environmental & Geological Engineering (AREA)
- Physics & Mathematics (AREA)
- Geochemistry & Mineralogy (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Fluid Mechanics (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Toxicology (AREA)
- Physical Water Treatments (AREA)
Abstract
Description
The present invention relates to an apparatus and a method for promoting recovery of crude oil stored in an oil well, and more particularly, to an apparatus and a method for treating waste water and treating water injected into an oil well for improving crude oil recovery.
In order to produce crude oil (petroleum), it is necessary to go through the process of drilling exploration and drilling.
First, in order to produce crude oil (oil), after exploration of the surface or the seabed, the location, size and nature of the nonexistence are estimated based on the exploration results, and based on this, the existence of crude oil (petroleum) is confirmed.
After that, to get additional precise underground information, drilling and exploration work in the basement, which is called drilling exploration.
Drilling work is to drill soil and rock while rotating in the ground using a rotary excavator called a bit.
Rotary drilling can be excavated not only in the vertical direction, but also horizontally or in any direction. It is also possible to dig up to thousands of meters by installing rigs for drilling not only on land but also at sea.
If crude oil (oil) is found during the drilling process, it is transferred to the development and production stage. On the ground, a production unit called a Christmas tree, which extracts crude oil (petroleum) and gas, is installed. On the sea, a platform is installed to produce crude oil.
The offshore platform is installed in various sizes according to the depth of the sea, the size of the oil field, and the distance from the land, and is fixed to the sea floor by using steel and concrete. Holes can be drilled because they use a dynamic positioning system (DPS). The largest platform is a 25-storey building taller than a football field, with more than 500 production engineers.
In the early stages of oil well production, petroleum spews upwards due to the pressure of water under gas or crude oil. This is often called magnetic powder.
Unless the reservoir is very shallow, in general, crude oil (petroleum) flows well in the early stages of production, but if the pressure in the reservoir decreases over time, the production of natural crude oil stops. Most of the crude oil (petroleum) is stored in the reservoir without being produced.
The production of crude oil (petroleum) by natural ejection by pressure in the oil layer is called primary recovery.
Crude oil (petroleum) produced by primary recovery is only 5-15% of reserves. The rest is forcibly recovered by injecting gas into the well or by injecting water, which is called secondary recovery.
After the second recovery, about 70% to 70% of crude oil (oil) remains in the well. Therefore, water vapor, surfactants, hydrocarbon gas, carbon dioxide gas and the like are injected into the oil layer to recover some of them somehow in a state where gas and crude oil (petroleum) are completely mixed, which is called tertiary recovery.
The crude oil coming from the underground is mixed with gas and water, so the gas and water are first separated from the crude oil, and the gas separates the crude oil and water, and removes impurities such as hydrogen sulfide and carbon dioxide. Are temporarily stored in tanks and then transported to destinations by pipelines.
The method for recovering crude oil (petroleum) that is not produced and stored, such as crude oil that requires secondary and tertiary recovery, is called enhanced oil recovery (EOR). Costs are required, resulting in higher production costs of crude oil (oil), and much research is needed to lower the production cost of crude oil (petroleum).
Therefore, the present invention has been invented in view of the above circumstances, and by changing the treatment method for water injected into oil wells for improving crude oil recovery, it is possible to prevent the system impact on the crude oil recovery enhancement device in advance, and to recover waste heat. It is an object of the present invention to provide an apparatus and method for lowering the maintenance cost of a recovery enhancing apparatus.
According to an aspect of the present invention for achieving the above object, in the water treatment apparatus for treating the water to be injected into the oil well in order to improve the recovery of the crude oil stored in the oil well, the water to be injected into the oil well supplied from the outside and stored A
The waste
The low temperature fluid is oil or hot water supply water;
It characterized in that it further comprises a;
It is characterized in that it further comprises; a
According to another aspect of the present invention, in the water treatment method for treating the water to be injected into the oil well in order to improve the recovery of the crude oil stored in the oil well, water supply step of receiving the water to be injected into the oil well chamber 300 (S10); A water storage step (S20) of storing the water supplied to the
According to another aspect of the present invention, in the water treatment method for treating the water to be injected into the oil well in order to improve the recovery of crude oil stored in the oil well, the water to be injected into the oil well is irradiated with ultraviolet rays, the water irradiated with ultraviolet light It provides a water treatment method for crude oil recovery, characterized in that for recovering waste heat from the injecting water into the well.
The waste heat is recovered by being delivered to the low temperature oil or low temperature hot water supply water is supplied to the demand destination.
The ultraviolet irradiation is made in the
According to the present invention, by changing the treatment of water injected into the oil well to improve the oil recovery to the method of irradiating ultraviolet light instead of the method of injecting chemicals to the oil recovery system due to delayed chemical injection to the oil recovery device The system shock that occurs can be prevented in advance.
In addition, the maintenance and repair of the oil recovery apparatus can be performed only by supplying a power supply for the operation of the ultraviolet lamp and replacing the lamp, thereby significantly lowering the maintenance and repair costs of the oil recovery apparatus.
In addition, the removal efficiency of microorganisms can be higher than existing methods using chemicals, and the safety of equipment for improving crude oil recovery is also increased.
In addition, the use of chemicals harmful to the human body increases the safety of the natural environment and the safety of the working environment.
In addition, energy efficiency can be improved by recovering the waste heat of the ultraviolet-treated water.
1 is a view schematically showing a device for improving the existing crude oil recovery.
Figure 2 schematically shows a water treatment apparatus for crude oil recovery in accordance with the present invention.
Figure 3 schematically shows a water treatment method for crude oil recovery in accordance with the present invention.
Hereinafter, with reference to the accompanying drawings will be described in detail the configuration and operation of the preferred embodiment of the present invention. In the drawings, like reference numerals refer to like elements throughout. The same reference numerals in the drawings denote like elements throughout the drawings.
Crude oil is installed from various production equipment and pulled from the basement (or seabed) to the ground (or sea). In the early stage of production, it is produced smoothly by natural pressure, but over time, the pressure decreases and the output decreases. The stage of oil extraction from the ground includes primary, secondary and tertiary recovery as described above.
Specifically, in the first recovery step, the reservoir is subjected to pressure by some natural mechanism. Groundwater pushes oil toward the borehole, increasing pressure as the gas above the reservoir and the gas contained in the crude oil expand. Sufficient underground pressure in the reservoir will push oil to the surface and align complex valves on the wellhead to connect to the pipelines for oil storage or disposal. Recovery rates in the first recovery stage are usually around 5-15%.
In the second recovery phase, the oil pressure gradually decreases over a period of time, making it impossible to push the oil to the surface. As described above, when the pressure of the oil reservoir decreases due to magnetic force, the secondary recovery method is performed.
External energy in the form of fluid is injected to artificially raise the pressure in the reservoir to push the oil out. Sometimes an oil pump is used to drain the oil, and another secondary recovery method is water (water) or gas. In addition, air, carbon dioxide, and other gases are injected to clean the wells, increasing oil flow and increasing production. The recovery rate from water injection is usually 30%, depending on the nature of the oil and the characteristics of the reservoir.
In the third stage of recovery, the pressure of the oil bed is not increased, but the viscosity of the crude oil itself is increased to improve the permeability, thereby increasing the yield. Steam is injected into the well, which is the usual method, by turning the gas turbine to generate electricity and injecting the steam generated by the waste heat. This method is mainly used in heavy crude oil production.
This third recovery should only be profitable if it is not feasible with the second recovery method. Therefore, if the oil price is high, the third recovery is performed, but if the oil price is low, it is stopped.
Maximizing recovery in three runs will only take 30-40% of the oil in places.
The manual method of the secondary recovery method is a technique that is generally widely used for recovery recovery. Water is the most preferred recovery promotion method because it has a very good fluidity in the reservoir and is effective for extracting oil, and it can be easily secured and the operation cost is low.
