US3838974A - Rich fume incinerator - Google Patents

Rich fume incinerator Download PDF

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Publication number
US3838974A
US3838974A US00274406A US27440672A US3838974A US 3838974 A US3838974 A US 3838974A US 00274406 A US00274406 A US 00274406A US 27440672 A US27440672 A US 27440672A US 3838974 A US3838974 A US 3838974A
Authority
US
United States
Prior art keywords
stack
housing
air
annular passageway
upper chamber
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.)
Expired - Lifetime
Application number
US00274406A
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English (en)
Inventor
K Hemsath
A Thekdi
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Surface Combustion Corp
Grimes Aerospace Co
Original Assignee
Midland Ross Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Midland Ross Corp filed Critical Midland Ross Corp
Priority to US00274406A priority Critical patent/US3838974A/en
Priority to CA168,372A priority patent/CA977620A/en
Priority to AU56682/73A priority patent/AU480459B2/en
Priority to GB2724573A priority patent/GB1428043A/en
Priority to ES1973192344U priority patent/ES192344Y/es
Priority to IT25882/73A priority patent/IT990697B/it
Priority to FR7324903A priority patent/FR2228196B1/fr
Priority to BR5083/73A priority patent/BR7305083D0/pt
Priority to JP48079353A priority patent/JPS5127893B2/ja
Priority to DE2337283A priority patent/DE2337283C3/de
Priority to US445480A priority patent/US3898317A/en
Application granted granted Critical
Publication of US3838974A publication Critical patent/US3838974A/en
Assigned to SURFACE COMBUSTION, INC. reassignment SURFACE COMBUSTION, INC. ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: FL AEROSPACE CORP.
Assigned to FL AEROSPACE CORP. reassignment FL AEROSPACE CORP. CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). 9/11/86 AND 1/05/88, OHIO Assignors: MIDLAND - ROSS CORPORATION, CHANGED TO, MIDLAND-ROSS CORPORATION MERGING INTO, MRC MERGER CORP., CHANGED NAME TO
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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
    • F23G7/061—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
    • F23G7/065—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2207/00—Control
    • F23G2207/10—Arrangement of sensing devices
    • F23G2207/101—Arrangement of sensing devices for temperature
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2207/00—Control
    • F23G2207/30—Oxidant supply

