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US3331194A - Flare stack structure and apparatus treating and controlling flow of gases to and from stack - Google Patents

Flare stack structure and apparatus treating and controlling flow of gases to and from stack Download PDF

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Publication number
US3331194A
US3331194A US512493A US51249365A US3331194A US 3331194 A US3331194 A US 3331194A US 512493 A US512493 A US 512493A US 51249365 A US51249365 A US 51249365A US 3331194 A US3331194 A US 3331194A
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Prior art keywords
housing
stack
gas
partition wall
tubular member
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US512493A
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Robert D Reed
Zink John Smith
Goodnight Hershel
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Zinklahoma Inc
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John Zink Co
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Priority to US512493A priority Critical patent/US3331194A/en
Priority to GB3688866A priority patent/GB1158401A/en
Priority to DE19661545316 priority patent/DE1545316A1/en
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Publication of US3331194A publication Critical patent/US3331194A/en
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    • 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

Definitions

  • the present invention relates to a flare stack and the base structure thereof for venting gases such as hydrocarbons or inflammable gaseous materials to the atmosphere and which are usually burned at the upper end of the stack and to apparatus for removing liquids from such gases prior to delivering into the lower end of the stack and to apparatus for preventing reverse flow of gas from the stack.
  • vent stacks which extend into the atmosphere to significant elevations above the surrounding terrain for the disposal of dump gases.
  • the upper end of such stacks are usually provided with burner elements for combustion of the gases.
  • Liquids are often present in the gases which are to be discharged into the stack.
  • High boiling point liquids are often vented through such stacks and in the gaseous phase which condense when cooled within the stack structure.
  • Such liquids are often highly inflammable and the equipment must serve to prevent such liquids from being vented to atmosphere. It is accordingly one of the objects of the present invention to provide a base structure for a vent stack which houses means separating liquids from a liquid laden dump gas as it moves through such means and before the dump gas arrives in the lower end stack.
  • the gas being vented therethrough usually has a temperature above ambient temperatures.
  • the apparatus is filled with hot gas. Some portions decant from the stack to atmosphere.
  • the stack structure cools and the volume of gas remaining in the stack is reduced.
  • These conditions develop pressures in the stack system which are below atmospheric pressure promoting an upstream or downward movement of air in the stack assembly. It is another object of the invention to provide means housed in and forming a part of the base structure of the stack preventing upstream movement of atmospheric air in the stack structure beyond a given zone therein.
  • Another object of the invention is to provide means for controlling the flow of gas Within the base structure of a vent stack assembly which distributes the dump gas below the level of water or liquid whereby the dump gas bubbles upwardly through the liquid such as a column of water which is of such height as to prevent rearward movement of atmospheric air or upstream propagation of a flame through the apparatus.
  • FIG. 1 is a sectional view of the base structure of a vent stack and apparatus for handling gases admitted to the lower end of the stack.
  • FIG. 2 is a transverse plan sectional view taken on the line 22 of FIG. 1.
  • FIG. 3 is a similar transverse sectional view taken on the line 3-3 of FIG. 1.
  • FIG. 4 is a fragmentary sectional view taken on the line 44 of FIG. 1.
  • FIG. 1 There is shown in FIG. 1 a tube 10 which is adapted to be erected in a substantially vertical position with the upper end positioned above adjacent buildings and at a significant level above the surrounding terrain.
  • the tube 10 may be formed of sections and the stack structure may be of any desired height.
  • the tube 10 forms a vent or flare stack through which dump gases are guided to the uper end thereof.
  • a burner tip is often mounted on the upper end of the tube 10 to provide for the combustion of the gases high in the atmosphere.
  • the tube 10 is supported by and extends upwardly from a housing 11 which is of larger cross sectional dimensions than the stack and the housing 11 serves as a Wide base for the tube 10.
  • the lower end of the housing is supported on a footing 12 having a substantially horizontal upper surface 14.
