US20200061572A1 - Aerosol Generator, In Particular Soot Generator - Google Patents
Aerosol Generator, In Particular Soot Generator Download PDFInfo
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- US20200061572A1 US20200061572A1 US16/666,724 US201916666724A US2020061572A1 US 20200061572 A1 US20200061572 A1 US 20200061572A1 US 201916666724 A US201916666724 A US 201916666724A US 2020061572 A1 US2020061572 A1 US 2020061572A1
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- Prior art keywords
- combustion chamber
- aerosol generator
- feed lines
- generator according
- end portions
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- 239000000443 aerosol Substances 0.000 title claims abstract description 35
- 239000004071 soot Substances 0.000 title claims abstract description 30
- 239000007789 gas Substances 0.000 claims abstract description 54
- 238000002485 combustion reaction Methods 0.000 claims abstract description 43
- 239000012530 fluid Substances 0.000 claims abstract description 39
- 239000000446 fuel Substances 0.000 claims abstract description 21
- 239000007800 oxidant agent Substances 0.000 claims abstract description 11
- 239000011261 inert gas Substances 0.000 claims description 13
- 230000001590 oxidative effect Effects 0.000 claims description 11
- 238000012856 packing Methods 0.000 claims description 4
- 239000002245 particle Substances 0.000 description 40
- 238000000034 method Methods 0.000 description 13
- 239000000203 mixture Substances 0.000 description 12
- 239000000126 substance Substances 0.000 description 7
- HSFWRNGVRCDJHI-UHFFFAOYSA-N Acetylene Chemical compound C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 239000001257 hydrogen Substances 0.000 description 6
- 229910052739 hydrogen Inorganic materials 0.000 description 6
- 229910052799 carbon Inorganic materials 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 4
- 150000002431 hydrogen Chemical class 0.000 description 4
- 230000008929 regeneration Effects 0.000 description 4
- 238000011069 regeneration method Methods 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 239000005864 Sulphur Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 125000005842 heteroatom Chemical group 0.000 description 1
- 238000010982 kinetic investigation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229910052756 noble gas Inorganic materials 0.000 description 1
- 150000002835 noble gases Chemical class 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000004088 simulation Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000010200 validation analysis Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/0095—Preparation of aerosols
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/05—Preparation or purification of carbon not covered by groups C01B32/15, C01B32/20, C01B32/25, C01B32/30
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/44—Carbon
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/44—Carbon
- C09C1/48—Carbon black
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/20—Non-premix gas burners, i.e. in which gaseous fuel is mixed with combustion air on arrival at the combustion zone
- F23D14/22—Non-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
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N15/00—Investigating characteristics of particles; Investigating permeability, pore-volume or surface-area of porous materials
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N15/00—Investigating characteristics of particles; Investigating permeability, pore-volume or surface-area of porous materials
- G01N15/10—Investigating individual particles
- G01N15/1012—Calibrating particle analysers; References therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00157—Controlling the temperature by means of a burner
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00164—Controlling or regulating processes controlling the flow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/24—Stationary reactors without moving elements inside
Definitions
- the invention relates to an aerosol generator, in particular a soot generator, and a method for creating an aerosol, in particular a method for creating soot.
- particle-reducing components are used, such as filter systems and/or catalytic converters.
- the filter systems that are used today differ essentially by the type of regeneration (burning off of the soot) they employ. Active regeneration is the term used here for the deliberate burning off of the soot for a limited time and passive regeneration is the term used here for the continuous breakdown of soot, ideally in dynamic equilibrium.
- model soots and actual soots are used for the technical testing of the filtering efficiency or the reactivity of soots.
- various particle measuring techniques which determine the particle mass and the number of particles, are used for testing the legally limited emission of particles.
- soot generators are used for producing soot particles.
- EP 0 353 746 A2 describes a device that creates soot particles by a spark discharge at graphite electrodes.
- U.S. Pat. No. 4,751,069 A describes a system for creating soot particles by cracking carbon-containing materials at high temperatures.