Definitions

  • ABSTRACT An incineration system for incinerating flue gases which contain varying quantities of combustibles [52] Cl 23/277 0 0 therein. Means is provided for controlling combustion dd d th fl h tl11 t b 151 int. c1.
  • the other type of fumes contains mainly a mixture of combustibles (hydrocarbons, soot particles, etc.) and other inert gases.
  • the oxygen content of such fumes is relatively small.
  • a source of ignition such as a premix pilot or a burner operating at stoichiometric air/fuel ratio
  • the fume cannot continue to burn because of insufficient oxygen.
  • incinerators are not able to complete combustion of the exhausts; thereby yielding exhaust gases with high quantities of pollutants.
  • FIG. 1 is a vertical cross-sectional view, partially schematic, of an incineration system incorporating the features of this invention.
  • FIG. 2 is a cross-sectional view taken along line 2-2 of FIG. 1.
  • a double chambered system is added to a stack emit ting industrial waste gases which contain various amounts of combustibles therein.
  • the first chamber terminates at the exit end of the stack in an annular passage, or restriction, so that air at high velocity is directed longitudinally relative the stack. This air acts as an air pump to enhance egress of the flue gases.
  • These gases then enter into the second chamber of the housing, which chamber includes a plurality of burners.
  • a thermocouple Within the second housing is a thermocouple which senses the temperature of the waste gases.
  • a preset temperature is achieved by varying the quantities of air emitted from the first chamber as opposed to the amount of fuel and air supplied to the burners in the second chamber. In this way a constant temperature may be maintained despite the variance of combustibles within the exhaust gas.
  • the fume composition, volume and temperature can vary considerably with time.
  • air and fuel supply to the incinerator must be controlled very carefully and independently.
  • an incineration system is shown generally at 10 and is adapted to incinerate exhaust fumes coming from a stack 12.
  • the stack 12 has refractory bricks 14 lined on the inside thereof in order to preserve its heat and, as shown, has its inner wall flared out at its upper end at a shallow angle to its axis to approximately meet with its outer wall.
  • Disposed about and above the stack 12 is a housing 16 having a lower chamber 18 and an upper chamber 20, the housing also being lined with refractory material 21.
  • the lower chamber 18 terminates at the upper end of the stack 12 and has a restricted channel 22 portion.
  • the lower chamber 18 also has an opening 24 therein which receives an air pipe 26.
  • the upper chamber 20 which, as shown, is formed of appreciably wider cross-sectional size than the re stricted channel portion 22 to form within the chamber an upwardly facing flame stabilization shoulder or step located just above the upper end of the stack 12, is supplied with tangential burners 28 that are received within openings 30 in the refractory 21 and are located laterally outward of the exit end of the annular passageway 22 and immediately above the exit end of the stack 112.
  • Gas lines 32 are attached to the burners 28 as are air lines 34.
  • the air lines 26 and 34 are in communication with an air control unit 36.
  • thermocouple 38 Received within the upper portion of the upper chamber 20 is a thermocouple 38 which has a lead 40 communicating with a temperature measuring and recording instrument 42.
  • the temperature measuring instrument 42 in turn has a lead 44 that communicates with the air controller 36.
  • the rich fumes are emitted from the stack 12 into the upper chamber 20.
  • the burners 28 are fired in order to provide the heat of combustion necessary for the exhaust gases.
  • a quantity of air is supplied to the lower chamber 18 from the air line 26 and passes through the channel 22 about the exit end of the stack 12. This air passing through the channel 22 acts as an air pump to aspirate and thereby enhance the discharge, or emission, of the exhaust gases from the stack 12.
  • the annular stream of air from channel 22 promotes uniform mixing of the gases within upper chamber 20.
  • the combustion products will ignite in the upper chamber and the temperature thereof is sensed by thermocouple 38.
  • the measuring instrument 42 will set a given temperature for the combustion products and will control the amount of air supplied to the lower chamber 18 and the upper chamber 20 in response to this temperature.
  • additional air will be supplied to the burners 28 in order to raise the temperature and assures complete incineration of the waste gases.
  • the burners 28 may be of the type that gas is supplied thereto in proportional response to the amount of air supplied to the burners. If the temperature becomes too high, the supply of air to the burners is discontinued and the temperature is controlled by air supplied through the air pipe 26 into the housing 16. So long as the temperature can be maintained at the set point through the supplying of air to the exhaust gases, the burners 28 need not be operated.
  • an incineration system is provided which is operative to completely combust waste gases emitted from a stack, regardless of the amount or percentage of combustibles contained in the gases.
  • an incineration system for exhaust gases emitting from a stack
  • the combination comprising: a housing confluent with and located over the upper portion of the stack, means defining a restricted annular passageway immediately surrounding the exit opening of the stack and confluent with the lower portion of the housing, means for supplying air from the said annular passageway and into said housing to produce an annular stream of air effective through its aspirating action to enhance the egress of the exhaust gases from said stack into said housing and entrain them in said air stream, at least one burner located within said housing adjacent and laterally outward of the exit end of said annular passageway, means for sensing the temperature in said housing, means responsive to said sensing means for controlling the quantity of air from said passageway and controlling the quantity of air and fuel to said burners.
  • an incineration system for exhaust gases emitting from a stack
  • the combination comprising: a housing having an upper chamber, a lower chamber, and a reduced section therebetween of essentially cylindrical form, the stack being received within said housing with its exhaust end located within the reduced section of said housing to define therewith a restricted annular passageway communicating with both said upper and lower chambers and immediately surrounding the exit opening of the stack, means for supplying air to said lower chamber to produce an annular stream of air exiting from said annular passageway into said upper chamber and effective through its aspirating action to enhance the egress of the exhaust gases from said stack into said upper chamber and entrain them in said air stream, burner means located within said upper chamber adjacent and laterally outward of the exit end of said annular passageway, means for sensing the temperature in said upper chamber, and means responsive to said temperature sensing means for controlling said air supply means and said burner means.
  • said burner means comprises a plurality of burners located adjacent and laterally outward of the exit end of said annular passageway with their longitudinal axes directed generally tangentially relative to the stack.
  • An incinerator for exhaust gases emitting from a stack and containing combustibles but insufficient oxygen to support the substantially complete combustion thereof, said incinerator comprising a housing having an upper chamber, a lower chamber, and a reduced passageway section therebetween of essentially cylindrical form, the stack being received within said housing with its exhaust end located within the reduced passageway section of said housing to define therewith a restricted annular passageway communicating with both said upper and lower chambers and immediately surrounding the exit opening of the stack, means for supplying air to said lower chamber to produce an annular stream of air exiting from said annular passageway into said upper chamber and effective through its aspirating action to enhance the egress of the exhaust gases from said stack into said upper chamber and entrain them in said air stream, an upwardly facing lateral shoulder in said upper chamber forming the lower end thereof and located immediately above and surrounding the exit end of said stack for stabilizing thereat the flame of the burning exhaust gases in the upper housing, and burner means in said upper housing located adjacent and laterally outward of the exit end of said annular passage
  • burner means comprises a plurality of burners located with their longitudinal axes directed generally tangentially relative to the stack.

