WO2014027915A1 - Brûleur à phases multiples à effet coanda à écrans - Google Patents

Brûleur à phases multiples à effet coanda à écrans Download PDF

Info

Publication number
WO2014027915A1
WO2014027915A1 PCT/RU2012/000675 RU2012000675W WO2014027915A1 WO 2014027915 A1 WO2014027915 A1 WO 2014027915A1 RU 2012000675 W RU2012000675 W RU 2012000675W WO 2014027915 A1 WO2014027915 A1 WO 2014027915A1
Authority
WO
WIPO (PCT)
Prior art keywords
gas
shroud
flare
head member
gas flow
Prior art date
Application number
PCT/RU2012/000675
Other languages
English (en)
Inventor
Christian Menger
Roman Alexandrovich SKACHKOV
Roman Pavlovich SOTSKIJ
Grigory Yurievich MIKHALEV
Original Assignee
Schlumberger Canada Limited
Services Petroliers Schlumberger
Schlumberger Holdings Limited
Schlumberger Technology B.V.
Prad Research And Development Limited
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 Schlumberger Canada Limited, Services Petroliers Schlumberger, Schlumberger Holdings Limited, Schlumberger Technology B.V., Prad Research And Development Limited filed Critical Schlumberger Canada Limited
Priority to EP12891401.7A priority Critical patent/EP2885579B1/fr
Priority to PCT/RU2012/000675 priority patent/WO2014027915A1/fr
Priority to NO12891401A priority patent/NO2885579T3/no
Priority to US14/421,985 priority patent/US20150211735A1/en
Publication of WO2014027915A1 publication Critical patent/WO2014027915A1/fr

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D14/00Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
    • F23D14/20Non-premix gas burners, i.e. in which gaseous fuel is mixed with combustion air on arrival at the combustion zone
    • F23D14/22Non-premix gas burners, i.e. in which gaseous fuel is mixed with combustion air on arrival at the combustion zone with separate air and gas feed ducts, e.g. with ducts running parallel or crossing each other
    • 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D14/00Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
    • F23D14/46Details, e.g. noise reduction means
    • F23D14/62Mixing devices; Mixing tubes
    • 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
    • F23G7/085Incinerators 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