- EP 1 055 877 B1 describes a burner for creating soot particles that burns a combustible gas and an oxidizing gas in a combustion chamber. A refinement of this burner is described in EP 1 590 408 B 1. A further refinement is described in WO 2014/085941 A1, which describes the use of a liquid fuel for creating soot particles.
- a disadvantage of the known devices is that the chemical composition of the particles and also the particle morphology, i.e. the size and nature of the particles created of the aerosol, cannot be influenced, or influenced only to a limited extent.
- An object of the invention is providing an improved device for creating model aerosols, in particular soot, with which disadvantages of conventional techniques can be avoided.
- An object of the invention is providing an aerosol generator, in particular a soot generator that makes it possible to exert a direct influence on the chemical composition and/or morphology of the particles created.
- a further object is that of providing a method for creating an aerosol or soot with which disadvantages of conventional methods can be avoided.
- an aerosol generator in particular a soot generator, comprises a combustion chamber, in which fuel can be burned with an oxidizing agent in at least one soot-particle-creating flame, and a fluid feeding device for feeding fuel and an oxidizing agent into the combustion chamber.
- the fluid feeding device is distinguished by the fact that the fluid feeding device has at least three feed lines for a fluid, the outlet-side end portions of which are parallel, so that at least three fluids of different types, in particular gases, can be introduced into the combustion chamber unmixed and in a parallel inflow direction.
- the fluids, in particular gases, are consequently conducted separately into the combustion chamber and to the flame.
- the inflow direction is the average direction of flow of the fluid stream that flows out at the outlet of the feed line and enters the combustion chamber.
- This arrangement of the feed lines offers the advantage that a number of combustible gases and/or oxidizing gases of different types and/or inert gases can be conducted into a combustion chamber.
- the combination of at least three feed lines and a parallel inflow direction makes a flexible combination and composition of the components of the gas mixture that can be burned in the flame possible, in order to bring about a desired particle morphology and/or chemical composition of the particles.
- the end portions of the at least three feed lines may be arranged coaxially in one another.
- the end portions have diameters of different sizes and are arranged nested coaxially in one another. This makes a compact arrangement of the end portions of the feed lines possible, in order to introduce the different gases into the combustion chamber as far as possible at the same point, or at the point at which the flame is created.
- the end portions may be arranged lying parallel next to one another.
- this embodiment can be produced with little effort.
- the end portions are arranged parallel next to one another to form an arrangement of lines with a packing density that is as great as possible.
- the fluid feeding device has at least four feed lines.
- at least two different combustible gases, an oxidizing gas and a further inert gas or reactive gas can be introduced into the combustion chamber.
- a reactive gas is a gas with so-called heteroatoms (non-carbon atoms), such as for example nitrogen, sulphur or other elements.
- these reactive gases can act as an oxidizing agent (for example S 0 2 , N 0 2 ) or as a reducing agent (for example NH 3 , H 2 S, N 2 O).
- a variant of this embodiment therefore provides that the fluid feeding device has four or more feed lines.
- a further advantageous variant of this embodiment provides that the fluid feeding device has seven feed lines.
- This variant offers still greater flexibility in setting the composition of the gas mixture that is burned in the flame.
- a further advantage is that, with seven feed lines, their seven parallel end portions can be arranged with a packing density that is as great as possible. For this purpose, the end portions are arranged parallel next to one another, one of the end portions being arranged in the middle, while the six remaining end portions are arranged uniformly distributed around the circumference and at as little distance as possible from the end portion that is arranged in the middle.
- outlets of the feed lines are located at the same height with respect to the inflow direction, so that the gases are introduced into the combustion chamber as close to one another as possible and as far as possible mix at the same time.
- a first of the feed lines is connected on the inlet side to a first fluid container (fuel container), containing a first fuel. Furthermore, a second of the feed lines is connected on the inlet side to a second fluid container (fuel container), containing a second fuel.
- the first fuel may be a first combustible gas and the second fuel may be a second combustible gas that is different from the first combustible gas. Examples of such combustible gases are hydrogen (H 2 ), propane (C 3 H 8 ) or ethine or acetylene (C 2 H 2 ).
- a further advantageous possibility for realizing the invention is a third of the feed lines are connected on the inlet side to a third fluid container containing an oxidizing gas
- a third fluid container containing an oxidizing gas Likewise possible is the use of one or more oxidizing gases with different oxygen components, for example air, oxygen, or ozone, which are conducted into the combustion chamber by way of separate feed lines in each case.
- at least two feed lines of the fluid feeding device are connected on the inlet side in each case to respective a container that contains an oxidizing gas, different oxidizing gases being stored in the containers.
- At least one of the feed lines may be connected on the inlet side to a fluid container, which contains a reactive gas. In this way, one or more different reactive gases can be introduced into the combustion chamber.
- the aerosol generator may be formed such that at least one of the feed lines is connected on the inlet side to a fluid container, which contains a so-called inert gas.
- Inert gases are distinguished by the fact that they do not take part directly in the combustion. Possible inert gases are, for example, N 2 , CO 2 or noble gases. In this way, one or more different inert gases can be introduced into the combustion chamber, in order to influence the physical-chemical boundary conditions of the combustion, and as a result the particle morphology.
- the aerosol generator may have a regulator, by which a fluid flow rate can be set in each of the feed lines.
- the regulator may for example be a valve arrangement, such that each feed line has at least one valve, by which a flow rate through the feed line can be set.
- the acetylene component in the combustible gas mixture leads to a greater carbon component in the combustible gas, and consequently to a greater formation of soot in the flame.
- Increasing the hydrogen component leads to a greater carbon component in the particles formed.
- the use of pure hydrogen leads to a flame that is free from soot.
- the emission of particles may be caused for example by other reactive or inert gas components, for example sulphur-containing particles due to the use of S 0 2 and/or H 2 S.
- a method for creating an aerosol in particular a method for creating soot, is provided, in which method at least one fuel and an oxidizing agent are fed to a combustion chamber by an aerosol generator as disclosed in this document, and a soot-particle-creating flame, in particular a diffusion flame, is formed in the combustion chamber.
- An advantageous variant provides here that, by an aerosol generator with at least four feed lines, at least two combustible gases, at least one oxidizing gas and at least one reactive gas or inert gas are introduced into the combustion chamber.
- the invention also relates to a method for testing or calibrating a particle measuring device, particle sensor, particle filter or particle catalyst, characterized in that, for testing or calibrating such a device, it is fed an aerosol, in particular soot particles, which are created by an aerosol generator as disclosed in this document or by means of a method as disclosed in this document.
- FIG. 1 is a schematic representation of a soot generator
- FIGS. 2A and 2B are sectional views of an outlet-side end portion of the fluid feeding device.
- FIG. 3 is a sectional view of an outlet-side end portion of the fluid feeding device.
- FIG. 1 schematically shows a cross section of an exemplary embodiment of the soot generator 1 according to the invention.
- the soot generator represented in FIG. 1 comprises a combustion chamber 7 , in which at least one fuel with an oxidizing agent can be burned in at least one soot-particle-creating flame 10 .
- the combustion chamber 7 may be embodied in a way known per se and be formed for example by a cylindrical outer tube 6 , at the lower end of which an end portion of a fluid feeding device 2 protrudes into the combustion chamber 7 .
- the fluid feeding device 2 can be used for introducing combustible gases, an oxidizing gas and possibly further gases, such as a reactive gas or an inert gas, into the combustion chamber.
- the fluid feeding device 2 has four feed lines 3 . 1 , 3 . 2 , 3 . 3 and 3 . 4 .
- the fluid feeding device may also have a greater number n of feed lines.
- the outlet-side end portions 4 . 1 , 4 . 2 , 4 . 3 and 4 . 4 of the feed lines 3 . 1 , 3 . 2 , 3 . 3 and 3 . 4 run parallel, the outlets 9 of the feed lines being located at a same height with respect to the inflow direction R.
- four gases of different types can be introduced into the combustion chamber 7 separately and in a parallel inflow direction.
- the inflow direction of the gases emerging from the outlets 9 of the feed lines is indicated by the arrow identified by the designation R.
