CA2287732A1 - Portable flare knockout - Google Patents
Portable flare knockout Download PDFInfo
- Publication number
- CA2287732A1 CA2287732A1 CA002287732A CA2287732A CA2287732A1 CA 2287732 A1 CA2287732 A1 CA 2287732A1 CA 002287732 A CA002287732 A CA 002287732A CA 2287732 A CA2287732 A CA 2287732A CA 2287732 A1 CA2287732 A1 CA 2287732A1
- Authority
- CA
- Canada
- Prior art keywords
- vessel
- gas
- valve
- flare stack
- pressure vessel
- 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
- 239000012530 fluid Substances 0.000 claims abstract description 18
- 239000007788 liquid Substances 0.000 claims abstract description 17
- 230000003213 activating effect Effects 0.000 claims description 2
- 239000007789 gas Substances 0.000 abstract description 31
- 231100000518 lethal Toxicity 0.000 abstract description 2
- 230000001665 lethal effect Effects 0.000 abstract description 2
- 239000007791 liquid phase Substances 0.000 abstract description 2
- 230000001105 regulatory effect Effects 0.000 abstract description 2
- 239000007792 gaseous phase Substances 0.000 abstract 1
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 6
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000001294 propane Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000011521 glass Substances 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
- 238000012544 monitoring process Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000012354 overpressurization Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 238000011179 visual inspection Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/08—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases using flares, e.g. in stacks
- F23G7/085—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases using flares, e.g. in stacks in stacks
-
- 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
- E21B41/00—Equipment or details not covered by groups E21B15/00 - E21B40/00
- E21B41/005—Waste disposal systems
- E21B41/0071—Adaptation of flares, e.g. arrangements of flares in offshore installations
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/50—Control or safety arrangements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/60—Separating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2203/00—Furnace arrangements
- F23G2203/60—Mobile furnace
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N2225/00—Measuring
- F23N2225/04—Measuring pressure
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Mining & Mineral Resources (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
The invention provides for a method of depressurizing a blocked pipeline at a producing well site. The invention permits depressurization in a vapour-tight manner and facilitates the disposal of any fluids and lethal gases present. In accordance with this method, there is provided a portable vapour-tight depressurizing apparatus with a pressure vessel and flare stack for incinerating gases, all mounted on a portable trailer. The pressure vessel is connected to the pipeline by means of a flow line at the blow down point. Incoming fluids are directed to the vessel where the pressurized fluid separates into liquid and gaseous phases.
The fluids are removed from the vessel through a liquid outlet. The gas is removed through a gas outlet. The gas outlet leads to flare stack where the gas is incinerated. Fluid and gas flow is regulated by a number of sensors and control valves.
The fluids are removed from the vessel through a liquid outlet. The gas is removed through a gas outlet. The gas outlet leads to flare stack where the gas is incinerated. Fluid and gas flow is regulated by a number of sensors and control valves.
Description
CANADIAN PATENT
Docket No. 12608-001 PORTABLE FLARE KNOCKOUT
FIELD OF THE INVENTION
The present invention relates to a portable depressurizing and gas flaring apparatus for vapour tight applications, which may be referred to as a portable flare knockout.
BACKGROUND OF THE INVENTION
Pipelines which carry oil and/gas from a producing wellsite sometimes become blocked with hydrate or water and require depressurizing, referred to as "blow down", so as to dehydrate or deice the blockage with methanol to bring the pipeline back on stream.
There is a need in the art for an apparatus which may be used to depressurize a blocked pipeline in a vapour-tight manner and dispose of any fluids including any lethal or poisonous gases which may be present. The apparatus may also be useful in providing a flaring system for use at the wellhead.
SUMMARY OF THE INVENTION
The present invention is directed to a portable vapour-tight depressurizing apparatus with a pressure vessel and a flare stack for capturing and incinerating gases from a wellhead or a pipeline.
Accordingly, in one aspect of the invention, the invention comprises an apparatus comprising:
(a) a portable platform;
(b) a pressure vessel mounted on the platform, said vessel comprising a fluid inlet, a liquid outlet, a gas outlet and a gas sensor;
(c) an inlet line including a shut-off valve;
(d) control means for activating the shut-off valve, said control means operatively connected to the shut-off valve and the gas sensor; and (e) a flare stack connected to the gas outlet of the pressure vessel by a gas outlet line.
In one embodiment, the vessel further comprises a liquid sensor which is operatively connected to the control means. The vessel may further comprise a phase separator disposed in the flow path of the fluid inlet of the pressure vessel. The flare stack may be pivotally mounted to the platform and moveable between a horizontal position and a vertical position.
The pressure vessel may be an elongate cylindrical vapour-tight vessel. The control means is operative to close the shut-off valve upon receiving a signal from the gas sensor that the gas pressure within the vessel has reached a pre-determined level.
BRIEF DESCRIPTION OF THE DRAWINGS
The invention will now be described by way of an exemplary embodiment with reference to the accompanying simplified, diagrammatic, not-to-scale drawings.
In the drawings:
Figure 1 is a schematic depiction of an embodiment of the apparatus.
Figure 2 is a side view of an embodiment including a trailer.
Figure 3 is a schematic view of an embodiment.
Docket No. 12608-001 PORTABLE FLARE KNOCKOUT
FIELD OF THE INVENTION
The present invention relates to a portable depressurizing and gas flaring apparatus for vapour tight applications, which may be referred to as a portable flare knockout.
BACKGROUND OF THE INVENTION
Pipelines which carry oil and/gas from a producing wellsite sometimes become blocked with hydrate or water and require depressurizing, referred to as "blow down", so as to dehydrate or deice the blockage with methanol to bring the pipeline back on stream.
There is a need in the art for an apparatus which may be used to depressurize a blocked pipeline in a vapour-tight manner and dispose of any fluids including any lethal or poisonous gases which may be present. The apparatus may also be useful in providing a flaring system for use at the wellhead.
SUMMARY OF THE INVENTION
The present invention is directed to a portable vapour-tight depressurizing apparatus with a pressure vessel and a flare stack for capturing and incinerating gases from a wellhead or a pipeline.
Accordingly, in one aspect of the invention, the invention comprises an apparatus comprising:
(a) a portable platform;
(b) a pressure vessel mounted on the platform, said vessel comprising a fluid inlet, a liquid outlet, a gas outlet and a gas sensor;
(c) an inlet line including a shut-off valve;
(d) control means for activating the shut-off valve, said control means operatively connected to the shut-off valve and the gas sensor; and (e) a flare stack connected to the gas outlet of the pressure vessel by a gas outlet line.
In one embodiment, the vessel further comprises a liquid sensor which is operatively connected to the control means. The vessel may further comprise a phase separator disposed in the flow path of the fluid inlet of the pressure vessel. The flare stack may be pivotally mounted to the platform and moveable between a horizontal position and a vertical position.
The pressure vessel may be an elongate cylindrical vapour-tight vessel. The control means is operative to close the shut-off valve upon receiving a signal from the gas sensor that the gas pressure within the vessel has reached a pre-determined level.
BRIEF DESCRIPTION OF THE DRAWINGS
The invention will now be described by way of an exemplary embodiment with reference to the accompanying simplified, diagrammatic, not-to-scale drawings.
In the drawings:
Figure 1 is a schematic depiction of an embodiment of the apparatus.
Figure 2 is a side view of an embodiment including a trailer.
Figure 3 is a schematic view of an embodiment.
DETAILED DESCRIPTION OF AN EMBODIMENT OF THE INVENTION
The present invention provides for a portable depressurizing unit for vapour tight applications that recovers and combusts any gases accumulated in the depressurizing operation.
The apparatus (10) according to the Figures comprises a trailer (12) which has mounted onto it a flare stack (30) and a pressure vessel (50). The pressure vessel (50) is mounted on some vessel supports (14) and includes a fluid inlet (52), a gas outlet (56), a liquid outlet (58). In basic operation, pressurized fluid consisting of liquids and gases enters the fluid inlet (52) and separates into a liquid phase which settles to the bottom of the vessel and a gas phase. A wedge demister (54) or other device which aids in phase separation may be placed in the path of the incoming fluid stream. The accumulated liquid may be withdrawn through the liquid outlet (58) and the liquid outlet valve (59). The gas may be withdrawn through the gas outlet (56), the gas outlet valve (57) and into the flare stack (30) where it may be disposed of by combustion.
Flow line (70) to be used in connecting the vessel to the fluid source is stored and transported on the trailer ( 12) on flow line racks (20) which are mounted to the trailer ( 12) as is shown in Figure 2.
The flare stack (30) comprises a main stack (32) of an appropriate length which has a drain valve (33) at the bottom end thereof. The flare stack (30) mounts to a pivot (34) which is mounted to a flare stack pivot support ( 16) which is rigidly attached to the trailer ( 12). When being transported to the work site, the flare stack (30) may be pivoted downwards to be in a substantially horizontal position as is shown in Figure 2, where it rests on a flare stack travelling cradle (18). The flare stack may then be raised to its operative vertical position by a winch (24) which has a cable (26) attached to the lower end of the flare stack by a snatch block (36). The top end of the flare stack is a burner (40), an igniter (44) and a pilot light and line (42). The pilot line carries propane gas from propane bottles (23) carned on racks (22) on the trailer (12). The igniter (44) includes a shot tube (45) which is closed at the bottom and has a meshed opening at the top. A flare within the shot tube may be used to ignite the pilot light.
Alternatively, the shot tube may be lowered to manually place a flame on the igniter and then raised into position to ignite the pilot.
The vessel (50) includes an access hatch (60) to allow visual inspection of the vessel and its components.
Incoming fluids are directed to the vessel (50) by the flow line (70) and may be regulated by a manual shut-off valve (76) and an automatic shut-off valve (78) controlled by gas and liquid sensors in the vessel. A liquid level sensor and gauge (62, 66) may activate the valve (78) in response to a high level of liquid within the vessel. A gas pressure sensor and gauge (64) may also activate closure of the valve (78) by control means (79) which are well known in the art, in response to gas pressures within the vessel (50) in excess of a predetermined level. Optionally, a one-way check valve (80) may be provided to prevent backflow of fluid through the flow line (70) The pressure vessel (50) includes a fail-safe pressure safety relief valve (68) which automatically releases gas to the flare stack and burner by safety relief line (46). These safety valves are well-known in the art and may be set to open at a pre-determined pressure to prevent overpressurization in the vessel (50).
A pressure gauge (69) may be prominently mounted to the vessel allowing for the operator to visually monitor the pressure within the vessel (50).
All piping should be connected by hammer unions which have a high pressure rating. All materials used should preferably have corrosion allowance where it is known that the apparatus ( 10) will be used in a corrosive environment.
The present invention provides for a portable depressurizing unit for vapour tight applications that recovers and combusts any gases accumulated in the depressurizing operation.
The apparatus (10) according to the Figures comprises a trailer (12) which has mounted onto it a flare stack (30) and a pressure vessel (50). The pressure vessel (50) is mounted on some vessel supports (14) and includes a fluid inlet (52), a gas outlet (56), a liquid outlet (58). In basic operation, pressurized fluid consisting of liquids and gases enters the fluid inlet (52) and separates into a liquid phase which settles to the bottom of the vessel and a gas phase. A wedge demister (54) or other device which aids in phase separation may be placed in the path of the incoming fluid stream. The accumulated liquid may be withdrawn through the liquid outlet (58) and the liquid outlet valve (59). The gas may be withdrawn through the gas outlet (56), the gas outlet valve (57) and into the flare stack (30) where it may be disposed of by combustion.
Flow line (70) to be used in connecting the vessel to the fluid source is stored and transported on the trailer ( 12) on flow line racks (20) which are mounted to the trailer ( 12) as is shown in Figure 2.
The flare stack (30) comprises a main stack (32) of an appropriate length which has a drain valve (33) at the bottom end thereof. The flare stack (30) mounts to a pivot (34) which is mounted to a flare stack pivot support ( 16) which is rigidly attached to the trailer ( 12). When being transported to the work site, the flare stack (30) may be pivoted downwards to be in a substantially horizontal position as is shown in Figure 2, where it rests on a flare stack travelling cradle (18). The flare stack may then be raised to its operative vertical position by a winch (24) which has a cable (26) attached to the lower end of the flare stack by a snatch block (36). The top end of the flare stack is a burner (40), an igniter (44) and a pilot light and line (42). The pilot line carries propane gas from propane bottles (23) carned on racks (22) on the trailer (12). The igniter (44) includes a shot tube (45) which is closed at the bottom and has a meshed opening at the top. A flare within the shot tube may be used to ignite the pilot light.
Alternatively, the shot tube may be lowered to manually place a flame on the igniter and then raised into position to ignite the pilot.
The vessel (50) includes an access hatch (60) to allow visual inspection of the vessel and its components.
Incoming fluids are directed to the vessel (50) by the flow line (70) and may be regulated by a manual shut-off valve (76) and an automatic shut-off valve (78) controlled by gas and liquid sensors in the vessel. A liquid level sensor and gauge (62, 66) may activate the valve (78) in response to a high level of liquid within the vessel. A gas pressure sensor and gauge (64) may also activate closure of the valve (78) by control means (79) which are well known in the art, in response to gas pressures within the vessel (50) in excess of a predetermined level. Optionally, a one-way check valve (80) may be provided to prevent backflow of fluid through the flow line (70) The pressure vessel (50) includes a fail-safe pressure safety relief valve (68) which automatically releases gas to the flare stack and burner by safety relief line (46). These safety valves are well-known in the art and may be set to open at a pre-determined pressure to prevent overpressurization in the vessel (50).
A pressure gauge (69) may be prominently mounted to the vessel allowing for the operator to visually monitor the pressure within the vessel (50).
All piping should be connected by hammer unions which have a high pressure rating. All materials used should preferably have corrosion allowance where it is known that the apparatus ( 10) will be used in a corrosive environment.
In operation, the apparatus (10) is towed or otherwise transported to an area close to the affected site and set up on level ground. Preferably, the location should be a safe distance from the wellhead or source of flow and chosen with prevailing winds in mind. The trailer (12) may be stabilized with jacks (not shown). The apparatus may be grounded using a ground rod and electrical ground cable (not shown). The winch (24) may then be used to elevate the flare stack (30) to its vertical operative position. The connecting spool (38) may then be connected between the vessel and the flare, completing the connection between the gas outlet (56) and the safety relief valve to the flare stack (30).
The connection to the wellhead or pipeline is made at the blowdown point (72) with an adjustable choke (74) which is rigged in directly off source of flow connection. Flow line (70) is then rigged to the choke from the manual valve (76). Fluid dump line (not shown) is rigged to the liquid outlet valve (59) to the liquid storage tank (not shown). A ammonia scrubber (not shown) should be used if the liquid is degassing to the atmosphere.
The entire system should be purged of oxygen as the failure to do so may cause explosion. Also, the sight glasses (not shown) should be prepared for use using a hand-held pump such as a Baker pump.
The vessel may then be pressurized to a low level by opening the manual choke (74) and the valve (76) and the burner (40) ignited using the pilot and ignitor (44).
The depressurizing operation may then be continuously operated by operating the manual choke (74) while monitoring the pressure and level gauges (62, 64, 66, 69) When rigging out, the vessel should be purged with propane or nitrogen to eliminate any residual sour gas. All liquids should be emptied from the vessel (50). The operator should confirm that the flare is extinguished. It is preferably that the flowline into the vessel is flushed with water after disconnection from the source and the water in the vessel flushed back out.
After lowering the flare stack onto the travelling cradle (18), it should be secured. All pipe or flow line (70) should be racked and secured.
The connection to the wellhead or pipeline is made at the blowdown point (72) with an adjustable choke (74) which is rigged in directly off source of flow connection. Flow line (70) is then rigged to the choke from the manual valve (76). Fluid dump line (not shown) is rigged to the liquid outlet valve (59) to the liquid storage tank (not shown). A ammonia scrubber (not shown) should be used if the liquid is degassing to the atmosphere.
The entire system should be purged of oxygen as the failure to do so may cause explosion. Also, the sight glasses (not shown) should be prepared for use using a hand-held pump such as a Baker pump.
The vessel may then be pressurized to a low level by opening the manual choke (74) and the valve (76) and the burner (40) ignited using the pilot and ignitor (44).
The depressurizing operation may then be continuously operated by operating the manual choke (74) while monitoring the pressure and level gauges (62, 64, 66, 69) When rigging out, the vessel should be purged with propane or nitrogen to eliminate any residual sour gas. All liquids should be emptied from the vessel (50). The operator should confirm that the flare is extinguished. It is preferably that the flowline into the vessel is flushed with water after disconnection from the source and the water in the vessel flushed back out.
After lowering the flare stack onto the travelling cradle (18), it should be secured. All pipe or flow line (70) should be racked and secured.
As will be apparent to those skilled in the art, various modifications, adaptations and variations of the foregoing specific disclosure can be made without departing from the scope of the invention claimed herein.
Claims (6)
1. An apparatus comprising:
(a) a portable platform;
(b) a pressure vessel mounted on the platform, said vessel comprising a fluid inlet, a liquid outlet, a gas outlet and a gas sensor;
(c) an inlet line including a shut-off valve;
(d) control means for activating the shut-off valve, said control means operatively connected to the shut-off valve and the gas sensor; and (e) a flare stack connected to the gas outlet of the pressure vessel by a gas outlet line.
(a) a portable platform;
(b) a pressure vessel mounted on the platform, said vessel comprising a fluid inlet, a liquid outlet, a gas outlet and a gas sensor;
(c) an inlet line including a shut-off valve;
(d) control means for activating the shut-off valve, said control means operatively connected to the shut-off valve and the gas sensor; and (e) a flare stack connected to the gas outlet of the pressure vessel by a gas outlet line.
2. The apparatus of claim wherein the vessel further comprises a liquid sensor which is operatively connected to the control means.
3. The apparatus of claim 1 further comprising a phase separator disposed in the flow path of the fluid inlet of the pressure vessel.
4. The apparatus of claim 1 or claim 2 wherein the flare stack is pivotally mounted to the platform and moveable between a horizontal position and a vertical position.
5. The apparatus of claim 1 or claim 2 wherein the pressure vessel is an elongate cylindrical vapour-tight vessel.
6. The apparatus of claim 1 wherein the control means is operative to close the shut-off valve upon receiving a signal from the gas sensor that the gas pressure within the vessel has reached a pre-determined level.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002287732A CA2287732A1 (en) | 1999-10-28 | 1999-10-28 | Portable flare knockout |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002287732A CA2287732A1 (en) | 1999-10-28 | 1999-10-28 | Portable flare knockout |
Publications (1)
Publication Number | Publication Date |
---|---|
CA2287732A1 true CA2287732A1 (en) | 2001-04-28 |
Family
ID=4164506
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002287732A Abandoned CA2287732A1 (en) | 1999-10-28 | 1999-10-28 | Portable flare knockout |
Country Status (1)
Country | Link |
---|---|
CA (1) | CA2287732A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7677883B2 (en) * | 2006-04-04 | 2010-03-16 | Expro Americas, Llc | Trailer mounted smokeless dual-phase burner system |
US7677882B2 (en) | 2006-04-04 | 2010-03-16 | Expro Americas, Llc | Smokeless liquid dual-phase burner system |
-
1999
- 1999-10-28 CA CA002287732A patent/CA2287732A1/en not_active Abandoned
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7677883B2 (en) * | 2006-04-04 | 2010-03-16 | Expro Americas, Llc | Trailer mounted smokeless dual-phase burner system |
US7677882B2 (en) | 2006-04-04 | 2010-03-16 | Expro Americas, Llc | Smokeless liquid dual-phase burner system |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EEER | Examination request | ||
FZDE | Dead |