US3730673A - Vent seal - Google Patents

Vent seal Download PDF

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Publication number
US3730673A
US3730673A US00142700A US3730673DA US3730673A US 3730673 A US3730673 A US 3730673A US 00142700 A US00142700 A US 00142700A US 3730673D A US3730673D A US 3730673DA US 3730673 A US3730673 A US 3730673A
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stack
flare
diode
air
fluidic
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US00142700A
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J Straitz
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COMBUSTION UNLIMITED INC US
Combustion Unlimited Inc
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Combustion Unlimited Inc
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/06Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
    • F23G7/08Incinerators 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

  • a vent seal is provided for use with vent stacks, blow down lines, flare systems and the like to prevent entrainment of air into the stack which comprises a diode interposed in the stack below the top, the diode comprising spaced frustoconicaI concentric baffles with aligned central openings providing an obstruction to downflow of air within the stack but not retarding upward delivery of hot gas 3 Claims, 6 Drawing Figures 2 Sheets-Sheet 1 77/ 7] v INVENTO/F' Patented May 1, 1973 2 Sheets-Sheet 2 INVENTOR JOHN F. STRA/TLE FIG. 4
  • a TTOR/VEV VENT SEAL BACKGROUND OF THE INVENTION tube or pressure drop effect.
  • a fluidic seal is provided in a vent stack, the seal having the action of .an obstruction to down flow of air within the stack together with an upward jet action of the stack or purge gases.
  • FIG. 1 is a view partly in elevation and partly in vertical section of a flare burner with the fluidic diode of the invention incorporated'therewith;
  • FIG. 2 is a horizontal sectional view taken approximately on the line 2-2 of FIG. 1;
  • FIG. 3 is a view similar to FIG. 1 but showing a different construction of flare burners
  • FIG. 4 is a top plan view of the flare burner shown in FIG. 3;
  • FIG. 5 is a view similar to FIG. 1 but showing a still different construction of flare burner.
  • FIG. 6 is a top plan view of the flare burner shown in FIG. 5.
  • FIGS. 1 and 2 of the drawings a stack 10 is shown to which hot flare gas from an oil refinery or the like is delivered for combustion.
  • the stack 10 has an upper section 11 to which a pipe 12 extends, the pipe 12 having a discharge nozzle or tip 13 centrally disposed within the stack section 11 for the delivery of gas free from oxygen for purging.
  • a fluidic diode 15 is provided in the stack 10.
  • the diode 15 preferably comprises a plurality of frustoconical baffles 16, 17, 18 and 19 of metal of suitable gage, or other material,- not adversely affected by the elevated temperature of the flare gas which may.
  • baffles 16, 17, 18 and 19 terminate at their peripheries at the stack 10.
  • the baffles 16, 17, 18 and 19 preferably have axially aligned central openings 21, 22, 23 and 24 of increasing ascending areas.
  • baffles 16, 17, 18 and 19 are shown, these having been found to be effective. With a reduced number of baffles, say three, a tendency of the oxygen level to increase to objectionable levels was noted.
  • the flare burner 25 is provided and may include within the stack 10 and below the inwardly flanged terminus 26 of the stack 10, a ceramic or other refractory liner 27. i t
  • a steam pipe 28 with a discharge nozzle 29 may be provided centrally disposed within the liner 27 for impelling the flare gases for discharge.
  • externally disposed nozzles 30 for supplying steam or air may be provided.
  • the effect of wind flow around the top of the stack is to produce a high pressure zone upstream of thestack l0 and a low pressure zone downstream of the stack 10 and this may result in a circulation of air down the interior of the stack.
  • the air progresses down the stack along the wall it is stopped by the uppermost baffle 19 and turned back on itself. Any air at the center or at the central opening 24 is impelled upwardly not by a discontinuity of flow but by the jet action of the gas passing upwardly through the opening 24.
  • the jet action occurs because the cross-sectional area at the opening 24 is reduced. so that the velocity of the gas passing therethrough is increased.
