US20020139524A1 - Wellsite inert gas generator - Google Patents
Wellsite inert gas generator Download PDFInfo
- Publication number
- US20020139524A1 US20020139524A1 US09/823,776 US82377601A US2002139524A1 US 20020139524 A1 US20020139524 A1 US 20020139524A1 US 82377601 A US82377601 A US 82377601A US 2002139524 A1 US2002139524 A1 US 2002139524A1
- Authority
- US
- United States
- Prior art keywords
- exhaust
- processing system
- wellsite
- inert gas
- compressor
- 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.)
- Abandoned
Links
- 239000011261 inert gas Substances 0.000 title claims abstract description 20
- 239000007789 gas Substances 0.000 claims abstract description 43
- 238000002485 combustion reaction Methods 0.000 claims abstract description 10
- 239000012530 fluid Substances 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 claims description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 12
- 229910052757 nitrogen Inorganic materials 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000004071 soot Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 241000237858 Gastropoda Species 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229910052878 cordierite Inorganic materials 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- JSKIRARMQDRGJZ-UHFFFAOYSA-N dimagnesium dioxido-bis[(1-oxido-3-oxo-2,4,6,8,9-pentaoxa-1,3-disila-5,7-dialuminabicyclo[3.3.1]nonan-7-yl)oxy]silane Chemical compound [Mg++].[Mg++].[O-][Si]([O-])(O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2)O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2 JSKIRARMQDRGJZ-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- -1 fill Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 239000003129 oil well Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Images
Classifications
-
- 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
- E21B37/00—Methods or apparatus for cleaning boreholes or wells
Definitions
- This invention relates to equipment used for well clean out operations.
- the inert gas injector comprises an internal combustion engine, a gas processing system connected to receive low pressure exhaust gas from the internal combustion engine, a pump within the gas processing system, the pump having a low pressure inlet for receiving exhaust gases and the pump having a high pressure outlet; and coil tubing connected to the high pressure outlet of the gas processing system.
- the gas processing system preferably comprises one or more of a particulate filter, exhaust cooler and exhaust separator in series, and in that order before the pump.
- the pump may be a compressor.
- exhaust gas is supplied to a downhole jet pump to drive production fluid to surface.
- FIG. 1 is a schematic showing an embodiment of the invention.
- FIG. 2 is a schematic showing a down hole jet pump for use with an embodiment of the invention.
- a wellsite inert gas injector 10 is preferably truck mounted as shown in the figure and utilizes exhaust from the truck's internal combustion engine 12 as source of inert gas.
- the engine is a diesel engine.
- the exhaust is provided to coil tubing 14 , which is mounted on the truck deck 16 in conventional manner.
- a conventional connection (not shown) is used to connect the outlet 18 to the coil tubing 14 .
- a gas processing system 20 that is connected to receive low pressure exhaust gas from the internal combustion engine and provide high pressure inert gas to the coil tubing 14 through outlet 18 .
- Low pressure and high pressure are relative terms. What matters is that gas at the high pressure outlet 18 has sufficient pressure for use down a well.
- the gas processing system 20 incorporates several modules to process the gas to make it suitable for downhole use.
- the modules are connected in series by conventional gas tight couplings.
- a catalytic diesel particulate filter 22 which may be one manufactured by Nett Technologies Inc. Details of the Nett diesel filter are available from Nett, and briefly described in the following.
- the Nett diesel filter 22 utilizes cordierite wall-flow monoliths to trap the soot produced by heavy-duty diesel engines.
- a cylindrical filter element in the filter 22 has of many square parallel channels running in the axial direction, separated by thin porous walls. The channels are open at one end, but plugged at the other. Particulate laden exhaust gases are forced to flow through the porous walls.
- a proprietary noble metal catalyst is coated onto the inside surface of the filter monolith. The catalyst lowers the soot combustion temperature to allow the filter to regenerate. The accumulated soot is oxidized in the filter during regular operation of the engine. Periods with exhaust temperatures of at least 350-400 degrees Fahrenheit are necessary for proper filter regeneration. However, so far as this invention is concerned in its broadest preferred aspect, a particulate filter is required to sufficiently clean the exhaust that the gas processing components are not damaged and the remaining particulate in the inert gas does not have a negative effect on the well.
- an exhaust cooler 24 for example a fin type fan driven cooler, or other suitable cooler to reduce the temperature of the gases to a temperature suitable for compression, as for example cooling the exhaust gases from about 500 degrees to 90 degrees Fahrenheit.
- a conventional liquid/gas separator 26 for removing any liquid droplets that condense out of the exhaust when it is cooled. It may be either free standing or built into the exhaust cooler.
- a compressor 28 or other suitable pump with a low pressure inlet 30 and a high pressure outlet 18 . The compressor 28 should compress the exhaust gas to a sufficient pressure for cleaning a well, or such other application that the invention might be used for.