Definitions

  • the disclosure relates to a gas flare, and in particular, but not exclusively to a Coanda-type gas burner flare used for combustion of waste gas during surface testing of hydrocarbon wells.
  • Hydrocarbons' importance for the world economy cannot be overstated.
  • the discovery and efficient production of hydrocarbons is becoming increasingly more difficult and poses many new technological challenges.
  • a borehole is drilled down into the earth, on land or in subsea operations, to reach a reservoir containing hydrocarbons.
  • fluid hydrocarbons take the form of oil, gas, or mixtures thereof found in reservoirs that can be produced by one or more wells.
  • Well testing includes flowing a well and measuring the response of several key parameters such as pressure and flow rate over time. Many different types of well tests are known to those skilled in the art, such as pressure drawdown, interference, reservoir limit tests, etc. Well testing enables the collection of data that help assess the economic viability of the well. However, the cost of testing operations is significant and often times it may exceed the cost associated with drilling the well. It is important, therefore, that testing operations are performed as efficiently and economically as possible.
  • the well effluent is separated into its individual phases, i.e., oil, water and gas via the use of one or more well test separators.
  • One of the key functions of a well testing operation is to combust the waste gas flow exiting the well test separator.
  • Coanda-type flaring systems are widely used in the petroleum industry for flaring waste gases of oil refineries or production platforms. Typical Coanda-type flare systems are described in the following patent documents: US 3709654, US 3915622, US 2006/0105276 Al, US 383337, EP 0054383 and RU 2315240.
  • Coanda flares offer relatively clean combustion by premixing the waste gas with ambient air prior to combustion. Coanda flares also offer generally good, stable flame combustion at high inlet pressure of combustible gas.
  • Coanda-type flaring systems offer stable and quite clean combustion of multiphase hydrocarbon effluents. Coanda-type flares are efficient and environmental friendly under proper operational conditions.
  • the Coanda-type flare apparatus described in patent US 4486167 comprises a Coanda body, a slot for gas outlet form the supply pipe, a fructo- conical shield for noise reduction, and another shield for noise reflection.
  • a fructo- conical shield for noise reduction for noise reduction
  • another shield for noise reflection for noise reflection.
  • the addition of these shield decreases the air supply to the burner and creates a narrow operational range on flow rates of gas.
  • the debris can be sand particles or other particulates present in the wellbore effluent.
  • Another source of debris is pipe scale or the built up of salt deposits around the Coanda slot that can become dislodged once they reach a critical mass. Debris ejected through the Coanda slot poses a risk of injury to the operators as well as damage to the surrounding equipment. There may also be a fraction of the big liquid droplets that do not follow the gas flow and spray sideways from the slot, causing some fallout, especially if the liquid present in gas stream is highly viscous.
  • a gas flare that overcomes the above mentioned deficiencies of existing Coanda-type gas flares.
  • the inventive gas flare comprises: a supply pipe for directing a gas flow to a head member; a slot for ejecting the gas flow; and a shroud surrounding the slot, at least part of the supply pipe and at least part of the head member.
  • the shroud directs the ejected gas flow between the shroud and the head member.
  • the shroud prevents the gas flow from being ejected substantially radially from the gas flare. So while the gas flow is still ejected radially from the slot to provide a Coanda effect and aspiration of an ambient air, such gas flow including any liquid progresses only as far as the shroud and adheres to the head member.
  • the safety of the device is improved, since any debris contained in the high-speed gas flow will be contained within the shroud.
  • a shroud for a gas flare the shroud surrounding at least a portion of the gas flare and designed for directing a gas flow ejected from the gas flare to flow between the shroud and the gas flare and for enabling an ambient air flow to be directed to mix with the gas flow ejected from the gas flare.
  • a shroud with an axial airfoil-shaped cross-section with a smooth bottom end and a sharp distal end, so that the air aspired by gas jet coming from a slot is being accelerated from the smooth bottom end to the sharp distal end of the shroud.
  • a method of combusting gas ejected from a gas flare comprising: directing the gas flow using a gas flare having a contoured shape; directing an ambient air flow using a shroud surrounding at least part of the gas flare to flow between the shroud and gas flare; mixing the gas flow with an ambient air flow; and combusting the mixture.
  • the disclosure could be used with other gas flare systems, however, it is particularly advantageous when used in combination with a Coanda-type flare, especially one having a tulip-contoured shape.
  • the Coanda gas flare comprises a stalk-shaped base member connected to a tulip-shaped head member. At least part of the stalk-shaped base member is located within at least part of a supply pipeline defining a first passage therebetween for directing a gas flow towards the head member.
  • the Coanda gas flare further comprises a slot located between the supply pipeline and the head member, substantially adjacent to where the head member is connected to the base member. The slot is surrounded by a shroud defining a second passage therebetween for directing the gas flow substantially around the tulip-shaped head member to be combusted.
  • Figure 1 shows a prior art Coanda gas flare
  • Figure 2 shows a cross-sectional view of a gas flare according to a one embodiment of the disclosure
  • 3AMEIffi0f3 ⁇ 4M JIHCT a multiphase hydrocarbon effluent into its oil, gas and water components.
  • gas effluent the effluent to be combusted
  • This liquid fraction is especially high during the flowing of high gas rate fluid at the upper operation limit of separator, or flowing bypass separator on gas-condensate wells.