  • baffles 17 and 16 also have a similar action.
  • the fluidic seal by reason of its having a higher pressure drop in the reverse direction, i.e. downwardly, prevents air flow being pulled down in the stack 10 due to contraction of the gas in the system therebelow.
  • the fluidic seal also tends to prevent flow oscillation by reason of its higher pressure in the reverse direction.
  • the stack 10 may have the diode 15 therein as before with the upper section 1 l thereabove having a refractory lining 27.
  • a steam delivery pipe 28 and nozzle 29 can also be provided and exteriorly of the stack 10 and, extending above the flame retention ring 26, air or steam delivery jets 30.
  • a pilot and igniter 35 is preferably also provided which has a combustible gas supply pipe 36 connected through a pilot inspirator 37 to provide the proper gasair mixture for combustion at the ingniter 35.
  • the stack may have diode therein as before with the upper section 11 thereabove having a refractory lining 27.
  • a plurality of pilots and igniters 35a are provided at the top of the stack section 11 and surrounded by a cylindrical wind shield 38.
  • the pilots and igniters 35a are supplied with combustible gas-air mixture from a gas supply pipe 36 through an inspirator 37.
  • said stack having a burner at its upper discharge end for combustion beyond said discharge end of flare gas supplied to the lower end of said stack, pilot means for ignition of said flare gas at said burner, and means in said stack for preventing downflow in said stack due to external wind or to contraction of gas therebelow, said means comprising a fluidic diode in spaced relation from the terminus of the discharge section permitting flow for discharge with increase of velocity and obstructing return flow in the stack, frustoconical said fluidic diode being closed from fluid access except for a single fluid inlet opening and a single fluid outlet opening and comprising a plurality of axially aligned frustoconical baffles with aligned central openings.

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  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)

Abstract

A vent seal is provided for use with vent stacks, blow down lines, flare systems and the like to prevent entrainment of air into the stack which comprises a diode interposed in the stack below the top, the diode comprising spaced frustoconical concentric baffles with aligned central openings providing an obstruction to down flow of air within the stack but not retarding upward delivery of hot gas.

Description

United States Patent 1191 Straitz, III
15 1 VENT SEAL [75] Inventor: John F. Straitz, III, CheItenham, Pa.
[73] Assignee: Combustion Unlimited, Incorporated, Elkins Park, Pa.
['22,] Filed: May 12, 1971 [21] App1.No.: 142,700
[52] US. Cl ..431/278, 126/307 A, 138/44,
431/4, 431/202, 431/346 [51] Int. Cl...; ..F23d 13/20 [58] Field of Search ..431/202, 278, 283,
[56] References Cited UNITED STATES PATENTS 738,433 9 1903 Graham ..431/346 1,663,998 3/1928 Schmidt ..l38/44 x 1,976,870 10 1934 Weber ..431/346 x 1451 May 1, 1973 2,537,091 1/1951 Rodman et a1 ..431/346 X 2,781,716 2/1957 Moran ..98/58 2,506,972 5/1950 Schellentrager et a1 ..431/202 FOREIGN PATENTS OR APPLICATIONS 93,949 4/1969 France ..126/307 A Primary Examiner-William F. ODea Assistant Examiner-Peter D. Ferguson Attorney-Zachary T. Wobensmith, 2nd
571 ABSTRACT A vent seal is provided for use with vent stacks, blow down lines, flare systems and the like to prevent entrainment of air into the stack which comprises a diode interposed in the stack below the top, the diode comprising spaced frustoconicaI concentric baffles with aligned central openings providing an obstruction to downflow of air within the stack but not retarding upward delivery of hot gas 3 Claims, 6 Drawing Figures 2 Sheets-Sheet 1 77/ 7] v INVENTO/F' Patented May 1, 1973 2 Sheets-Sheet 2 INVENTOR JOHN F. STRA/TLE FIG. 4
A TTOR/VEV VENT SEAL BACKGROUND OF THE INVENTION tube or pressure drop effect.