However, the method is simple and inexpensive compared to other crude oil recovery methods, but after a certain time, the oil well is blocked by foreign substances or residues, or underwater microorganisms such as bacteria grow and block the oil well or water supply pipe. There is a need for a water treatment process for treating the chemicals for the water supplied to the filtration device and the oil well, which causes a lot of additional costs, causing a rise in the production cost of crude oil.
In addition, if there is a slight time lag when supplying chemicals and the quality of the water supplied to the well is not met, the water should be discarded, and the water of suitable quality to be supplied to the well again. You have to make it. The system impact on the oil recovery increaser also raises the production cost of crude oil.
In addition, a significant amount of chemicals are used to remove the microorganisms in the water, and the chemicals are very harmful to the body and the environment, and the chemicals leave toxic or residues. In addition, caution should be exercised in the formation of other compounds which may cause secondary contamination.
Ultraviolet light is a light with a wavelength ranging from approximately 0.1 nm to 400 nm, and has a relatively high energy. When directly irradiated onto the cell membrane of the microorganism, the ultraviolet ray destroys the cell wall or cell membrane of the microorganism and prevents the growth of the microorganism. Have
Therefore, if the method of removing microorganisms with chemicals for the water supplied to the oil well is changed to the method of ultraviolet irradiation, microorganisms that have not reacted with chemicals must also pass through an ultraviolet lamp, so microorganisms can be removed. Higher efficiency, no chemicals harmful to the human body, safety of the environment and safety of the working environment are also enhanced. Operation costs are also used only by the electricity supplied to the lamp, except for the initial installation cost of UV lamps. This can be significantly reduced compared to the cost.
Existing crude oil recovery water treatment device, as shown in Figure 1, after filtering the seawater withdrawal is installed a water treatment device to directly put chemicals into the piping through which the seawater was removed to remove microorganisms in the water Water treatment apparatus for improving crude oil recovery according to the present invention, by irradiating ultraviolet light into the water to irradiate the microorganisms in the water by causing the photochemical reaction, sterilization, ozone and the like action on the microorganisms in the water It is sterilized to recover the waste heat of water.
In one embodiment of the present invention shown in Figure 2, a water treatment apparatus for treating the water to be injected into the oil well in order to improve the recovery of crude oil stored in the oil well, the
The
The
The
Since the
As the ultraviolet lamp, a conventional ultraviolet tube may be used, or a plurality of ultraviolet tubes having different shapes or outputs may be appropriately disposed in the
Ultraviolet light has a short wavelength and thus has a weak penetrating power, and thus, the number of UV lamps should be sufficiently installed so that the microbial value in the
The capacity of the
It is preferable that the residence time of the water staying in the
In addition, in the
The front of the
Since the
In particular, if the
In the case of installing the
Waste
The surface temperature of the ultraviolet lamp constituting the
The waste
The low temperature fluid changed into a high temperature fluid may be stored in a
By using the waste
The low temperature fluid may be oil or water for hot water supply, and the waste
In addition, the water treatment apparatus for crude oil water promotion according to the present invention may further include a filtration device (150).
That is, water may contain large or non-living organisms such as solids, algae, mud, and the like, which greatly reduces the removal efficiency of aquatic microorganisms by ultraviolet irradiation. Is to install an additional filtration device to remove large foreign objects.
In addition, another embodiment of the present invention shown in Figure 3, a water treatment method for treating the water to be injected into the oil well to improve the recovery of crude oil stored in the oil well, water supply step (S10), water storage step (S20) ), Ultraviolet irradiation step (S30), waste heat recovery step (S40), water injection step (S40).
Water supply step (S10) is to supply the water to be injected into the oil well to the
In addition, another embodiment of the present invention is a water treatment method for treating water to be injected into an oil well in order to improve the recovery of crude oil stored in the oil well, irradiated with ultraviolet light to the water to be injected into the oil well, irradiated with ultraviolet light A method of injecting water into an oil well after recovering waste heat from the wastewater is provided.