  • the housing 11 encases equipment for treating and controlling the flow of gas to the stack and this auxiliary equipment is also supported by the housing on the footing 12.
  • the housing 11 may be of cylindrical shape and a bottom wall 17 closes the lower end thereof.
  • the bottom wall 17 has a concave inner upper face as shown in FIG. 1 and a drain conduit 18 equipped with a valve 19 is provided for removing liquid from the lower portion of the housing 11.
  • the inner end portion 21 of the conduit 18 extends above the bottom wall 17.
  • a partition wall 22 is disposed transversely of the housing 11 and the perimeter thereof is attached to the cylindrical wall of 'the housing 11 in a sealed relationship.
  • a cylindrical baffle 23 of smaller diameter than the housing 11 depends from the partition wall 22 to provide an annular space 24 between the circumference of the baffle 23 and the annular wall of the housing 11.
  • a pipe 26 carried by the housing serves as an inlet for the gas.
  • the axis of the pipe 26 is disposed tangentially of the housing 11.
  • the liquid laden dump gas enters the housing in a tangential relationship with respect to the bafile 23.
  • the dump gas is delivered to the annular space 24 at velocities which range from about fifty feet per second to about two hundred feet per second and at static pressures ranging from approximately 0.10 to about 25 pounds per square inch.
  • the liquid laden dump gas moves circumferentially Within the annular space 24 as indicated by the arrows in FIG. 2. Centrifugal force is thus developed which acts on the droplets of liquid.
  • the liquid components move radially outwardly into engagement with the inner annular surface of the housing 11.
  • the droplets of liquid on the inner surface of the cylindrical wall of the housing 11 flow downwardly and are collected within the housing above the wall 17.
  • the velocity energy of the incoming gas is virtually spent as the gaseous components with most of the liquid removed escapes through the lower end of the annular space 24.
  • any residual liquid retained in the gas as it escapes through the lower end of the annular space 24 is directed towards liquid accumulated and retained within the lower part of the housing where due to impact of any residual liquid droplets on the surface of the liquid body 27 insures substantially complete removal of the liquid from the gas.
  • the extension 21 of the conduit 18 within the housing 11 insures that there will always be some liquid retained within the housing. The liquid removed from the gas when inflammable is safely collected in the lower portion of the housing 11 below the partition wall 22.
  • the gas substantially free of liquid turns upwardly and enters the interior of the bafile 23.
  • the partition Wall 22 has a concave under surface.
  • a cylindrical shaped flange 28 depends from the partition wall 22 adjacent the axis of the housing 11- and in surrounding relationship to an exit opening 30. Any liquid particles remaining in the gas engages the exterior of the flange 28 to drop therefrom into the lower end of the housing and into the body of liquid 27.
  • a tubular element 29 is connected to the partition wall 22 and extends upwardly therefrom. This tubular element registers with the opening 30 and guides the gas upwardly through a body of water or liquid and above its static level 31.
  • An inverted cup-shaped member 32 is supported within the housing 11 above the impervious partition wall 22 by means of a tubular member 33 which is of larger diameter than the tubular element 29.
  • a plurality of radially disposed arms 34 support the tubular member 33 on the tubular element 29.
  • the upper end of the tubular member 33 is closed by means of an end wall 35.
  • An annular passage 36 is thereby provided between the exterior of the tubular element 29 and the interior of the tubular member 33.
  • a dispersion unit 37 mounted under the inverted cup-shaped member 32 is provided with radially disposed vanes 38 as best shown in FIG. 4 to distribute the gas throughout substantially all sectors of the inverted cupshaped member 32.
  • the liquid maintained within the housing 11 above the partition wall 22 has a static level at 31 and the horizontal disc 42 of the inverted cup-shaped member 32 is positioned below the surface of the water.
  • the disc 42 is provided with ports 43 which are spaced from each other throughout the area of the horizontally disposed disc 42 which provide for the escape of the gas as bubbles moving upwardly through the liquid.
  • the gas bubbles through the liquid and moves into the upper portion of the housing 11.
  • a depending flange 44 on the inverted cup-shaped member 32 housing 11 to provide an annular space 46 between the interior of the housing 11 and the exterior of the flange 44. If there is a sudden increase in the volume of gas delivered through the tubular element 29 the excess gas escapes through the annular space 46 which then serves as an emergency spill area.
  • a conical shaped housing member 47 connects the upper end of the cylindrical housing 11 with the lower end of the tube whereby the gas is guided into the lower end of the stack.
  • a cylindrical shaped baffle 48 is supported within the conical housing member 47 in sealed relationship with respect to the conical wall. Any water particles that may be carried upwardly with the gas along the inner surface of the member 47 engages the exterior of the baffle 48 and drains back into the body of water to maintain the static level 31. The gas moves into the lower end of the stack.
  • the structure above the partition wall 22 serves to prevent atmospheric air which may settle in the tube 10 from moving rearwardly beyond the upper end of the tubular element 29 and into the presence of inflammable liquid collected in the lower portion of the housing 11.
  • the vertical dimension indicated at X represents the height of a water column greater than atmospheric pressure so that it is impossible for air or a flame to propagate rearwardly through the apparatus beyond the free end of the tubular element 29.
  • a base structure for a vent stack for treating gas moving towards the stack and preventing rearward movement of gas from the stack through the base structure comprising, a vertically disposed vent stack, a generally cylindrical shaped housing of larger cross sectional dimensions than the stack supporting and providing a base therefor, a bottom wall within said housing, a partition wall within the housing spaced upwardly from said bottom wall, a generally cylindrical shaped baflle depending from said partition wall providing an annular space between the perimeter thereof and the interior of said housing, an
  • inlet pipe disposed to guide gas tangentially into said annular space
  • said partition wall having an opening therethrough within said baflle
  • a tubular element carried by the partition wall extending upwardly therefrom within said housing
  • said partition wall and said housing providing a receptacle containing a body of liquid within the housing having a static level below the upper end of said tubular element
  • a tubular member surrounding said tubular element providing an annular passage between the perimeter of the tubular element and the interior of the tubular member, means closing the upper end of said tubular member
  • means supporting the tubular member on said tubular element a substantially horizontal disc supported by said tubular member below the static level of said liquid, said disc having spaced ports therethrough
  • dispersion unit means provided with a plurality of radially disposed vanes at the lower end of said tubular member for dispersing gas from said annular passages throughout the underside of said disc, an annular flange depending from said disc having a diameter smaller than said housing providing an annular space between said f

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  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Gas Separation By Absorption (AREA)

Description

3,331,194 AND STACK y 18, 1967 R. D. REED ETAL FLARE STACK STRUCTURE AND APPARATUS TREATING CONTROLLING FLOW OF GASES TO AND FROM Filed Dec. 8, 1965 7 W W: \3 m: x 4 :TL 3 5 mm fl w 2 E F M BF 2 F T w J j M 4 3 A i x mm \l E 0K7 FNH $5.0m H m M M m mafim n 5 6 E L w R 05 J y H B United States Patent FLARE STACK STRUCTURE AND APPARATUS TREATING AND CONTROLLING FLQW 0F GASES TO AND FROM STACK Robert D. Reed, John Smith Zink, and Hershel Goodnight, Tulsa, Olrlan, assignors to John Zink Company,
Tulsa, Okla, a corporation of Delaware Filed Dec. 8, 1965, Ser. No. 512,493 2 Claims. (Cl. 55-235) The present invention relates to a flare stack and the base structure thereof for venting gases such as hydrocarbons or inflammable gaseous materials to the atmosphere and which are usually burned at the upper end of the stack and to apparatus for removing liquids from such gases prior to delivering into the lower end of the stack and to apparatus for preventing reverse flow of gas from the stack.
It is a practice in process industries to provide vent stacks which extend into the atmosphere to significant elevations above the surrounding terrain for the disposal of dump gases. The upper end of such stacks are usually provided with burner elements for combustion of the gases. Liquids are often present in the gases which are to be discharged into the stack. High boiling point liquids are often vented through such stacks and in the gaseous phase which condense when cooled within the stack structure. Such liquids are often highly inflammable and the equipment must serve to prevent such liquids from being vented to atmosphere. It is accordingly one of the objects of the present invention to provide a base structure for a vent stack which houses means separating liquids from a liquid laden dump gas as it moves through such means and before the dump gas arrives in the lower end stack.
In the operation of a flare stack the gas being vented therethrough usually has a temperature above ambient temperatures. When the flow of the dump gases being fed to the stack is interrupted the aparatus is filled with hot gas. Some portions decant from the stack to atmosphere. The stack structure cools and the volume of gas remaining in the stack is reduced. These conditions develop pressures in the stack system which are below atmospheric pressure promoting an upstream or downward movement of air in the stack assembly. It is another object of the invention to provide means housed in and forming a part of the base structure of the stack preventing upstream movement of atmospheric air in the stack structure beyond a given zone therein.
Another object of the invention is to provide means for controlling the flow of gas Within the base structure of a vent stack assembly which distributes the dump gas below the level of water or liquid whereby the dump gas bubbles upwardly through the liquid such as a column of water which is of such height as to prevent rearward movement of atmospheric air or upstream propagation of a flame through the apparatus.
Other objects and features of the invention will be appreciated and become apparent as the present disclosure proceeds and upon consideration of the following detailed description taken in conjunction with the annexed drawing wherein an embodiment of the invention is disclosed.
In the drawing:
FIG. 1 is a sectional view of the base structure of a vent stack and apparatus for handling gases admitted to the lower end of the stack.
FIG. 2 is a transverse plan sectional view taken on the line 22 of FIG. 1.
FIG. 3 is a similar transverse sectional view taken on the line 3-3 of FIG. 1.
FIG. 4 is a fragmentary sectional view taken on the line 44 of FIG. 1.
ice
There is shown in FIG. 1 a tube 10 which is adapted to be erected in a substantially vertical position with the upper end positioned above adjacent buildings and at a significant level above the surrounding terrain. The tube 10 may be formed of sections and the stack structure may be of any desired height. The tube 10 forms a vent or flare stack through which dump gases are guided to the uper end thereof. A burner tip is often mounted on the upper end of the tube 10 to provide for the combustion of the gases high in the atmosphere. The tube 10 is supported by and extends upwardly from a housing 11 which is of larger cross sectional dimensions than the stack and the housing 11 serves as a Wide base for the tube 10. The lower end of the housing is supported on a footing 12 having a substantially horizontal upper surface 14. The housing 11 encases equipment for treating and controlling the flow of gas to the stack and this auxiliary equipment is also supported by the housing on the footing 12.
The housing 11 may be of cylindrical shape and a bottom wall 17 closes the lower end thereof. The bottom wall 17 has a concave inner upper face as shown in FIG. 1 and a drain conduit 18 equipped with a valve 19 is provided for removing liquid from the lower portion of the housing 11. The inner end portion 21 of the conduit 18 extends above the bottom wall 17. A partition wall 22 is disposed transversely of the housing 11 and the perimeter thereof is attached to the cylindrical wall of 'the housing 11 in a sealed relationship. A cylindrical baffle 23 of smaller diameter than the housing 11 depends from the partition wall 22 to provide an annular space 24 between the circumference of the baffle 23 and the annular wall of the housing 11. A pipe 26 carried by the housing serves as an inlet for the gas. The axis of the pipe 26 is disposed tangentially of the housing 11. The liquid laden dump gas enters the housing in a tangential relationship with respect to the bafile 23. The dump gas is delivered to the annular space 24 at velocities which range from about fifty feet per second to about two hundred feet per second and at static pressures ranging from approximately 0.10 to about 25 pounds per square inch.
The liquid laden dump gas moves circumferentially Within the annular space 24 as indicated by the arrows in FIG. 2. Centrifugal force is thus developed which acts on the droplets of liquid. The liquid components move radially outwardly into engagement with the inner annular surface of the housing 11. The droplets of liquid on the inner surface of the cylindrical wall of the housing 11 flow downwardly and are collected within the housing above the wall 17. The velocity energy of the incoming gas is virtually spent as the gaseous components with most of the liquid removed escapes through the lower end of the annular space 24.
Any residual liquid retained in the gas as it escapes through the lower end of the annular space 24 is directed towards liquid accumulated and retained within the lower part of the housing where due to impact of any residual liquid droplets on the surface of the liquid body 27 insures substantially complete removal of the liquid from the gas. The extension 21 of the conduit 18 within the housing 11 insures that there will always be some liquid retained within the housing. The liquid removed from the gas when inflammable is safely collected in the lower portion of the housing 11 below the partition wall 22.
The gas substantially free of liquid turns upwardly and enters the interior of the bafile 23. The partition Wall 22 has a concave under surface. A cylindrical shaped flange 28 depends from the partition wall 22 adjacent the axis of the housing 11- and in surrounding relationship to an exit opening 30. Any liquid particles remaining in the gas engages the exterior of the flange 28 to drop therefrom into the lower end of the housing and into the body of liquid 27.
A tubular element 29 is connected to the partition wall 22 and extends upwardly therefrom. This tubular element registers with the opening 30 and guides the gas upwardly through a body of water or liquid and above its static level 31. An inverted cup-shaped member 32 is supported within the housing 11 above the impervious partition wall 22 by means of a tubular member 33 which is of larger diameter than the tubular element 29. A plurality of radially disposed arms 34 support the tubular member 33 on the tubular element 29. The upper end of the tubular member 33 is closed by means of an end wall 35. An annular passage 36 is thereby provided between the exterior of the tubular element 29 and the interior of the tubular member 33. Thus the gas virtually free of liquid after moving upwardly within the tubular element 29 turns and moves downwardly in the annular passage 36 to escape under the inverted cup-shaped member 32. A dispersion unit 37 mounted under the inverted cup-shaped member 32 is provided with radially disposed vanes 38 as best shown in FIG. 4 to distribute the gas throughout substantially all sectors of the inverted cupshaped member 32.
The liquid maintained within the housing 11 above the partition wall 22 has a static level at 31 and the horizontal disc 42 of the inverted cup-shaped member 32 is positioned below the surface of the water. The disc 42 is provided with ports 43 which are spaced from each other throughout the area of the horizontally disposed disc 42 which provide for the escape of the gas as bubbles moving upwardly through the liquid. The gas bubbles through the liquid and moves into the upper portion of the housing 11. A depending flange 44 on the inverted cup-shaped member 32 housing 11 to provide an annular space 46 between the interior of the housing 11 and the exterior of the flange 44. If there is a sudden increase in the volume of gas delivered through the tubular element 29 the excess gas escapes through the annular space 46 which then serves as an emergency spill area.
A conical shaped housing member 47 connects the upper end of the cylindrical housing 11 with the lower end of the tube whereby the gas is guided into the lower end of the stack. A cylindrical shaped baffle 48 is supported within the conical housing member 47 in sealed relationship with respect to the conical wall. Any water particles that may be carried upwardly with the gas along the inner surface of the member 47 engages the exterior of the baffle 48 and drains back into the body of water to maintain the static level 31. The gas moves into the lower end of the stack.
The structure above the partition wall 22 serves to prevent atmospheric air which may settle in the tube 10 from moving rearwardly beyond the upper end of the tubular element 29 and into the presence of inflammable liquid collected in the lower portion of the housing 11. The vertical dimension indicated at X represents the height of a water column greater than atmospheric pressure so that it is impossible for air or a flame to propagate rearwardly through the apparatus beyond the free end of the tubular element 29.
While the invention has been shown and described with reference to one assembly it will be appreciated that changes may be made in the overall organization as well as in the various elements. Other types of equipment insuring that the gas bubbles through the liquid and which prevents reversed flow of gas may be employed in the assembly. Such changes and other modifications may be has a diameter smaller than the made without departing from the spirit and scope of the invention as set forth in the appended claims.
What we claim and desire to secure by Letters Patent is:
1. A base structure for a vent stack for treating gas moving towards the stack and preventing rearward movement of gas from the stack through the base structure comprising, a vertically disposed vent stack, a generally cylindrical shaped housing of larger cross sectional dimensions than the stack supporting and providing a base therefor, a bottom wall within said housing, a partition wall within the housing spaced upwardly from said bottom wall, a generally cylindrical shaped baflle depending from said partition wall providing an annular space between the perimeter thereof and the interior of said housing, an
inlet pipe disposed to guide gas tangentially into said annular space, said partition wall having an opening therethrough within said baflle, a tubular element carried by the partition wall extending upwardly therefrom within said housing, said partition wall and said housing providing a receptacle containing a body of liquid within the housing having a static level below the upper end of said tubular element, a tubular member surrounding said tubular element providing an annular passage between the perimeter of the tubular element and the interior of the tubular member, means closing the upper end of said tubular member, means supporting the tubular member on said tubular element, a substantially horizontal disc supported by said tubular member below the static level of said liquid, said disc having spaced ports therethrough, dispersion unit means provided with a plurality of radially disposed vanes at the lower end of said tubular member for dispersing gas from said annular passages throughout the underside of said disc, an annular flange depending from said disc having a diameter smaller than said housing providing an annular space between said flange and the interior of the housing, a frusto-conical shaped housing member connecting said housing to the lower end of said stack, a cylindrical shaped baffle depending from said frusto-conical housing member around the lower end of said stack, the upper end of said tubular element being disposed above the static level of said liquid a distance sufficient to prevent gas at atmospheric pressure entering the housing from said stack and moving beyond the upper end of said tubular element, a pipe for draining liquid from the lower end of the housing, and said pipe having a vertically disposed portion which extends above the upper face of said bottom wall.
2. A base structure for a vent stack for treating gas moving into the stack and preventing rearward movement of gas from the stack through the base structure according to claim 1 wherein a cylindrical flange depends from said partition wall around said opening.
References Cited UNITED STATES PATENTS 881,194 3/1908 Moughler 55256 X 1,123,232 1/1915 Brassert et al 55457 X 1,776,032 9/ 1930 Kobernik. 1,800,831 4/1931 Hawley 55254 X 2,238,824 4/1941 Ryner 55236 X 2,250,226 7/1941 Juelson 55255 X 2,496,281 2/1950 Fisher 55398 X 2,511,967 6/1950 Campbell 55458 X FOREIGN PATENTS 864,216 l/ 1941 France. 871,760 1/ 1942 France.