The prior designs overlooked the phenomena best suited to prevent air from moving down the stack by imposing a discontinuity on the flow pattern so that the air current moving down the stack is turned back upon itself as well as by an upward jet action of the purge gases.
SUMMARY OF THE INVENTION In accordance with the invention a fluidic seal is provided in a vent stack, the seal having the action of .an obstruction to down flow of air within the stack together with an upward jet action of the stack or purge gases.
It is the principal object of the present invention to provide a seal system which prevents downflow of air in the stack whether by external wind conditions or contraction by cooling of hot gas in the system.
It is a further object of the present invention to provide a seal system in which fluid oscillations will be prevented.
Other objects and advantageous features of the invention will be apparent from the description and claims.
BRIEF DESCRI ITION OF THE DRAWINGS The nature and characteristic features of the invention will be more readily understood from the following description taken in connection with the accompanying drawings forming part thereof, in which:
FIG. 1 is a view partly in elevation and partly in vertical section of a flare burner with the fluidic diode of the invention incorporated'therewith;
FIG. 2 is a horizontal sectional view taken approximately on the line 2-2 of FIG. 1;
FIG. 3 is a view similar to FIG. 1 but showing a different construction of flare burners;
FIG. 4 is a top plan view of the flare burner shown in FIG. 3;
FIG. 5 is a view similar to FIG. 1 but showing a still different construction of flare burner; and
FIG. 6 is a top plan view of the flare burner shown in FIG. 5.
It should, of course, be understood that the description and drawings herein are illustrative merely and that various modifications and changes can be made in the structure disclosed without departing from the spirit of the invention.
Like numerals refer to like parts throughout the several views.
DESCRIPTION OF THE PREFERRED EMBODIMENTS Referring now more particularly to FIGS. 1 and 2 of the drawings a stack 10 is shown to which hot flare gas from an oil refinery or the like is delivered for combustion.
The stack 10 has an upper section 11 to which a pipe 12 extends, the pipe 12 having a discharge nozzle or tip 13 centrally disposed within the stack section 11 for the delivery of gas free from oxygen for purging.
Immediately above the section 11, a fluidic diode 15 is provided in the stack 10.
The diode 15 preferably comprises a plurality of frustoconical baffles 16, 17, 18 and 19 of metal of suitable gage, or other material,- not adversely affected by the elevated temperature of the flare gas which may.
be of the order of 400 to 700 Fahrenheit. The baffles 16, 17, 18 and 19 terminate at their peripheries at the stack 10.
The baffles 16, 17, 18 and 19 preferably have axially aligned central openings 21, 22, 23 and 24 of increasing ascending areas.
In the specific embodiment illustrated fourbaffles 16, 17, 18 and 19 are shown, these having been found to be effective. With a reduced number of baffles, say three, a tendency of the oxygen level to increase to objectionable levels was noted.
Above the diode 15 the flare burner 25 is provided and may include within the stack 10 and below the inwardly flanged terminus 26 of the stack 10, a ceramic or other refractory liner 27. i t
, A steam pipe 28 with a discharge nozzle 29 may be provided centrally disposed within the liner 27 for impelling the flare gases for discharge. i
If desired, also, externally disposed nozzles 30 for supplying steam or air, may be provided. by
The effect of wind flow around the top of the stack is to produce a high pressure zone upstream of thestack l0 and a low pressure zone downstream of the stack 10 and this may result in a circulation of air down the interior of the stack. As the air progresses down the stack along the wall it is stopped by the uppermost baffle 19 and turned back on itself. Any air at the center or at the central opening 24 is impelled upwardly not by a discontinuity of flow but by the jet action of the gas passing upwardly through the opening 24. The jet action occurs because the cross-sectional area at the opening 24 is reduced. so that the velocity of the gas passing therethrough is increased.