- the inert gas generator so described is mobile and may be taken from well site to well site.
- the engine supplies nitrogen rich, essentially oxygen free, but contaminated inert gas for use in well clean out operations.
- the gas processing system cleans the gas for use downhole.
- the resulting exhaust will be essentially oxygen free, with any remaining free oxygen captured by carbon monoxide to form carbon dioxide. Incorporation of other inert gases from the atmosphere besides nitrogen is acceptable.
- the water separator should separate out water droplets to avoid damage to the compressor, but need not render the exhaust stream free of water vapor.
- the exhaust stream may be 100% water saturated.
- the maximum preferred inlet temperature to the compressor is 10° F. above ambient.
- a preferred compressor is a Hurricane Compressor capable of pumping at 330 cubic feet per minute at 2000 psi.
- the compressor 28 pumps gas downhole for use in driving a downhole jet pump.
- the coil tubing 14 in this embodiment is formed of two strings of endless tubing running in the well simultaneously (one inside the other).
- FIG. 2 shows the inner tubing 40 and outer tubing 42 with an annulus 44 between them.
- the inner tubing 40 extends below the outer tubing 42 and has an opening 46 for the flow of downhole fluid, for example production hydrocarbons, into the inner tubing 40 .
- a venturi 48 is provided with an inlet 50 communicating with the annulus 44 and an outlet 52 communicating with the bore of the inner tubing 40 .
- the venturi 48 may be formed by a horizontal passageway 54 communicating with a vertical passageway 56 having a restriction 58 at the outlet 52 where the flow through the venturi enters the inner tubing 40 . Exhaust is pumped down the annulus 44 between the two strings 40 , 42 , through the venturi 48 and lifts well fluids up the inside string 40 . Such a system may be used to produce oil wells.
- jet pump By using a jet pump, the well need not be vented to atmosphere and would have to be taken off production to be cleaned out.
- jet pumps are known in the art in themselves, but the use of the exhaust system described would provide lower installation costs, quicker start up, less harm from sand to the pump and ready variation of production volumes from the well. This application is filed simultaneously with an application claiming the jet pump configuration.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Geology (AREA)
- Mining & Mineral Resources (AREA)
- Physics & Mathematics (AREA)
- Environmental & Geological Engineering (AREA)
- Fluid Mechanics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Exhaust Gas After Treatment (AREA)
Abstract
A wellsite inert gas injector, comprising an internal combustion engine, a gas processing system connected to receive low pressure exhaust gas from the internal combustion engine, a compressor within the gas processing system, the compressor having a low pressure inlet for receiving exhaust gases and the compressor having a high pressure outlet; and coil tubing connected to the high pressure outlet of the gas processing system. The gas processing system preferably comprises one or more of a particulate filter, exhaust cooler and exhaust separator in series, and in that order before the compressor.
Description
- This invention relates to equipment used for well clean out operations.
- Oil and gas wells and the equipment within them frequently become clogged with sand and other debris. Well clean out operations have been developed to remove the debris from the well. In one method, nitrogen is pumped down the well through coil tubing to dislodge the debris and allow it to be circulated up the well. Nitrogen is used because it is inert and does not damage the formation. However, nitrogen is expensive to obtain by conventional separation from air at a well site or by transporting it to a well site. This invention provides a method of providing inert nitrogen inexpensively at a well site for use in clean out operations.
- Cleaning out wells conventionally with a coiled tubing unit is accomplished by forcing compressed air/gas down the coiled tubing to the bottom of the well and returning the fluid/fill up the annulus between the coiled tubing and the wells original production casing. The fluids are carried up the annulus in slugs causing a pressure build-up in the lower portion of the well. This pressure build up may force fluids, fill, and air back into the producing zone, which may cause formation damage. Wells with production casing larger than four and one half inch are difficult to clean out due to reduced annular velocity of the compressed air. To clean a well out in this manner, the casing gas is vented to atmosphere through the entire job. This is expensive and not environmentally friendly. This invention provides an improved source of gas for use in treating wells.
- There is therefore provided in accordance with the invention a wellsite inert gas injector. The inert gas injector comprises an internal combustion engine, a gas processing system connected to receive low pressure exhaust gas from the internal combustion engine, a pump within the gas processing system, the pump having a low pressure inlet for receiving exhaust gases and the pump having a high pressure outlet; and coil tubing connected to the high pressure outlet of the gas processing system. The gas processing system preferably comprises one or more of a particulate filter, exhaust cooler and exhaust separator in series, and in that order before the pump. The pump may be a compressor. In one aspect of the invention, exhaust gas is supplied to a downhole jet pump to drive production fluid to surface.