  • the Coanda-type flare is often useful to combust this liquid fraction, since the gas flow ejected from the Coanda-gas flare reaches supersonic speeds. This creates Shockwaves, which atomize the liquid fraction in the gas flow into a fine mist that is more easily and completely combusted by the burner flame.
  • Figure 1 shows an example of a prior art Coanda flare having a supply pipe 1 14 connected to a tulip-shaped head member 1 10 via a base member 1 12 with pylons.
  • the tulip shape produces the Coanda effect, which is advantageous in that the waste gas flow 1 16 is directed around the bulge 108 of the tulip which causes an accelerated gas flow in this area and thus produces low pressure.
  • the gas flow is directed, by this low pressure, adjacent to the surface of the tulip-shaped head member, and also causes ambient air flow to be directed toward the low pressure.
  • ambient air flow mixes with the gas flow ejected from a slot 104 of the gas flare, making the mixture 1 17 even more suitable for combustion by the burner flame at the distal end of the head member 1 10.
  • the supply pipe 1 14 and base member 1 12 provides a first passageway there between having a particular cross-section through which the high pressured gas 116 flows. This high pressured gas flow would typically come from a well test separator gas outlet or directly from a tested well.
  • the slot 104 defines a second narrower passageway for choking the ejected gas flow between the supply pipe 1 14 and the head member 1 10. Since the second
  • 3AMEH3fOUiK3 ⁇ 4 ffiCT passageway of the slot 104 is narrower, the gas flow is accelerated to sonic speed within the slot, and furthermore (due to expansion along with the tulip) the flow reaches supersonic velocities; this produces Shockwaves that help to atomize the liquid droplets entrained by the gas flow. Then, the tulip-shaped head of the Coanda flare causes ambient air flow to mix with the combustible gas flow. This premixing allows achieving a good fuel-oxidant ratio and makes the flame more stable and clean.
  • Figure 2 shows a cross-sectional view of a gas flare according to one embodiment of the disclosure described herein.
  • Figure 2 shows a Coanda gas flare with base member 12 connected to the supply pipe 13.
  • the base member 12 may be at least partially located within a supply pipe 13.
  • the base member 12 and supply pipe 13 are shaped so as to define a passageway there between through which the gas flow is directed towards the head member 10.
  • As the gas flow reaches the head member there is a slot 4 between the supply pipe 13 and the head member 10 and base member 12.
  • the slot 4 defines a narrowed passageway for accelerating and ejecting the gas flow outside of the gas flare.
  • the directed gas flow is ejected substantially radially from the slot 4.
  • the gas flare has a shroud 14 which surrounds the slot and a portion of supply pipe and the bottom part 1 1 of the head member 10. More specifically, the shroud surrounds and yet is spaced a distance from the slot 4, to define a further passageway for the gas and aspirated air to flow around the contour of the tulip-shaped head member 10 and to mix with each other.
  • This allows for Shockwaves that aid liquid atomization, but furthermore acts as a shield in preventing particulates in the gas flow from being ejected past the shroud - which may be of danger to working nearby personnel.
  • the containment of the Shockwaves within the shroud 14 is partially responsible for the observed noise reduction in the backward direction.
  • the frusto-conical shroud 14 has an airfoil-shaped vertical cross-section with a sharp top edge 15 and a smooth bottom end 16.
  • This airfoil-shaped geometry of the shroud 14 adds additional functionality to the shroud.
  • the shroud 12 works as an efficient air ejector toward the flow of gas emitted from the slot 4.
  • the smooth and streamlined geometry of the bottom end of the shroud 14 reduces the drag effects of the inlet air.
  • the reduced area of the cross-section defined by the supply pipe 13 and shroud 14 induces acceleration of the inlet air.
  • the high velocity air flow detaches from the sharp top edge 15 of the shroud 14 and removes the portion of liquid droplets produced by atomization in the slot 4, that occasionally separate from the main gas stream.
  • top edge of shroud 14 may have a serrated rim 20.
  • serrated rim 20 are known in the designing of jet nozzles as tabs (directed inward the streamlining flow) or chevrons (sharp corner of the structure directed outward the flow). The function of this small-scale serration is for the redistribution and better atomization of liquid jets occurring on the inside surface of shroud 14 and for improving the mixing of different flows.
  • tabs Although the geometry of tabs is depicted as small sharp triangles, it should be appreciated that other shapes are possible: polygonal elements, combination of rounded elements with polygons, etc.
  • the shroud 14 is also able to absorb high-frequency noise bands resulting from the share layer and Shockwaves, for example by constructing the shroud with a sound absorption structure (porous material or honeycomb) intermediary layer.
  • a sound absorption structure porous material or honeycomb
  • the flare apparatus is equipped with a back-shield 17 for noise attenuation in the backward direction of the flare apparatus.
  • the back-shield 17 has a slightly concave geometry for improving the air inlet in the annulus defined by the bottom end 16 of the shroud and the back-shield 17.
  • the back-shield may be flat plate attached to the supply pipe 13.
  • the back-shield 17 is performed from sound-absorbing materials (similar to materials for shroud 14) with a rigid back wall for additional noise redirection towards the flame area.
  • the shroud covers a portion of the Coanda flare and is able to perform multiple functions which improve the flare.
  • the shroud may act as a protective shield to capture any debris (sand, salt deposits, etc.) that is ejected radially from the Coanda slot. It also prevents any gas or liquid from being sprayed radially in the case of an unexpected sudden flow rate spike or high liquid loading that causes the Coanda effect to break down.
  • the directed and accelerated airflow will ensure that any gas or liquid droplets, not following the Coanda profile, will be redirected in an axial direction into the combustion zone.

Landscapes

  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Nozzles (AREA)

Abstract

L'invention porte sur une torche qui est disposée à une extrémité d'un élément de tuyau d'alimentation pour diriger un écoulement de gaz vers un élément de tête, la torche comprenant une fente pour éjecter l'écoulement de gaz et un écran. L'écran entoure la fente, au moins une partie de l'élément de base et au moins une partie de l'élément de tête de la torche. L'écran dirige l'écoulement de gaz éjecté entre l'écran et l'élément de tête.
PCT/RU2012/000675 2012-08-16 2012-08-16 Brûleur à phases multiples à effet coanda à écrans WO2014027915A1 (fr)

Priority Applications (4)

Application Number Priority Date Filing Date Title
EP12891401.7A EP2885579B1 (fr) 2012-08-16 2012-08-16 Brûleur à phases multiples à effet coanda à écrans
PCT/RU2012/000675 WO2014027915A1 (fr) 2012-08-16 2012-08-16 Brûleur à phases multiples à effet coanda à écrans
NO12891401A NO2885579T3 (fr) 2012-08-16 2012-08-16
US14/421,985 US20150211735A1 (en) 2012-08-16 2012-08-16 Shrouded-coanda multiphase burner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/RU2012/000675 WO2014027915A1 (fr) 2012-08-16 2012-08-16 Brûleur à phases multiples à effet coanda à écrans

Publications (1)

Publication Number Publication Date
WO2014027915A1 true WO2014027915A1 (fr) 2014-02-20

Family

ID=50685660

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/RU2012/000675 WO2014027915A1 (fr) 2012-08-16 2012-08-16 Brûleur à phases multiples à effet coanda à écrans

Country Status (4)

Country Link
US (1) US20150211735A1 (fr)
EP (1) EP2885579B1 (fr)
NO (1) NO2885579T3 (fr)
WO (1) WO2014027915A1 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105180182A (zh) * 2015-10-13 2015-12-23 中国石油化工股份有限公司 放喷气处理用狭长孔燃烧器
GB2523020B (en) * 2012-12-06 2017-09-20 Schlumberger Holdings Multiphase flare for effluent flow

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10920979B2 (en) * 2018-04-06 2021-02-16 Zeeco, Inc. Low NOx burner and flow momentum enhancing device
US11067272B2 (en) 2019-04-24 2021-07-20 Cimarron Tandem flare

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4099908A (en) * 1976-08-13 1978-07-11 Martin Josef Beckmann Low pressure gas burner
SU987290A2 (ru) * 1981-09-04 1983-01-07 Государственный Научно-Исследовательский И Проектно-Конструкторский Институт "Южниигипрогаз" Горелка
US4486167A (en) * 1980-12-10 1984-12-04 The British Petroleum Company Limited Flare having noise attenuation
GB2225101A (en) * 1988-11-09 1990-05-23 S & C Thermofluids Ltd Hot air balloon burners
RU2315239C1 (ru) * 2006-07-27 2008-01-20 Общество с ограниченной ответственностью Финансово-промышленная компания "Космос-Нефть-Газ" Факельная горелка

Family Cites Families (35)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1737911A (en) * 1926-05-06 1929-12-03 James H Birch Vapor-oil heater
US1674631A (en) * 1926-10-28 1928-06-26 Benniger John Oil burner
FR2035265A5 (fr) * 1969-02-11 1970-12-18 Maile Hans Fabrik Gasbre
US3568792A (en) * 1969-06-18 1971-03-09 Rohr Corp Sound-suppressing and thrust-reversing apparatus
US3709654A (en) * 1969-11-19 1973-01-09 British Petroleum Co Burner
CH532752A (it) * 1971-02-25 1973-01-15 Finterm Spa Testa di combustione per bruciatori
GB1383294A (en) * 1971-04-29 1974-02-12 British Petroleum Co Flarestacks
GB1381867A (en) * 1971-04-29 1975-01-29 British Petroleum Co Flarestacks
RO54896A2 (fr) * 1971-12-13 1973-09-20
CA980258A (en) * 1973-06-14 1975-12-23 Peter Postma Exhaust gas silencer
GB1460576A (en) * 1973-09-18 1977-01-06 British Petroleum Co Flare stack burner tip
GB1593391A (en) * 1977-01-28 1981-07-15 British Petroleum Co Flare
US4021189A (en) * 1975-01-16 1977-05-03 Porta-Test Manufacturing Ltd. Gas burner
GB1551915A (en) * 1975-11-12 1979-09-05 British Petroleum Co Burner element
US4088270A (en) * 1976-03-31 1978-05-09 The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration Two dimensional wedge/translating shroud nozzle
US4137992A (en) * 1976-12-30 1979-02-06 The Boeing Company Turbojet engine nozzle for attenuating core and turbine noise
US4344751A (en) * 1979-03-24 1982-08-17 The British Petroleum Company Limited Flares
US4464110A (en) * 1980-12-10 1984-08-07 The British Petroleum Company Limited Flare using a Coanda director surface
US4486168A (en) * 1981-06-20 1984-12-04 The British Petroleum Company P.L.C. Flare
EP0153866B1 (fr) * 1984-03-02 1989-03-22 The British Petroleum Company p.l.c. Torche
US4643669A (en) * 1985-08-26 1987-02-17 Peabody Engineering Corporation Smokeless flare gas burner
US5364262A (en) * 1993-01-22 1994-11-15 Phillips Douglas E Apparatus for the early detection and relief of unsafe conditions in a gaseous system
DE19859829A1 (de) * 1998-12-23 2000-06-29 Abb Alstom Power Ch Ag Brenner zum Betrieb eines Wärmeerzeugers
KR100413057B1 (ko) * 2000-08-22 2003-12-31 한국과학기술연구원 토네이도의 원리를 이용한 그라운드 플레어의 소각 용량증대방법 및 그 장치
US7175423B1 (en) * 2000-10-26 2007-02-13 Bloom Engineering Company, Inc. Air staged low-NOx burner
US7484929B1 (en) * 2004-07-09 2009-02-03 Loren Cook Company Exhaust fan systems
US20060105276A1 (en) * 2004-11-16 2006-05-18 James Wilkins Linear Coanda flare methods and apparatus
US7354265B2 (en) * 2004-12-02 2008-04-08 Saudi Arabian Oil Company Flare stack combustion method and apparatus
US7878798B2 (en) * 2006-06-14 2011-02-01 John Zink Company, Llc Coanda gas burner apparatus and methods
US8857733B1 (en) * 2009-01-14 2014-10-14 Resodyn Corporation Flameless thermal spray system using flame heat source
US20150316257A1 (en) * 2012-12-06 2015-11-05 Roman Alexandrovich Skachkov Multiphase flare for effluent flow
US9970658B2 (en) * 2013-01-18 2018-05-15 Steffes Corporation Pressure relief valve with rotating damper
US20140329185A1 (en) * 2013-05-03 2014-11-06 Uop Llc Apparatus and method for minimizing smoke formation in a flaring stack
US20140329186A1 (en) * 2013-05-03 2014-11-06 Uop Llc Apparatus and method for minimizing smoke formation in a flaring stack
US9470418B2 (en) * 2014-06-05 2016-10-18 David Bacon Gas assist assembly for use with a waste gas flare stack

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4099908A (en) * 1976-08-13 1978-07-11 Martin Josef Beckmann Low pressure gas burner
US4486167A (en) * 1980-12-10 1984-12-04 The British Petroleum Company Limited Flare having noise attenuation
SU987290A2 (ru) * 1981-09-04 1983-01-07 Государственный Научно-Исследовательский И Проектно-Конструкторский Институт "Южниигипрогаз" Горелка
GB2225101A (en) * 1988-11-09 1990-05-23 S & C Thermofluids Ltd Hot air balloon burners
RU2315239C1 (ru) * 2006-07-27 2008-01-20 Общество с ограниченной ответственностью Финансово-промышленная компания "Космос-Нефть-Газ" Факельная горелка

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP2885579A4 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2523020B (en) * 2012-12-06 2017-09-20 Schlumberger Holdings Multiphase flare for effluent flow
CN105180182A (zh) * 2015-10-13 2015-12-23 中国石油化工股份有限公司 放喷气处理用狭长孔燃烧器

Also Published As

Publication number Publication date
EP2885579A4 (fr) 2015-08-05
EP2885579A1 (fr) 2015-06-24
NO2885579T3 (fr) 2017-12-16
US20150211735A1 (en) 2015-07-30
EP2885579B1 (fr) 2017-07-19

Similar Documents

Publication Publication Date Title
US20150316257A1 (en) Multiphase flare for effluent flow
EP2885579B1 (fr) Brûleur à phases multiples à effet coanda à écrans
CA1149731A (fr) Capteur de particules sur echappement de moteur a combustion interne
RU2622353C1 (ru) Блок горелки для сжигания низкокалорийных газов
EP2383425A2 (fr) Ensemble formant doseur
Nie et al. Optimization of spraying dust reduction technology of continuous miner machine and the dust environment in a tunnel, based on computational fluid dynamics (CFD) technology
EA001591B1 (ru) Способ удаления газообразного компонента из текучей среды
BRPI0612038B1 (pt) High speed low pressure issuer
US10281147B2 (en) Housing assembly for a flare tip apparatus for use on a waste gas flare stack
CN108005598B (zh) 一种矿山钻孔用气射流除尘器
US3749377A (en) Orifice scrubber for removing solid particles from high pressure gas
US4319647A (en) Flame drill channelling method and apparatus for reducing noise and dust levels
JP2024512208A (ja) 大気汚染物質吸入除去用ベンチュリ型複合ノズル装置
US10288283B2 (en) Multiphase burner
RU156921U1 (ru) Пылеулавливающая установка для станков термохимического бурения и термического расширения скважин
CN116867559A (zh) 大气污染物质吸入及清除用文丘里式复合喷嘴装置
RU2056178C1 (ru) Вихревой пылеуловитель
RU2552860C1 (ru) Генератор высокократной пены для пожаротушения
KR102575349B1 (ko) 대기오염물질 흡입 제거용 벤투리형 복합노즐장치
Widger Improvement of high pressure water sprays used for coal dust extraction in mine safety
RU2524070C1 (ru) Устройство для разработки и удаления грунта под водой
US7073612B2 (en) Surge device for air drilling
Hou et al. Effects of structural parameters of pressure-swirl nozzle on atomization and dust removal characteristics
RU16181U1 (ru) Устройство для пылеподавления
JP2005537827A (ja) 液体防護壁を発生させる装置および方法

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 12891401

Country of ref document: EP

Kind code of ref document: A1

REEP Request for entry into the european phase

Ref document number: 2012891401

Country of ref document: EP

WWE Wipo information: entry into national phase

Ref document number: 2012891401

Country of ref document: EP

NENP Non-entry into the national phase

Ref country code: DE

WWE Wipo information: entry into national phase

Ref document number: 14421985

Country of ref document: US