Landscapes

  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Incineration Of Waste (AREA)
  • Control Of Combustion (AREA)
  • Treating Waste Gases (AREA)
US00274406A 1972-07-24 1972-07-24 Rich fume incinerator Expired - Lifetime US3838974A (en)

Priority Applications (11)

Application Number Priority Date Filing Date Title
US00274406A US3838974A (en) 1972-07-24 1972-07-24 Rich fume incinerator
CA168,372A CA977620A (en) 1972-07-24 1973-04-10 Rich fume incinerator
AU56682/73A AU480459B2 (en) 1972-07-24 1973-06-07 Fume incinerator
GB2724573A GB1428043A (en) 1972-07-24 1973-06-07 Incineration apparatus
ES1973192344U ES192344Y (es) 1972-07-24 1973-06-09 Nuevo incinerador de humos.
IT25882/73A IT990697B (it) 1972-07-24 1973-06-27 Inceneritore dei fumi
FR7324903A FR2228196B1 (de) 1972-07-24 1973-07-06
BR5083/73A BR7305083D0 (pt) 1972-07-24 1973-07-09 Processo para queimar gases residuais e aparelho de incineracao
JP48079353A JPS5127893B2 (de) 1972-07-24 1973-07-16
DE2337283A DE2337283C3 (de) 1972-07-24 1973-07-23 Vorrichtung zum Verbrennen von aus einem Schornstein kommenden Abgasen
US445480A US3898317A (en) 1972-07-24 1974-02-25 Method for incinerating flue gases

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US00274406A US3838974A (en) 1972-07-24 1972-07-24 Rich fume incinerator

Publications (1)

Publication Number Publication Date
US3838974A true US3838974A (en) 1974-10-01

Family

ID=23048050

Family Applications (1)

Application Number Title Priority Date Filing Date
US00274406A Expired - Lifetime US3838974A (en) 1972-07-24 1972-07-24 Rich fume incinerator

Country Status (9)

Country Link
US (1) US3838974A (de)
JP (1) JPS5127893B2 (de)
BR (1) BR7305083D0 (de)
CA (1) CA977620A (de)
DE (1) DE2337283C3 (de)
ES (1) ES192344Y (de)
FR (1) FR2228196B1 (de)
GB (1) GB1428043A (de)
IT (1) IT990697B (de)

Cited By (31)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3909953A (en) * 1974-02-28 1975-10-07 Midland Ross Corp Paint drying method and apparatus
US3917796A (en) * 1972-07-18 1975-11-04 Black Sivalls & Bryson Inc Method of incinerating vent gas
US3941868A (en) * 1973-02-24 1976-03-02 Georg Fischer Aktiengesellschaft Method of removing exhaust gases from plastic binded sand molds
US3988421A (en) * 1972-05-10 1976-10-26 Tecnochim S.R.L. Gas cleaning process and equipment
US4063870A (en) * 1974-11-06 1977-12-20 Stein Industrie Combustion of hot gases of low calorific power
US4218426A (en) * 1976-04-09 1980-08-19 Continental Carbon Company Method and apparatus for the combustion of waste gases
US4378334A (en) * 1980-07-11 1983-03-29 Griffith Laboratories U.S.A., Inc. Apparatus for disposal of spent sterilant or biocidal gases
US4913069A (en) * 1989-03-17 1990-04-03 Surface Combustion, Inc. Batch pyrolysis system
US5061463A (en) * 1989-08-24 1991-10-29 Hoechst Celanese Corporation Coincinerator apparatus and method for processing waste gases
US6120281A (en) * 1996-02-06 2000-09-19 Vatsky; Joel Combustion method utilizing tangential firing
WO2001009547A1 (en) * 1999-07-29 2001-02-08 Independent Stave Co. Burners with high turndown ratio and gas combustor
US20050161868A1 (en) * 2004-01-28 2005-07-28 Hugens John R.Jr. Vertical shaft melting furnace
US20080145281A1 (en) * 2006-12-14 2008-06-19 Jenne Richard A Gas oxygen incinerator
US20080173176A1 (en) * 2007-01-19 2008-07-24 Duesel Bernard F Fluid scrubber
US20080174033A1 (en) * 2007-01-19 2008-07-24 Duesel Bernard F Air stripper
US20080173031A1 (en) * 2007-01-19 2008-07-24 Duesel Bernard F Cooling tower
US20080256010A1 (en) * 2006-12-22 2008-10-16 Verizon Data Services Inc. Neural networks within a network management system
US7832714B2 (en) 2007-01-19 2010-11-16 Heartland Technology Partners Llc Desalination system
US20110174604A1 (en) * 2007-03-13 2011-07-21 Heartland Technology Partners Llc Compact wastewater concentrator using waste heat
US8568557B2 (en) 2007-03-13 2013-10-29 Heartland Technology Partners Llc Compact wastewater concentrator using waste heat
US8585869B1 (en) 2013-02-07 2013-11-19 Heartland Technology Partners Llc Multi-stage wastewater treatment system
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
US8790496B2 (en) 2007-03-13 2014-07-29 Heartland Technology Partners Llc Compact wastewater concentrator and pollutant scrubber
US8801897B2 (en) 2007-03-13 2014-08-12 Heartland Technology Partners Llc Compact wastewater concentrator and contaminant scrubber
US8808497B2 (en) 2012-03-23 2014-08-19 Heartland Technology Partners Llc Fluid evaporator for an open fluid reservoir
US9199861B2 (en) 2013-02-07 2015-12-01 Heartland Technology Partners Llc Wastewater processing systems for power plants and other industrial sources
US9296624B2 (en) 2011-10-11 2016-03-29 Heartland Technology Partners Llc Portable compact wastewater concentrator
US10005678B2 (en) 2007-03-13 2018-06-26 Heartland Technology Partners Llc Method of cleaning a compact wastewater concentrator
EP3502560A4 (de) * 2016-08-19 2020-07-29 Ebara Corporation Brennerkopf für abgasbehandlungsvorrichtung und verfahren zur herstellung davon, brennkammer für abgasbehandlungsvorrichtung sowie herstellungsverfahren und wartungsverfahren dafür

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52153140U (de) * 1976-05-18 1977-11-19
DE3929044A1 (de) * 1989-09-01 1991-03-14 Stephan Dipl Ing Winkelhorst Oelabscheider
JPH11218316A (ja) * 1998-02-03 1999-08-10 Risou Burner Kk 廃液焼却炉及び焼却方法

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3545918A (en) * 1968-02-21 1970-12-08 Ajem Lab Inc Afterburner system for cupola furnace
US3607119A (en) * 1969-09-30 1971-09-21 Midland Ross Corp Apparatus for treating gases
US3695192A (en) * 1970-10-12 1972-10-03 Joe W Von Brimer Combustion product processing device and method
US3697229A (en) * 1970-09-25 1972-10-10 Combustion Eng Automatic ignition system for flaring waste combustible gases
US3741713A (en) * 1972-03-10 1973-06-26 Zink Co John Purge gas admission control for flare system

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2105394A5 (de) * 1970-09-04 1972-04-28 Cimab Sa
FR2089445A5 (de) * 1971-04-02 1972-01-07 Sigoure Freres Sa

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3545918A (en) * 1968-02-21 1970-12-08 Ajem Lab Inc Afterburner system for cupola furnace
US3607119A (en) * 1969-09-30 1971-09-21 Midland Ross Corp Apparatus for treating gases
US3697229A (en) * 1970-09-25 1972-10-10 Combustion Eng Automatic ignition system for flaring waste combustible gases
US3695192A (en) * 1970-10-12 1972-10-03 Joe W Von Brimer Combustion product processing device and method
US3741713A (en) * 1972-03-10 1973-06-26 Zink Co John Purge gas admission control for flare system

Cited By (50)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3988421A (en) * 1972-05-10 1976-10-26 Tecnochim S.R.L. Gas cleaning process and equipment
US3917796A (en) * 1972-07-18 1975-11-04 Black Sivalls & Bryson Inc Method of incinerating vent gas
US3941868A (en) * 1973-02-24 1976-03-02 Georg Fischer Aktiengesellschaft Method of removing exhaust gases from plastic binded sand molds
US3909953A (en) * 1974-02-28 1975-10-07 Midland Ross Corp Paint drying method and apparatus
US4063870A (en) * 1974-11-06 1977-12-20 Stein Industrie Combustion of hot gases of low calorific power
US4218426A (en) * 1976-04-09 1980-08-19 Continental Carbon Company Method and apparatus for the combustion of waste gases
US4378334A (en) * 1980-07-11 1983-03-29 Griffith Laboratories U.S.A., Inc. Apparatus for disposal of spent sterilant or biocidal gases
US4913069A (en) * 1989-03-17 1990-04-03 Surface Combustion, Inc. Batch pyrolysis system
US5061463A (en) * 1989-08-24 1991-10-29 Hoechst Celanese Corporation Coincinerator apparatus and method for processing waste gases
US6120281A (en) * 1996-02-06 2000-09-19 Vatsky; Joel Combustion method utilizing tangential firing
WO2001009547A1 (en) * 1999-07-29 2001-02-08 Independent Stave Co. Burners with high turndown ratio and gas combustor
US7282172B2 (en) 2004-01-28 2007-10-16 North American Manufacturing Company Vertical shaft melting furnace
US20050161868A1 (en) * 2004-01-28 2005-07-28 Hugens John R.Jr. Vertical shaft melting furnace
US20080145281A1 (en) * 2006-12-14 2008-06-19 Jenne Richard A Gas oxygen incinerator
US20080256010A1 (en) * 2006-12-22 2008-10-16 Verizon Data Services Inc. Neural networks within a network management system
US8136797B2 (en) 2007-01-19 2012-03-20 Heartland Technology Partners, Llc Cooling tower
US20080173176A1 (en) * 2007-01-19 2008-07-24 Duesel Bernard F Fluid scrubber
US20080174033A1 (en) * 2007-01-19 2008-07-24 Duesel Bernard F Air stripper
US20080173031A1 (en) * 2007-01-19 2008-07-24 Duesel Bernard F Cooling tower
US7832714B2 (en) 2007-01-19 2010-11-16 Heartland Technology Partners Llc Desalination system
US20110036703A1 (en) * 2007-01-19 2011-02-17 Heartland Technology Partners Llc Desalination system
US8425665B2 (en) 2007-01-19 2013-04-23 Heartland Technology Partners, Llc Fluid scrubber
US8382075B2 (en) 2007-01-19 2013-02-26 Heartland Technology Partners, Llc Air stripper
US8043479B2 (en) 2007-01-19 2011-10-25 Heartland Technology Partners Llc Desalination system
US8066844B2 (en) 2007-03-13 2011-11-29 Heartland Technology Partners Llc Compact wastewater concentrator using waste heat
US8741100B2 (en) 2007-03-13 2014-06-03 Heartland Technology Partners Llc Liquid concentrator
US20110174447A1 (en) * 2007-03-13 2011-07-21 Heartland Technology Partners Llc Compact wastewater concentrator using waste heat