- There will now be described preferred embodiments of the invention with reference to the drawings by way of illustration, and without intending to limit the generality of the claims, in which:
- FIG. 1 is a schematic showing an embodiment of the invention; and
- FIG. 2 is a schematic showing a down hole jet pump for use with an embodiment of the invention.
- In this patent document, “comprising” is used in its inclusive sense, and does not exclude other elements being present in the invention to which a claim refers. Use of the indefinite article “a” before an element of a claim means that at least one of the elements is present.
- A wellsite
inert gas injector 10 is preferably truck mounted as shown in the figure and utilizes exhaust from the truck's internal combustion engine 12 as source of inert gas. Preferably, the engine is a diesel engine. The exhaust is provided to coil tubing 14, which is mounted on thetruck deck 16 in conventional manner. A conventional connection (not shown) is used to connect theoutlet 18 to the coil tubing 14. Between the engine 12 andcoil tubing 18 is agas processing system 20 that is connected to receive low pressure exhaust gas from the internal combustion engine and provide high pressure inert gas to the coil tubing 14 throughoutlet 18. Low pressure and high pressure are relative terms. What matters is that gas at thehigh pressure outlet 18 has sufficient pressure for use down a well. - The
gas processing system 20 incorporates several modules to process the gas to make it suitable for downhole use. The modules are connected in series by conventional gas tight couplings. First, on the exhaust outlet of the engine 12, is a catalyticdiesel particulate filter 22, which may be one manufactured by Nett Technologies Inc. Details of the Nett diesel filter are available from Nett, and briefly described in the following. TheNett diesel filter 22 utilizes cordierite wall-flow monoliths to trap the soot produced by heavy-duty diesel engines. A cylindrical filter element in thefilter 22 has of many square parallel channels running in the axial direction, separated by thin porous walls. The channels are open at one end, but plugged at the other. Particulate laden exhaust gases are forced to flow through the porous walls. Gas is able to escape through the pores in the wall material. Particulates, however, are too large to escape and are trapped in the filter walls. A proprietary noble metal catalyst is coated onto the inside surface of the filter monolith. The catalyst lowers the soot combustion temperature to allow the filter to regenerate. The accumulated soot is oxidized in the filter during regular operation of the engine. Periods with exhaust temperatures of at least 350-400 degrees Fahrenheit are necessary for proper filter regeneration. However, so far as this invention is concerned in its broadest preferred aspect, a particulate filter is required to sufficiently clean the exhaust that the gas processing components are not damaged and the remaining particulate in the inert gas does not have a negative effect on the well. - Following the
filter 22 is anexhaust cooler 24, for example a fin type fan driven cooler, or other suitable cooler to reduce the temperature of the gases to a temperature suitable for compression, as for example cooling the exhaust gases from about 500 degrees to 90 degrees Fahrenheit. Following thecooler 24 is a conventional liquid/gas separator 26for removing any liquid droplets that condense out of the exhaust when it is cooled. It may be either free standing or built into the exhaust cooler. Following theseparator 26 is acompressor 28 or other suitable pump with a low pressure inlet 30 and ahigh pressure outlet 18. Thecompressor 28 should compress the exhaust gas to a sufficient pressure for cleaning a well, or such other application that the invention might be used for. - The inert gas generator so described is mobile and may be taken from well site to well site. At the well site, the engine supplies nitrogen rich, essentially oxygen free, but contaminated inert gas for use in well clean out operations. The gas processing system cleans the gas for use downhole.
- With an efficient internal combustion engine, it is expected that the resulting exhaust will be essentially oxygen free, with any remaining free oxygen captured by carbon monoxide to form carbon dioxide. Incorporation of other inert gases from the atmosphere besides nitrogen is acceptable. The water separator should separate out water droplets to avoid damage to the compressor, but need not render the exhaust stream free of water vapor. The exhaust stream may be 100% water saturated. The maximum preferred inlet temperature to the compressor is 10° F. above ambient. A preferred compressor is a Hurricane Compressor capable of pumping at 330 cubic feet per minute at 2000 psi.
- In another embodiment, the
compressor 28 pumps gas downhole for use in driving a downhole jet pump. The coil tubing 14 in this embodiment is formed of two strings of endless tubing running in the well simultaneously (one inside the other). FIG. 2 shows theinner tubing 40 and outer tubing 42 with anannulus 44 between them. Theinner tubing 40 extends below the outer tubing 42 and has anopening 46 for the flow of downhole fluid, for example production hydrocarbons, into theinner tubing 40. Aventuri 48 is provided with aninlet 50 communicating with theannulus 44 and an outlet 52 communicating with the bore of theinner tubing 40. Theventuri 48 may be formed by ahorizontal passageway 54 communicating with a vertical passageway 56 having a restriction 58 at the outlet 52 where the flow through the venturi enters theinner tubing 40. Exhaust is pumped down theannulus 44 between the twostrings 40, 42, through theventuri 48 and lifts well fluids up theinside string 40. Such a system may be used to produce oil wells. - By using a jet pump, the well need not be vented to atmosphere and would have to be taken off production to be cleaned out. Such jet pumps are known in the art in themselves, but the use of the exhaust system described would provide lower installation costs, quicker start up, less harm from sand to the pump and ready variation of production volumes from the well. This application is filed simultaneously with an application claiming the jet pump configuration.