As mentioned above, the two embodiments of the invention are illustrated as being carried out at sea, so the water mentioned in the two embodiments would be preferably seawater that can be readily obtained at sea, and the waste heat recovered is cold oil or cold hot water. It can be delivered to the supply water so that it can be supplied to various demand sources in the plant for oil recovery.
In addition, the ultraviolet irradiation is to be made in the
Naturally, the two embodiments of the method invention may be configured by additionally adding various devices constituting the above-described water treatment device invention, and the method invention will be implemented to have the same purpose and function.
Hereinafter, the operation of a water treatment apparatus and method for treating water to be injected into an oil well in order to promote recovery of crude oil stored in the oil well according to the present invention will be described.
First, the seawater is withdrawn by the
The seawater that has passed through the
The high temperature seawater from which the microorganisms are removed from the
The treated seawater is again injected into the oil well by the
It will be apparent to those skilled in the art that various modifications and variations can be made in the present invention without departing from the spirit and scope of the invention will be.
100: first pump 150: filtration device
200: second pump 250: water transfer pipe
300: chamber 310: outlet
400: ultraviolet irradiation device 500: waste heat recovery device
600 tank 650: low temperature fluid pipe
S10: water supply step S20: water storage step
S30: UV irradiation step S40: Waste heat recovery step
S50: water injection step
Claims (9)
A chamber 300 for receiving and storing water to be injected into the well and injecting the stored water into the well;
An ultraviolet irradiation device 400 for irradiating ultraviolet rays to the water stored in the chamber 300; And
A waste heat recovery apparatus 500 installed at a rear end of the chamber 300 to recover waste heat of water injected into the well from the chamber 300;
Water treatment apparatus for crude oil recovery, characterized in that it comprises a.
The waste heat recovery device 500,
Heat exchange occurs between the water transfer pipe 250 through which water injected from the chamber 300 flows into the oil well and the low temperature fluid pipe 650 through which the low temperature fluid flows so that the low temperature fluid recovers waste heat of the water;
Water treatment apparatus for improving crude oil recovery.
The low temperature fluid is water for oil or hot water supply;
Water treatment apparatus for improving crude oil recovery.
A filtration device (150) installed at the front end of the chamber (300);
Water treatment apparatus for crude oil recovery further comprising a.
An outlet 310 disposed at a lower end of the chamber 300 to discharge the precipitate;
Water treatment apparatus for crude oil recovery further comprising a.
A water supply step of receiving water to be injected into the oil well into the chamber 300 (S10);
A water storage step (S20) of storing the water supplied to the chamber 300 for a predetermined time;
UV irradiation step (S30) for irradiating the ultraviolet light to the water stored in the chamber 300 by the ultraviolet irradiation device (400);
Waste heat recovery step (S40) for recovering the waste heat of the water irradiated with ultraviolet rays; And
A water injection step of injecting UV-irradiated water into the oil well (S40);
Water treatment method for crude oil recovery, characterized in that it comprises a.
Irradiating ultraviolet light to water to be injected into the oil well, recovering waste heat from the water irradiated with ultraviolet light, and then injecting water into the oil well;
Water treatment method for improving crude oil recovery.
The waste heat is recovered by being transferred to low temperature oil or low temperature hot water supply water and supplied to a demand destination;
Water treatment method for improving crude oil recovery.
The ultraviolet irradiation is made in the chamber 300 in which water to be supplied to the well can stay for a predetermined time;
Water treatment method for improving crude oil recovery.
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KR1020110085024A KR20130022193A (en) | 2011-08-25 | 2011-08-25 | Water treatment apparatus and method for enhancing oil recovery |
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KR1020110085024A KR20130022193A (en) | 2011-08-25 | 2011-08-25 | Water treatment apparatus and method for enhancing oil recovery |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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KR101995822B1 (en) | 2018-04-27 | 2019-07-03 | 주식회사 이피에스이앤이 | Movable smart water system |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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KR101995822B1 (en) | 2018-04-27 | 2019-07-03 | 주식회사 이피에스이앤이 | Movable smart water system |
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