There may be some air leakage downwardly at the edge of opening 24 and this, upon downward movement, encounters the baffle .18 where the action is.
similar to that previously described. The baffles 17 and 16 also have a similar action.
It will be noted that the fluidic seal, by reason of its having a higher pressure drop in the reverse direction, i.e. downwardly, prevents air flow being pulled down in the stack 10 due to contraction of the gas in the system therebelow.
The fluidic seal also tends to prevent flow oscillation by reason of its higher pressure in the reverse direction.
Referring now to FIGS. 3 and 4, in the embodiment of the invention there illustrated, the stack 10 may have the diode 15 therein as before with the upper section 1 l thereabove having a refractory lining 27.
A steam delivery pipe 28 and nozzle 29 can also be provided and exteriorly of the stack 10 and, extending above the flame retention ring 26, air or steam delivery jets 30.
A pilot and igniter 35 is preferably also provided which has a combustible gas supply pipe 36 connected through a pilot inspirator 37 to provide the proper gasair mixture for combustion at the ingniter 35.
Referring now to FIGS. 5 and 6, in the embodiment of the invention there illustrated, the stack may have diode therein as before with the upper section 11 thereabove having a refractory lining 27.
A plurality of pilots and igniters 35a are provided at the top of the stack section 11 and surrounded by a cylindrical wind shield 38. The pilots and igniters 35a are supplied with combustible gas-air mixture from a gas supply pipe 36 through an inspirator 37.
The action of the diode 15 with respect to air externally at the top of the stack section 11 is the same as that previously described.
I claim:
1. The combination comprising a vertical tubular flare stack,
said stack having a burner at its upper discharge end for combustion beyond said discharge end of flare gas supplied to the lower end of said stack, pilot means for ignition of said flare gas at said burner, and means in said stack for preventing downflow in said stack due to external wind or to contraction of gas therebelow, said means comprising a fluidic diode in spaced relation from the terminus of the discharge section permitting flow for discharge with increase of velocity and obstructing return flow in the stack, frustoconical said fluidic diode being closed from fluid access except for a single fluid inlet opening and a single fluid outlet opening and comprising a plurality of axially aligned frustoconical baffles with aligned central openings. 2. A fluidic seal as defined in claim 1 in which said openings are of increasing diameter from bottom to top. 3. A fluidic seal as defined in claim 1 in which said baffles are in a stacked arrangement within said stack.

Claims (3)

1. The combination comprising a vertical tubular flare stack, said stack having a burner at its upper discharge end for combustion beyond said discharge end of flare gas supplied to the lower end of said stack, pilot means for ignition of said flare gas at said burner, and means in said stack for preventing downflow in said stack due to external wind or to contraction of gas therebelow, said means comprising a fluidic diode in spaced relation from the terminus of the discharge section permitting flow for discharge with increase of velocity and obstructing return flow in the stack, frustoconical said fluidic diode being closed from fluid access except for a single fluid inlet opening and a single fluid outlet opening and comprising a plurality of axially aligned frustoconical baffles with aligned central openings.
2. A fluidic seal as defined in claim 1 in which said openings are of increasing diameter from bottom to top.
3. A fluidic seal as defined in claim 1 in which said baffles are in a stacked arrangement within said stack.
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Cited By (47)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3994671A (en) * 1975-03-14 1976-11-30 Combustion Unlimited Incorporated Flare gas burner
US4038024A (en) * 1975-12-03 1977-07-26 Combustion Unlimited Incorporated Flare stack gas burner
US4092908A (en) * 1977-07-15 1978-06-06 Combustion Unlimited Incorporated Fluidic seal
US4101257A (en) * 1977-06-16 1978-07-18 Combustion Unlimited Incorporated Pilot gas conservation system for flare stacks
US4118173A (en) * 1977-08-08 1978-10-03 Samuel Lebidine Unidirectional seal for flow passages
US4128389A (en) * 1977-08-22 1978-12-05 Combustion Unlimited Incorporated Flare stack gas burner
US4140471A (en) * 1977-05-09 1979-02-20 National Airoil Burner Company, Inc. Ground flare stack
US4147495A (en) * 1977-10-26 1979-04-03 Combustion Unlimited Incorporated Waste gas dispersion stack
US4194876A (en) * 1977-09-29 1980-03-25 Combustion Unlimited Incorporated Liquid burnpits
US4344751A (en) * 1979-03-24 1982-08-17 The British Petroleum Company Limited Flares
DE3200395A1 (en) * 1981-01-10 1982-09-30 JGC Corp., Tokyo FLOOR TORCH PIPE
US4565522A (en) * 1984-08-29 1986-01-21 John Zink Company Shielded flare gas burner
US4573906A (en) * 1984-08-29 1986-03-04 John Zink Company Shielded smoke suppressing flare gas burner
US4579521A (en) * 1984-08-29 1986-04-01 John Zink Company Flare gas burner
US4637793A (en) * 1984-08-29 1987-01-20 John Zink Company Flare gas burner
US4664617A (en) * 1985-11-26 1987-05-12 John Zink Company Method and burner apparatus for flaring inert vitiated waste gases
US4834645A (en) * 1988-03-07 1989-05-30 Iowa State University Research Foundation, Inc. Method and apparatus for transport, introduction, atomization and excitation of emission spectrum for quantitative analysis of high temperature gas sample streams containing vapor and particulates without degradation of sample stream temperature
US4952137A (en) * 1986-09-08 1990-08-28 John Zink Company Flare gas burner
US4975042A (en) * 1985-11-26 1990-12-04 John Zink Company Method and burner apparatus for flaring inert vitiated waste gases
US5681160A (en) * 1994-07-26 1997-10-28 Hamworthy Combustion Eng Ltd Flare tip structure and a method of disposal of gas ulilizing such a structure
US5758605A (en) * 1995-10-17 1998-06-02 Calkins; Noel C. Steam generator
US6840760B1 (en) * 2003-08-13 2005-01-11 Michael R. Keller Gas-assisted flare burner
US20060240369A1 (en) * 2005-04-26 2006-10-26 Heat Recovery Systems, Llc Waste heat recovery system
US7442035B2 (en) 2005-04-26 2008-10-28 Gei Development, Llc Gas induction bustle for use with a flare or exhaust stack
US20100176042A1 (en) * 2007-03-13 2010-07-15 Duesel Jr Bernard F Wastewater Concentrator
US20110061816A1 (en) * 2007-03-13 2011-03-17 Heartland Technology Partners Llc Compact wastewater concentrator using waste heat
US20110083556A1 (en) * 2007-03-13 2011-04-14 Heartland Technology Partners Compact wastewater concentrator and pollutant scrubber
US20110100924A1 (en) * 2007-03-13 2011-05-05 Heartland Technology Partners Llc Compact Wastewater Concentrator and Contaminant Scrubber
US20110139453A1 (en) * 2009-12-10 2011-06-16 Halliburton Energy Services, Inc. Fluid flow control device
US20110186300A1 (en) * 2009-08-18 2011-08-04 Dykstra Jason D Method and apparatus for autonomous downhole fluid selection with pathway dependent resistance system
US20120070790A1 (en) * 2010-09-22 2012-03-22 US Gov't Represented by the Secretary of the Navy Office of Naval Research (ONR/NRL) Code OOCCIP Apparatus methods and systems of unidirectional propagation of gaseous detonations
US8585869B1 (en) 2013-02-07 2013-11-19 Heartland Technology Partners Llc Multi-stage wastewater treatment system
US8616290B2 (en) 2010-04-29 2013-12-31 Halliburton Energy Services, Inc. Method and apparatus for controlling fluid flow using movable flow diverter assembly
US8721771B2 (en) 2011-01-21 2014-05-13 Heartland Technology Partners Llc Condensation plume mitigation system for exhaust stacks
US8741101B2 (en) 2012-07-13 2014-06-03 Heartland Technology Partners Llc Liquid concentrator
US8741100B2 (en) 2007-03-13 2014-06-03 Heartland Technology Partners Llc Liquid concentrator
US8808497B2 (en) 2012-03-23 2014-08-19 Heartland Technology Partners Llc Fluid evaporator for an open fluid reservoir
US8991506B2 (en) 2011-10-31 2015-03-31 Halliburton Energy Services, Inc. Autonomous fluid control device having a movable valve plate for downhole fluid selection
US9127526B2 (en) 2012-12-03 2015-09-08 Halliburton Energy Services, Inc. Fast pressure protection system and method
US9199861B2 (en) 2013-02-07 2015-12-01 Heartland Technology Partners Llc Wastewater processing systems for power plants and other industrial sources
US9260952B2 (en) 2009-08-18 2016-02-16 Halliburton Energy Services, Inc. Method and apparatus for controlling fluid flow in an autonomous valve using a sticky switch
US9291032B2 (en) 2011-10-31 2016-03-22 Halliburton Energy Services, Inc. Autonomous fluid control device having a reciprocating valve for downhole fluid selection
US9296624B2 (en) 2011-10-11 2016-03-29 Heartland Technology Partners Llc Portable compact wastewater concentrator
US9404349B2 (en) 2012-10-22 2016-08-02 Halliburton Energy Services, Inc. Autonomous fluid control system having a fluid diode
US9695654B2 (en) 2012-12-03 2017-07-04 Halliburton Energy Services, Inc. Wellhead flowback control system and method
US9808738B2 (en) 2007-03-13 2017-11-07 Heartland Water Technology, Inc. Compact wastewater concentrator using waste heat
US10005678B2 (en) 2007-03-13 2018-06-26 Heartland Technology Partners Llc Method of cleaning a compact wastewater concentrator

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US1976870A (en) * 1930-07-02 1934-10-16 Weber Anton Cooking range flame protector
US2506972A (en) * 1947-03-08 1950-05-09 Standard Oil Co Flare stack tip
US2537091A (en) * 1945-10-20 1951-01-09 Universal Oil Prod Co Waste gas burner
US2781716A (en) * 1955-02-02 1957-02-19 William O Moran Draft equalizing stack head with rain guards
FR93949E (en) * 1967-03-03 1969-06-06 Zaniewski Michel Henry Improved device increasing and stabilizing the chimney draft.

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US738433A (en) * 1902-08-25 1903-09-08 James L Graham Gas-burner.
US1663998A (en) * 1925-05-28 1928-03-27 Westinghouse Electric & Mfg Co Means for minimizing fluid pulsations
US1976870A (en) * 1930-07-02 1934-10-16 Weber Anton Cooking range flame protector
US2537091A (en) * 1945-10-20 1951-01-09 Universal Oil Prod Co Waste gas burner
US2506972A (en) * 1947-03-08 1950-05-09 Standard Oil Co Flare stack tip
US2781716A (en) * 1955-02-02 1957-02-19 William O Moran Draft equalizing stack head with rain guards
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Cited By (74)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3994671A (en) * 1975-03-14 1976-11-30 Combustion Unlimited Incorporated Flare gas burner
US4038024A (en) * 1975-12-03 1977-07-26 Combustion Unlimited Incorporated Flare stack gas burner
US4140471A (en) * 1977-05-09 1979-02-20 National Airoil Burner Company, Inc. Ground flare stack