- Immaterial modifications may be made to the invention described here without departing from the essence of the invention.
Claims (9)
1. A wellsite inert gas injector, comprising:
an internal combustion engine;
a gas processing system connected to receive low pressure exhaust gas from the internal combustion engine;
a pump within the gas processing system, the pump having a low pressure inlet for receiving exhaust gases and the pump having a high pressure outlet; and
coil tubing connected to the high pressure outlet of the gas processing system.
2. The wellsite inert gas generator of claim 1 in which the pump is a compressor and the gas processing system comprises an exhaust cooler.
3. The wellsite inert gas generator of claim 1 in which the pump is a compressor and the gas processing system comprises an exhaust separator.
4. The wellsite inert gas generator of claim 1 in which the pump is a compressor and the gas processing system comprises a particulate filter.
5. The wellsite inert gas generator of claim 1 in which the gas processing system comprises a particulate filter, exhaust cooler and exhaust separator in series, followed by a compressor.
6. The wellsite inert gas generator of claim 1 in which the pump is a compressor and the gas processing system comprises a particulate filter followed by an exhaust cooler and exhaust separator.
7. The wellsite inert gas generator of claim 6 in which the exhaust cooler is followed by the exhaust separator.
8. The wellsite inert gas generator of claim 1 in which the coiled tubing comprises:
a first tubing string connected to the high pressure outlet;
a second tubing string running parallel to the first tubing string and having an opening for entry of fluid at a remote end from the high pressure outlet; and
a venturi connecting the second tubing string to the first tubing string such that, in operation, passage of fluid through the venturi from the first tubing string draws production fluid into the second tubing string.
9. The wellsite inert gas generator of claim 8 in which the first tubing string is disposed within the second tubing string.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002339685A CA2339685A1 (en) | 2001-03-02 | 2001-03-02 | Wellsite inert gas generator |
US09/823,776 US20020139524A1 (en) | 2001-03-02 | 2001-03-29 | Wellsite inert gas generator |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002339685A CA2339685A1 (en) | 2001-03-02 | 2001-03-02 | Wellsite inert gas generator |
US09/823,776 US20020139524A1 (en) | 2001-03-02 | 2001-03-29 | Wellsite inert gas generator |
Publications (1)
Publication Number | Publication Date |
---|---|
US20020139524A1 true US20020139524A1 (en) | 2002-10-03 |
Family
ID=25682438
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US09/823,776 Abandoned US20020139524A1 (en) | 2001-03-02 | 2001-03-29 | Wellsite inert gas generator |
Country Status (2)
Country | Link |
---|---|
US (1) | US20020139524A1 (en) |
CA (1) | CA2339685A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20100038070A1 (en) * | 2008-08-12 | 2010-02-18 | Halliburton Energy Services, Inc. | Top suction fluid end |
WO2019070289A1 (en) * | 2017-10-05 | 2019-04-11 | Surgitech Inc. | Unique chemical delivery method for stimulating production in oil & gas wells |
CN112502688A (en) * | 2019-07-19 | 2021-03-16 | 廖文勇 | System and method for realizing mixed transportation and recovery of sleeve gas by multi-phase compression |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA2421376A1 (en) | 2003-03-07 | 2004-09-07 | Robert Joseph Foster | Hybrid coiled tubing/fluid pumping unit |
-
2001
- 2001-03-02 CA CA002339685A patent/CA2339685A1/en not_active Abandoned
- 2001-03-29 US US09/823,776 patent/US20020139524A1/en not_active Abandoned
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20100038070A1 (en) * | 2008-08-12 | 2010-02-18 | Halliburton Energy Services, Inc. | Top suction fluid end |
US8069923B2 (en) * | 2008-08-12 | 2011-12-06 | Halliburton Energy Services Inc. | Top suction fluid end |
WO2019070289A1 (en) * | 2017-10-05 | 2019-04-11 | Surgitech Inc. | Unique chemical delivery method for stimulating production in oil & gas wells |
CN112502688A (en) * | 2019-07-19 | 2021-03-16 | 廖文勇 | System and method for realizing mixed transportation and recovery of sleeve gas by multi-phase compression |
Also Published As
Publication number | Publication date |
---|---|
CA2339685A1 (en) | 2001-06-05 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: COIL-TECH SERVICES LTD., CANADA Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:ERICK, LEONARD LARRY;REEL/FRAME:011664/0501 Effective date: 20010314 |
|
STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |