WO2011059417A1 - Pressurized premixing of gases in an injector - Google Patents

Pressurized premixing of gases in an injector Download PDF

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Publication number
WO2011059417A1
WO2011059417A1 PCT/US2009/006037 US2009006037W WO2011059417A1 WO 2011059417 A1 WO2011059417 A1 WO 2011059417A1 US 2009006037 W US2009006037 W US 2009006037W WO 2011059417 A1 WO2011059417 A1 WO 2011059417A1
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WO
WIPO (PCT)
Prior art keywords
primary
flow
injector
conduit
gas flow
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.)
Ceased
Application number
PCT/US2009/006037
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French (fr)
Inventor
Benjamin P. Lacy
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.)
UTC Power Corp
Original Assignee
UTC Power 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 UTC Power Corp filed Critical UTC Power Corp
Priority to PCT/US2009/006037 priority Critical patent/WO2011059417A1/en
Publication of WO2011059417A1 publication Critical patent/WO2011059417A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/10Mixing gases with gases
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/313Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/313Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit
    • B01F25/3133Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit characterised by the specific design of the injector
    • B01F25/31331Perforated, multi-opening, with a plurality of holes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/314Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/314Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
    • B01F25/3142Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit the conduit having a plurality of openings in the axial direction or in the circumferential direction
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/314Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
    • B01F25/3142Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit the conduit having a plurality of openings in the axial direction or in the circumferential direction
    • B01F25/31425Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit the conduit having a plurality of openings in the axial direction or in the circumferential direction with a plurality of perforations in the axial and circumferential direction covering the whole surface
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04089Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Definitions

  • a primary gas is injected into and mixed with a secondary gas in response to pressure of the primary gas forcing it through premix holes into the secondary gas upstream of the injector holes, which provides a high degree of mixing at relatively low pressure drop across a wide range of flow rates.
  • An example of the mixing of two gases is the mixing of air with fuel cell power plant anode exhaust for combustion in a downstream catalytic burner.
  • the normal method of mixing these gases is to use a static mixing device downstream of the injection location, to mix the gases well. Suitable commercial static mixers are costly.
  • An alternative method is to inject the gas through many small holes at high velocity, relying on the number of holes and the velocity to mix the flows. However, this results either in a large pressure drop at the highest injection flow rates, or it results in poor mixing at the lowest injection rates, depending on how the holes are sized. It is desirable to have a mixing injector for two gases that operates within the necessary parameters across a wide range of operating conditions which are likely to occur in the environment of use.
  • An injector mixes a secondary gas, such as fuel cell power plant anode exhaust, with a primary gas, such as air, for combustion in a catalytic burner in a fuel processing system.
  • a secondary gas such as fuel cell power plant anode exhaust
  • a primary gas such as air
  • the mixing injector disclosed herein uses an excess of pressure in the primary flow versus secondary flow to force some primary flow into the secondary flow, upstream of the point of injecting the secondary flow into the primary flow through the injector holes.
  • a back pressure is provided to the primary stream by restricting the flow of the primary stream just upstream of the injector, by means of some form of blockage which is described in more detail with respect to the figures, hereinafter.
  • the premixing injector system improves mixing in two ways. First, the premixing itself provides additional mixing of the primary gas and the secondary gas. Second, the premixed secondary gas, having itself more flow momentum than the primary gas causes the combined primary gas and secondary gas mixture in the injector to have a greater flow momentum than would the secondary gas by itself. Therefore, the gas passing through the injector holes has a greater cross-flow penetration, which provides an additional improvement in mixing.
  • the amount of premixing is a function of how much primary gas is forced to mix with the secondary gas upstream of the injector holes.
  • the pressurized premixing injector may be used in a large variety of manners.
  • the primary gas stream may be the anode effluent, and the secondary gas stream be the air to mix therewith, for combustion.
  • the primary stream may be high pressure air and the secondary stream might be the output of a shift converter, to provide a gas mixture for processing in a preferential oxidizer (PROX).
  • PROX preferential oxidizer
  • the secondary gas flow may be reversed.
  • the primary gas flow is the higher pressure fluid.
  • the sizing of the premix holes and the injector holes are the critical performance features in determining the amount of premixing and hence the performance improvement. This sizing can be achieved using pressure drop
  • Fig. 1 is a partially broken away perspective view of a first premixing injector embodiment.
  • Fig. 2 is a partially broken away perspective view of a second premixing injector embodiment.
  • FIG. 3 is a highly simplified schematic diagram of a third embodiment.
  • a first embodiment of a premixing injector 12 includes a secondary flow conduit or pipe 14 that is disposed within an injector conduit or pipe 15 that is fed primary gas flow from a primary flow conduit or pipe 17 which is connected to the injector pipe 14 at a Y-joint 20.
  • the secondary flow pipe 14 is sealed within the injector pipe 15 at the inlet end of the pipe, such as a ring 22 bonded to the injector pipe 14 and 15 in any suitable fashion. Not shown for simplicity are spacers to maintain the central spacing of the secondary flow pipe 14 within the injector pipe 15.
  • a blockage 25 is disposed on the injector pipe 14.
  • the primary gas flow, being obstructed by the blockage 25, creates a greater pressure upstream of the blockage 25 (to the right as seen in Fig. 1 ) in contrast with the primary gas stream pressure downstream of the blockage 25.
  • the portion of primary gas flow that enters the injector pipe through the holes 27 is mixed with the secondary flow as it proceeds toward the injector passages, such as holes 28 provided in the secondary flow pipe 14.
  • the secondary flow pipe 14 is blocked off in any suitable fashion, such as by an end plate 31 suitably bonded thereto by any appropriate process; the end plate 31 acts as a diffuser.
  • the premixture flowing within the secondary flow pipe 14 is injected outwardly into the primary gas that flows past the obstruction 25 so as to cause significant additional mixing.
  • the obstruction 25 causes a portion of the primary flow to enter through the premix holes 27 to mix with the secondary flow and thus have a somewhat higher secondary mass flow, so the premixed gas reaching the injector holes 28 has a higher ratio of momentum relative to the primary gas flow passing the obstruction 25. This provides greater cross flow penetration resulting in better mixing.
  • the premixing itself provides more thorough mixing of the primary gas and the secondary gas, but in addition, the combined primary and secondary gas mixture in the injector has an increased momentum ratio relative to the primary flow just outside the injector holes 28, so a greater cross flow penetration results in better mixing, as well.
  • FIG. 2 A simpler embodiment is illustrated in Fig. 2.
  • the primary flow pipe 17a is unaltered except for allowing the secondary flow pipe 14a to be inserted within the primary flow pipe 17a.
  • the secondary flow pipe 14a has an increased diameter premix/injector section 30 which is blocked off at its end 31.
  • the premix/injector section 30 has a ring 33 of premix holes 34.
  • the ring 33 also provides an obstruction to the primary flow to increase the upstream pressure above the pressure downstream of the injector section 30 sufficiently to cause significant flow through the premix holes 34 into the premixer 30.
  • the premix gas in the injector 30 is injected into the primary flow through injection holes 37. As before, the premixing not only provides more thorough mixing, but it also increases the flow penetration through the injector holes due to the increased pressure.
  • a pressure restriction 42 may be a plate with holes in it, or some other combination of flow inhibitors, to ensure that the pressure upstream thereof is higher than the pressure of the primary flow at the injector holes 43. At the higher pressure, some of the primary flow will pass through the premix holes 45 and the premixture will thereafter be injected downstream of the pressure restriction 42 through the premix holes 43.
  • the term "primary flow” means the one that will be injected into the other one by means of the pressure differential at the premixing holes, and the secondary flow is defined as the one that, following being mixed with the primary flow, is injected into the primary flow. Which of two gases will be chosen as primary, and which of two gases will be chosen as secondary depends much on the purposes, gas characteristics and pressure considerations of the particular use.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)

Abstract

A pressure induced premixing injector (12) for mixing a secondary gas (14, 14a, 14b) into a primary gas (17, 17a, 17b) includes a flow restriction (25, 33, 42) in the primary conduit with premix holes (27, 34, 35) upstream thereof allowing a portion of primary gas to flow into secondary gas to form a premix gas and injector holes (28, 37, 43) downstream thereof allowing premix gas to flow into the unmixed portion of primary gas.

Description

Pressurized Premixing of Gases in an Injector
Technical Field
[0001] A primary gas is injected into and mixed with a secondary gas in response to pressure of the primary gas forcing it through premix holes into the secondary gas upstream of the injector holes, which provides a high degree of mixing at relatively low pressure drop across a wide range of flow rates.
Background Art
[0002] An example of the mixing of two gases is the mixing of air with fuel cell power plant anode exhaust for combustion in a downstream catalytic burner. The normal method of mixing these gases is to use a static mixing device downstream of the injection location, to mix the gases well. Suitable commercial static mixers are costly. An alternative method is to inject the gas through many small holes at high velocity, relying on the number of holes and the velocity to mix the flows. However, this results either in a large pressure drop at the highest injection flow rates, or it results in poor mixing at the lowest injection rates, depending on how the holes are sized. It is desirable to have a mixing injector for two gases that operates within the necessary parameters across a wide range of operating conditions which are likely to occur in the environment of use.
Summary
[0003] An injector mixes a secondary gas, such as fuel cell power plant anode exhaust, with a primary gas, such as air, for combustion in a catalytic burner in a fuel processing system. The mixing injector disclosed herein uses an excess of pressure in the primary flow versus secondary flow to force some primary flow into the secondary flow, upstream of the point of injecting the secondary flow into the primary flow through the injector holes.
[0004] A back pressure is provided to the primary stream by restricting the flow of the primary stream just upstream of the injector, by means of some form of blockage which is described in more detail with respect to the figures, hereinafter. The premixing injector system improves mixing in two ways. First, the premixing itself provides additional mixing of the primary gas and the secondary gas. Second, the premixed secondary gas, having itself more flow momentum than the primary gas causes the combined primary gas and secondary gas mixture in the injector to have a greater flow momentum than would the secondary gas by itself. Therefore, the gas passing through the injector holes has a greater cross-flow penetration, which provides an additional improvement in mixing.
[0005] The amount of premixing is a function of how much primary gas is forced to mix with the secondary gas upstream of the injector holes.
This can be controlled several ways: by the relative size difference of the two pipes, the number and size of premixer holes, and pressure
differentials between the primary gas and the secondary gas, such as by blockage in the primary gas flow. Ultimately, all of the primary gases can be forced into the secondary gas, improving mixing at a cost of increased pressure drop, allowing control over the degree of mixing versus the allowable pressure drop.
[0006] In one sample application using the device illustrated in Fig. 1 , it was shown that the disparity (unmixedness) at entrance to the diffuser (31 , Fig. 1) decreases by about 70% with a pressure drop increase of only 14%, compared to when the secondary gas is injected without pressure-induced premixing of the primary gas.
[0007] The pressurized premixing injector may be used in a large variety of manners. For instance, the primary gas stream may be the anode effluent, and the secondary gas stream be the air to mix therewith, for combustion. Also, the primary stream may be high pressure air and the secondary stream might be the output of a shift converter, to provide a gas mixture for processing in a preferential oxidizer (PROX). And if desired in any given utilization, the roles of primary gas flow and
secondary gas flow may be reversed. Normally, the primary gas flow is the higher pressure fluid.
[0008] In the pressure-induced premixing injector, the sizing of the premix holes and the injector holes are the critical performance features in determining the amount of premixing and hence the performance improvement. This sizing can be achieved using pressure drop
calculations of the different flow streams to determine the flow through the premixer holes.
[0009] Other variations will become more apparent in the light of the following detailed description of exemplary embodiments, as illustrated in the accompanying drawings.
Brief Description of the Drawings
[0010] Fig. 1 is a partially broken away perspective view of a first premixing injector embodiment.
[0011] Fig. 2 is a partially broken away perspective view of a second premixing injector embodiment.
[0012] Fig. 3 is a highly simplified schematic diagram of a third embodiment.
Mode(s) of Implementation
[0013] Referring to Fig. 1 , a first embodiment of a premixing injector 12 includes a secondary flow conduit or pipe 14 that is disposed within an injector conduit or pipe 15 that is fed primary gas flow from a primary flow conduit or pipe 17 which is connected to the injector pipe 14 at a Y-joint 20. The secondary flow pipe 14 is sealed within the injector pipe 15 at the inlet end of the pipe, such as a ring 22 bonded to the injector pipe 14 and 15 in any suitable fashion. Not shown for simplicity are spacers to maintain the central spacing of the secondary flow pipe 14 within the injector pipe 15.
[0014] To maintain pressure within the injector, suitable to cause premixing, a blockage 25 is disposed on the injector pipe 14. The primary gas flow, being obstructed by the blockage 25, creates a greater pressure upstream of the blockage 25 (to the right as seen in Fig. 1 ) in contrast with the primary gas stream pressure downstream of the blockage 25. This forces some of the primary flow through premixing passages, such as holes 27 in the secondary flow pipe 14. The portion of primary gas flow that enters the injector pipe through the holes 27 is mixed with the secondary flow as it proceeds toward the injector passages, such as holes 28 provided in the secondary flow pipe 14. [0015] The secondary flow pipe 14 is blocked off in any suitable fashion, such as by an end plate 31 suitably bonded thereto by any appropriate process; the end plate 31 acts as a diffuser. The premixture flowing within the secondary flow pipe 14 is injected outwardly into the primary gas that flows past the obstruction 25 so as to cause significant additional mixing. The obstruction 25 causes a portion of the primary flow to enter through the premix holes 27 to mix with the secondary flow and thus have a somewhat higher secondary mass flow, so the premixed gas reaching the injector holes 28 has a higher ratio of momentum relative to the primary gas flow passing the obstruction 25. This provides greater cross flow penetration resulting in better mixing. Thus, the premixing itself provides more thorough mixing of the primary gas and the secondary gas, but in addition, the combined primary and secondary gas mixture in the injector has an increased momentum ratio relative to the primary flow just outside the injector holes 28, so a greater cross flow penetration results in better mixing, as well.
[0016] A simpler embodiment is illustrated in Fig. 2. Therein, the primary flow pipe 17a is unaltered except for allowing the secondary flow pipe 14a to be inserted within the primary flow pipe 17a. The secondary flow pipe 14a has an increased diameter premix/injector section 30 which is blocked off at its end 31. At the upstream end, the premix/injector section 30 has a ring 33 of premix holes 34. The ring 33 also provides an obstruction to the primary flow to increase the upstream pressure above the pressure downstream of the injector section 30 sufficiently to cause significant flow through the premix holes 34 into the premixer 30. The premix gas in the injector 30 is injected into the primary flow through injection holes 37. As before, the premixing not only provides more thorough mixing, but it also increases the flow penetration through the injector holes due to the increased pressure.
[0017] Perhaps the simplest embodiment is that illustrated, in
schematic form, in Fig. 3. In Fig. 3, the secondary gas flow pipe 14b is fitted with the primary gas flow pipe 17b, and is blocked off at its
downstream end 39 so as to form an injector 40. A pressure restriction 42 may be a plate with holes in it, or some other combination of flow inhibitors, to ensure that the pressure upstream thereof is higher than the pressure of the primary flow at the injector holes 43. At the higher pressure, some of the primary flow will pass through the premix holes 45 and the premixture will thereafter be injected downstream of the pressure restriction 42 through the premix holes 43. The effects are the same as with the previous embodiments.
[0018] As the terms are used herein, the term "primary flow" means the one that will be injected into the other one by means of the pressure differential at the premixing holes, and the secondary flow is defined as the one that, following being mixed with the primary flow, is injected into the primary flow. Which of two gases will be chosen as primary, and which of two gases will be chosen as secondary depends much on the purposes, gas characteristics and pressure considerations of the particular use.
[0019] Instead of flow restrictions 25, 33, 42, the requisite amount of pressure may be created by adjusting sizes of the pipes involved.
However, it is possible that pipe size restrictions might impede the free premixing and injection processes thereby reducing the mixing value of the configuration.

Claims

Claims
1. A method of mixing a secondary gas flow from a secondary gas conduit (14, 14a, 14b) into a primary gas flow provided by a primary gas conduit (17, 17a, 17b),
characterized by:
partially obstructing (25, 33, 42) the primary gas flow and conducting (27, 33, 45) a portion of the primary gas flow, from a point upstream of where the primary gas flow is partially obstructed, into the secondary gas flow at a point downstream of where the primary gas flow is partially obstructed, to form a premixed gas flow; and
injecting (28, 37, 43) the premixed gas flow into a non-mixed portion of the primary gas flow.
2. A method according to claim 1 further characterized in that: said step of injecting comprises injecting (28, 37, 43) the premixed gas flow into a non-mixed portion of the primary gas flow at a point downstream of where the primary gas flow is partially obstructed.
3. Apparatus comprising:
a primary conduit (17, 17a, 17b) for a primary gas flow;
a secondary conduit ( 4, 14a, 14b) for a secondary gas flow;
an injector (15, 30, 40) having injection passages (28, 37, 43) configured to inject said secondary gas flow into said primary gas flow;
characterized by:
a flow restriction (25, 33, 42) in said primary conduit; and
a plurality of premix passages (27, 34, 45) configured to flow a portion of said primary gas upstream of said flow restriction into said flow of secondary gas downstream of said flow restriction;
said injection passages being disposed downstream of said flow restriction.
4. Apparatus according to claim 3 further characterized in that: said secondary conduit (14) is disposed within said injector (15) and has a fluid seal (22) to the injector at the upstream end of the injector;
said primary conduit (17) directing the primary gas flow into space between said injector and said secondary conduit;
said flow restriction comprising a ring (25) extending outward from the secondary conduit;
the premix passages (27) being upstream of the ring;
the secondary conduit being sealed off (31) at its downstream end with the injector passages (28) located between the ring and the downstream end.
5. Apparatus according to claim 3 further characterized in that: the secondary conduit (14a) comprises an elbow terminating within the primary conduit (17a);
the injector (30) comprises an extension of the secondary conduit having a diameter larger than the secondary conduit but smaller than the primary conduit, forming the flow restriction (33) and the premix passages (34) in a ring extending between the secondary conduit and the injector; the injector having a fluid seal (31) at its downstream end with the injection passages (37) being adjacent the seal.
6. Apparatus according to claim 3 further characterized in that: the primary flow conduit (17b) includes an elbow leading it into an end of the secondary conduit (14b), the end of the secondary conduit being sealed (39) to the primary conduit;
the flow restriction (42) being disposed between the premix passages
(45) upstream thereof and the injection passages (28, 37, 43) downstream thereof.
PCT/US2009/006037 2009-11-10 2009-11-10 Pressurized premixing of gases in an injector Ceased WO2011059417A1 (en)

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Cited By (8)

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Publication number Priority date Publication date Assignee Title
JP2013063393A (en) * 2011-09-16 2013-04-11 Jfe Steel Corp Gas mixing structure
CN105546349A (en) * 2015-12-09 2016-05-04 无锡拓能自动化科技有限公司 Gas filling pipe applied to gas filling station
CN105546348A (en) * 2015-12-09 2016-05-04 无锡拓能自动化科技有限公司 Efficient mixed gas filling pipeline applied to gas filling station
CN107252640A (en) * 2017-06-23 2017-10-17 东风商用车有限公司 Pipeline fluid mixer assembly
CN107261873A (en) * 2017-06-23 2017-10-20 东风商用车有限公司 Pipeline fluid mixer structure
CN114738748A (en) * 2022-05-17 2022-07-12 陕西环通标准锅炉有限公司 Channel type rectangular array gas mixer
WO2024116103A1 (en) * 2022-11-30 2024-06-06 Breath Of Health Ltd. Method and system for detecting non-volatile and semi-volatile organic compounds in mid-ir spectrometry gas cell configurations
AT527036B1 (en) * 2023-06-16 2024-10-15 Avl List Gmbh gas mixing system for a fuel cell system

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JPH0945350A (en) * 1995-07-28 1997-02-14 Toshiba Corp Fuel cell power plant
US6303243B1 (en) * 1998-07-31 2001-10-16 Sulzer Hexis Ag Plant with high temperature fuel cells II
KR20080038229A (en) * 2005-08-16 2008-05-02 에너다이 게엠베하 How fuel cell systems and reformers work
JP2008533656A (en) * 2005-03-09 2008-08-21 ベバスト・アクチィエンゲゼルシャフト Reformer, fuel cell system, and method of operating fuel cell system

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Publication number Priority date Publication date Assignee Title
JPH0945350A (en) * 1995-07-28 1997-02-14 Toshiba Corp Fuel cell power plant
US6303243B1 (en) * 1998-07-31 2001-10-16 Sulzer Hexis Ag Plant with high temperature fuel cells II
JP2008533656A (en) * 2005-03-09 2008-08-21 ベバスト・アクチィエンゲゼルシャフト Reformer, fuel cell system, and method of operating fuel cell system
KR20080038229A (en) * 2005-08-16 2008-05-02 에너다이 게엠베하 How fuel cell systems and reformers work

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013063393A (en) * 2011-09-16 2013-04-11 Jfe Steel Corp Gas mixing structure
CN105546349A (en) * 2015-12-09 2016-05-04 无锡拓能自动化科技有限公司 Gas filling pipe applied to gas filling station
CN105546348A (en) * 2015-12-09 2016-05-04 无锡拓能自动化科技有限公司 Efficient mixed gas filling pipeline applied to gas filling station
CN107252640A (en) * 2017-06-23 2017-10-17 东风商用车有限公司 Pipeline fluid mixer assembly
CN107261873A (en) * 2017-06-23 2017-10-20 东风商用车有限公司 Pipeline fluid mixer structure
CN107261873B (en) * 2017-06-23 2023-06-02 东风商用车有限公司 Pipeline fluid mixer structure
CN107252640B (en) * 2017-06-23 2023-06-27 东风商用车有限公司 Pipeline fluid mixer assembly
CN114738748A (en) * 2022-05-17 2022-07-12 陕西环通标准锅炉有限公司 Channel type rectangular array gas mixer
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