US20110174604A1 (en) * 2007-03-13 2011-07-21 Heartland Technology Partners Llc Compact wastewater concentrator using waste heat
US8568557B2 (en) 2007-03-13 2013-10-29 Heartland Technology Partners Llc Compact wastewater concentrator using waste heat
US11376520B2 (en) 2007-03-13 2022-07-05 Heartland Water Technology, Inc. Compact wastewater concentrator using waste heat
US8679291B2 (en) 2007-03-13 2014-03-25 Heartland Technology Partners Llc Compact wastewater concentrator using waste heat
US8066845B2 (en) 2007-03-13 2011-11-29 Heartland Technology Partners Llc Compact wastewater concentrator using waste heat
US10946301B2 (en) 2007-03-13 2021-03-16 Heartland Technology Partners Llc Compact wastewater concentrator using waste heat
US9926215B2 (en) 2007-03-13 2018-03-27 Heartland Technology Partners Llc Compact wastewater concentrator and pollutant scrubber
US8790496B2 (en) 2007-03-13 2014-07-29 Heartland Technology Partners Llc Compact wastewater concentrator and pollutant scrubber
US8801897B2 (en) 2007-03-13 2014-08-12 Heartland Technology Partners Llc Compact wastewater concentrator and contaminant scrubber
US10596481B2 (en) 2007-03-13 2020-03-24 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
US10005678B2 (en) 2007-03-13 2018-06-26 Heartland Technology Partners Llc Method of cleaning a compact wastewater concentrator
US9617168B2 (en) 2007-03-13 2017-04-11 Heartland Technology Partners Llc Compact wastewater concentrator using waste heat
US9808738B2 (en) 2007-03-13 2017-11-07 Heartland Water Technology, Inc. Compact wastewater concentrator using waste heat
US8721771B2 (en) 2011-01-21 2014-05-13 Heartland Technology Partners Llc Condensation plume mitigation system for exhaust stacks
US9296624B2 (en) 2011-10-11 2016-03-29 Heartland Technology Partners Llc Portable compact wastewater concentrator
US9943774B2 (en) 2012-03-23 2018-04-17 Heartland Technology Partners Llc Fluid evaporator for an open fluid reservoir
US8808497B2 (en) 2012-03-23 2014-08-19 Heartland Technology Partners Llc Fluid evaporator for an open fluid reservoir
US8741101B2 (en) 2012-07-13 2014-06-03 Heartland Technology Partners Llc Liquid concentrator
US9199861B2 (en) 2013-02-07 2015-12-01 Heartland Technology Partners Llc Wastewater processing systems for power plants and other industrial sources
US8585869B1 (en) 2013-02-07 2013-11-19 Heartland Technology Partners Llc Multi-stage wastewater treatment system
EP3502560A4 (de) * 2016-08-19 2020-07-29 Ebara Corporation Brennerkopf für abgasbehandlungsvorrichtung und verfahren zur herstellung davon, brennkammer für abgasbehandlungsvorrichtung sowie herstellungsverfahren und wartungsverfahren dafür
US10920981B2 (en) 2016-08-19 2021-02-16 Ebara Corporation Burner head for exhaust gas processing apparatus, manufacturing method of the same, combustion chamber for exhaust gas processing apparatus, and manufacturing method and maintenance method of the same

Also Published As

Publication number Publication date
JPS4945437A (de) 1974-04-30
DE2337283B2 (de) 1977-07-28
DE2337283C3 (de) 1978-03-16
IT990697B (it) 1975-07-10
GB1428043A (en) 1976-03-17
AU5668273A (en) 1974-12-12
ES192344Y (es) 1975-01-01
CA977620A (en) 1975-11-11
DE2337283A1 (de) 1974-02-07
FR2228196B1 (de) 1978-07-21
FR2228196A1 (de) 1974-11-29
JPS5127893B2 (de) 1976-08-16
BR7305083D0 (pt) 1974-09-05
ES192344U (es) 1974-09-01

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