US4101257A (en) * 1977-06-16 1978-07-18 Combustion Unlimited Incorporated Pilot gas conservation system for flare stacks
US4092908A (en) * 1977-07-15 1978-06-06 Combustion Unlimited Incorporated Fluidic seal
DE2829971A1 (en) * 1977-07-15 1979-01-25 Combustion Unltd Inc FLUE PIPE FOR WASTE GAS
US4118173A (en) * 1977-08-08 1978-10-03 Samuel Lebidine Unidirectional seal for flow passages
US4128389A (en) * 1977-08-22 1978-12-05 Combustion Unlimited Incorporated Flare stack gas burner
US4194876A (en) * 1977-09-29 1980-03-25 Combustion Unlimited Incorporated Liquid burnpits
US4147495A (en) * 1977-10-26 1979-04-03 Combustion Unlimited Incorporated Waste gas dispersion stack
US4344751A (en) * 1979-03-24 1982-08-17 The British Petroleum Company Limited Flares
DE3200395A1 (en) * 1981-01-10 1982-09-30 JGC Corp., Tokyo FLOOR TORCH PIPE
US4565522A (en) * 1984-08-29 1986-01-21 John Zink Company Shielded flare gas burner
US4573906A (en) * 1984-08-29 1986-03-04 John Zink Company Shielded smoke suppressing flare gas burner
US4579521A (en) * 1984-08-29 1986-04-01 John Zink Company Flare gas burner
US4637793A (en) * 1984-08-29 1987-01-20 John Zink Company Flare gas burner
US4664617A (en) * 1985-11-26 1987-05-12 John Zink Company Method and burner apparatus for flaring inert vitiated waste gases
AU585382B2 (en) * 1985-11-26 1989-06-15 John Zink Company Llc Method and burner apparatus for flaring waste gases
US4975042A (en) * 1985-11-26 1990-12-04 John Zink Company Method and burner apparatus for flaring inert vitiated waste gases
US4952137A (en) * 1986-09-08 1990-08-28 John Zink Company Flare gas burner
US4834645A (en) * 1988-03-07 1989-05-30 Iowa State University Research Foundation, Inc. Method and apparatus for transport, introduction, atomization and excitation of emission spectrum for quantitative analysis of high temperature gas sample streams containing vapor and particulates without degradation of sample stream temperature
US5681160A (en) * 1994-07-26 1997-10-28 Hamworthy Combustion Eng Ltd Flare tip structure and a method of disposal of gas ulilizing such a structure
US5758605A (en) * 1995-10-17 1998-06-02 Calkins; Noel C. Steam generator
US6840760B1 (en) * 2003-08-13 2005-01-11 Michael R. Keller Gas-assisted flare burner
US20060240369A1 (en) * 2005-04-26 2006-10-26 Heat Recovery Systems, Llc Waste heat recovery system
US7442035B2 (en) 2005-04-26 2008-10-28 Gei Development, Llc Gas induction bustle for use with a flare or exhaust stack
US20090053659A1 (en) * 2005-04-26 2009-02-26 Gei Development Llc Gas induction bustle for use with a flare or exhaust stack
US8459984B2 (en) 2005-04-26 2013-06-11 Heartland Technology Partners Llc Waste heat recovery system
US8172565B2 (en) 2005-04-26 2012-05-08 Heartland Technology Partners Llc Gas induction bustle for use with a flare or exhaust stack
US10596481B2 (en) 2007-03-13 2020-03-24 Heartland Technology Partners Llc Compact wastewater concentrator using waste heat
US20100176042A1 (en) * 2007-03-13 2010-07-15 Duesel Jr Bernard F Wastewater Concentrator
US11376520B2 (en) 2007-03-13 2022-07-05 Heartland Water Technology, Inc. Compact wastewater concentrator using waste heat
US10946301B2 (en) 2007-03-13 2021-03-16 Heartland Technology Partners Llc Compact wastewater concentrator using waste heat
US20110083556A1 (en) * 2007-03-13 2011-04-14 Heartland Technology Partners Compact wastewater concentrator and pollutant scrubber
US20110061816A1 (en) * 2007-03-13 2011-03-17 Heartland Technology Partners Llc Compact wastewater concentrator using waste heat
US10179297B2 (en) 2007-03-13 2019-01-15 Heartland Technology Partners Llc Compact wastewater concentrator using waste heat
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