D. TALBERT, Assistant Examiner.

Claims (1)

1. A BASE STRUCTURE FOR A VENT STACK FOR TREATING GAS MOVING TOWARDS THE STACK AND PREVENTING REARWARD MOVEMENT OF GAS FROM THE STACK THROUGH THE BASE STRUCTURE COMPRISING, A VERTICALLY DISPOSED VENT STACK, A GENERALLY CYLINDRICAL SHAPED HOUSING OF LARGER CROSS SECTIONAL DIMENSIONS THAN THE STACK SUPPORTING AND PROVIDING A BASE THEREFOR, A BOTTOM WALL WITHIN SAID HOUSING, A PARTITION WALL WITHIN THE HOUSING SPACED UPWARDLY FROM SAID BOTTOM WALL, A GENERALLY CYLINDRICAL SHAPED BAFFLE DEPENDING FROM SAID PARTITION WALL PROVIDING AN ANNULAR SPACE BETWEEN THE PERIMETER THEREOF AND THE INTERIOR OF SAID HOUSING, AN INLET PIPE DISPOSED TO GUIDE GAS TANGENTIALLY INTO SAID ANNULAR SPACE, SAID PARTITION WALL HAVING AN OPENING THERETHROUGH WITHIN SAID BAFFLE, A TUBULAR ELEMENT CARRIED BY THE PARTITION WALL EXTENDING UPWARDLY THEREFROM WITHIN SAID HOUSING, SAID PARTITION WALL AND SAID HOUSING PROVIDING A RECEPTACLE CONTAINING A BODY OF LIQUID WITHIN THE HOUSING HAVING A STATIC LEVEL BELOW THE UPPER END OF SAID TUBULAR ELEMENT, A TUBULAR MEMBER SURROUNDING SAID TUBULAR ELEMENT PROVIDING AN ANNULAR PASSAGE BETWEEN THE PERIMETER OF THE TUBULAR ELEMENT AND THE INTERIOR OF THE TUBULAR MEMBER, MEANS CLOSING THE UPPER END OF SAID TUBULAR MEMBER, MEANS SUPPORTING THE TUBULAR MEMBER ON SAID TUBULAR ELEMENT, A SUBSTANTIALLY HORIZONTAL DISC SUPPORTED BY SAID TUBULAR MEMBER BELOW THE STATIC LEVEL OF SAID LIQUID, SAID DISC HAVING SPACED PORTS THERETHROUGH, DISPERSION UNIT MEANS PROVIDED WITH A PLURALITY OF RADIALLY DISPOSED VANES AT THE LOWER END OF SAID TUBULAR MEMBER FOR DISPERSING GAS FROM SAID ANNULAR PASSAGES THROUGHOUT THE UNDERSIDE OF SAID DISC, AN ANNULAR FLANGE DEPENDING FROM SAID DISC HAVING A DIAMETER SMALLER THAN SAID HOUS-
US512493A 1965-10-13 1965-12-08 Flare stack structure and apparatus treating and controlling flow of gases to and from stack Expired - Lifetime US3331194A (en)

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US512493A US3331194A (en) 1965-12-08 1965-12-08 Flare stack structure and apparatus treating and controlling flow of gases to and from stack
GB3688866A GB1158401A (en) 1965-10-13 1966-08-17 Stack Structure and Apparatus Treating and Controlling Flow of Gases to and from Stack
DE19661545316 DE1545316A1 (en) 1965-10-13 1966-09-16 Exhaust flare

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US3892519A (en) * 1974-04-15 1975-07-01 Zink Co John Liquid bubble screen seal for controlling combustible gases
USRE28616E (en) * 1969-04-04 1975-11-18 Mass contact between media of different densities
US3957466A (en) * 1974-03-08 1976-05-18 Coppola John J Gas washing device
US4200443A (en) * 1977-11-30 1980-04-29 Stein Industrie Vertical separator for separating a mixture of fluid phases
US4214880A (en) * 1977-05-03 1980-07-29 Kamphorst Hendrik A Liquid seal system, e.g. for a flare stack
US4424069A (en) 1982-08-12 1984-01-03 Chang Shien Fang Dry and wet dual-purpose dust-collecting device
US5397381A (en) * 1992-09-11 1995-03-14 L. & C. Steinuller GmbH Method of cooling and optionally cleaning a hot gas, especially of a gas generated upon combustion or gasification of carbon-containing fuels
WO1997039818A1 (en) * 1996-04-25 1997-10-30 Miracle Marketing Corporation Ultra-filtration vacuum system
USD392377S (en) 1997-02-26 1998-03-17 Hicks Charles G Air cleaning system unit
WO1999019045A1 (en) * 1997-10-14 1999-04-22 Miracle Marketing Corporation Ultra-filtration vacuum system
US5904753A (en) * 1992-01-23 1999-05-18 Kvaerner Pulping Ab Separation device and process
US20040139711A1 (en) * 2002-12-11 2004-07-22 Donglei Wang Dust collector with an inbuilt cyclonic water filter
US8992838B1 (en) 2011-02-02 2015-03-31 EcoVapor Recovery Systems, LLC Hydrocarbon vapor recovery system
US9334109B1 (en) 2012-02-02 2016-05-10 EcoVapor Recovery Systems, LLC Vapor recovery systems and methods utilizing selective recirculation of recovered gases
US9776155B1 (en) 2012-02-02 2017-10-03 EcoVapor Recovery Systems, LLC Hydrocarbon vapor recovery system with oxygen reduction
WO2021001941A1 (en) * 2019-07-02 2021-01-07 大崎クールジェン株式会社 Ground flare

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Cited By (21)

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USRE28616E (en) * 1969-04-04 1975-11-18 Mass contact between media of different densities
US3957466A (en) * 1974-03-08 1976-05-18 Coppola John J Gas washing device
US3892519A (en) * 1974-04-15 1975-07-01 Zink Co John Liquid bubble screen seal for controlling combustible gases
US4214880A (en) * 1977-05-03 1980-07-29 Kamphorst Hendrik A Liquid seal system, e.g. for a flare stack
US4200443A (en) * 1977-11-30 1980-04-29 Stein Industrie Vertical separator for separating a mixture of fluid phases
US4424069A (en) 1982-08-12 1984-01-03 Chang Shien Fang Dry and wet dual-purpose dust-collecting device
US5904753A (en) * 1992-01-23 1999-05-18 Kvaerner Pulping Ab Separation device and process
US6004364A (en) * 1992-01-23 1999-12-21 Kamyr Aktiebolag Separation device
US5397381A (en) * 1992-09-11 1995-03-14 L. & C. Steinuller GmbH Method of cooling and optionally cleaning a hot gas, especially of a gas generated upon combustion or gasification of carbon-containing fuels
WO1997039818A1 (en) * 1996-04-25 1997-10-30 Miracle Marketing Corporation Ultra-filtration vacuum system
US5922093A (en) * 1996-04-25 1999-07-13 Miracle Marketing Corporation Ultra-filtration vacuum system
USD392377S (en) 1997-02-26 1998-03-17 Hicks Charles G Air cleaning system unit
WO1999019045A1 (en) * 1997-10-14 1999-04-22 Miracle Marketing Corporation Ultra-filtration vacuum system
US20040139711A1 (en) * 2002-12-11 2004-07-22 Donglei Wang Dust collector with an inbuilt cyclonic water filter
US7037361B2 (en) * 2002-12-11 2006-05-02 Donglei Wang Dust collector with an inbuilt cyclonic water filter
US8992838B1 (en) 2011-02-02 2015-03-31 EcoVapor Recovery Systems, LLC Hydrocarbon vapor recovery system
US9764255B1 (en) 2011-02-02 2017-09-19 EcoVapor Recovery Systems, LLC Hydrocarbon vapor recovery system
US9334109B1 (en) 2012-02-02 2016-05-10 EcoVapor Recovery Systems, LLC Vapor recovery systems and methods utilizing selective recirculation of recovered gases
US9776155B1 (en) 2012-02-02 2017-10-03 EcoVapor Recovery Systems, LLC Hydrocarbon vapor recovery system with oxygen reduction
WO2021001941A1 (en) * 2019-07-02 2021-01-07 大崎クールジェン株式会社 Ground flare
JPWO2021001941A1 (en) * 2019-07-02 2021-09-13 大崎クールジェン株式会社 Grand flare

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