- the end portions 4 . 1 , 4 . 2 , 4 . 3 and 4 . 4 of the feed lines 3 . 1 , 3 . 2 , 3 . 3 and 3 . 4 are arranged nested coaxially in one another, which is represented in FIG. 1 by the dashed lines.
- the feed line 3 . 4 for example goes over into a cylindrical inner tube portion 4 . 4 , which runs coaxially and inside the tube portion 4 . 3 of the feed line 3 . 3 .
- the feed line 3 . 2 goes into a tube portion 4 . 2 , inside which there runs the tube portion 4 . 3 .
- the feed line 3 . 1 goes into an outer tube portion 4 . 1 , inside which there runs the tube portion 4 . 2 .
- FIGS. 2A and 2B Such an arrangement of the respective end portions of the feed lines nested coaxially in one another is illustrated once again in FIGS. 2A and 2B , but for an exemplary embodiment with three feed lines.
- FIG. 2A shows here a plan view of the outlets 9 of the end portions 4 . 1 , 4 . 2 and 4 . 3
- FIG. 2B shows a sectional view along the direction of flow.
- the inlet 13 of one of the feed lines is connected to a fluid container (not represented), in which an oxidizing agent is stored, so that an oxidizing agent stored therein can be conducted with a certain inflow rate through the outlet 9 of the corresponding end portion into the combustion chamber 7 .
- Respective inflow rates can be set by way of a valve 5 .
- the inlets 13 of two more of the feed lines are respectively connected to different fuel containers, different combustible gases being stored in the fuel containers. In this way, two different combustible gases can be conducted into the combustion chamber 7 .
- the inflow rate in each feed line can in turn be set by way of a valve 5 .
- the inlet of the fourth feed line can be connected or is connected to a fluid container (not represented), in which a reactive gas or an inert gas is stored, so that a reactive gas or an inert gas can be conducted with a certain inflow rate through the outlet 9 of the corresponding end portion into the combustion chamber 7 .
- the inflow rate can in turn be set by way of a valve 5 .
- the fluid or fuel containers may for example be in each case a gas bottle, in which a gas is stored under positive pressure.
- the valves 5 may be embodied as reducing valves.
- a flame 10 in which soot particles are formed as a result of combustion of the fuel with the oxidizing gas, forms over the outlets 9 of the feed lines 3 . 1 to 3 . 4 .
- the mixing ratio of the gases fed in can be varied, and consequently a direct influence can be exerted on the morphology (size and nature) of the particles generated and also on the chemical composition of the particles. Consequently, factors that influence the combustion, and with it the particle formation, can be varied independently of one another. If one of the combustible gases fed in is acetylene, then, for example, increasing the acetylene component in the combustible gas mixture leads to a greater carbon component in the combustible gas, and consequently to a greater formation of soot in the flame. If one of the combustible gases fed in is hydrogen, then increasing the hydrogen component leads to a greater carbon content in the particles formed.
- the emission of particles may be caused for example by other reactive or inert gas components, for example sulphur-containing particles due to the use of S 0 2 and/or H 2 S.
- the upper end 8 of the combustion chamber may be embodied in a way known per se.
- an aerosol or soot discharging line (not represented) may be provided, with a mouth opening into the combustion chamber, through which soot particles and/or aerosols formed in the combustion chamber can be discharged.
- FIG. 3 illustrates a further variant of an embodiment of the feeding device, a plan view of the outlets 9 of the end portion of the feeding device that opens out into the combustion chamber being shown.
- the feeding device has seven separate feed lines, the end portions of which are arranged parallel next to one another to form an arrangement of lines 12 with a packing density that is as great as possible.
- the end portions are arranged parallel next to one another, one of the end portions being arranged in the middle, while the six remaining end portions are arranged uniformly distributed around the circumference and at as little distance as possible from the end portion that is arranged in the middle.
- the particles or the aerosols Possible applications for the particles or the aerosols are for validating and/or calibrating particle measuring devices and particle sensors and also for testing and assessing filters and catalysts.
- the aerosol generated can also be used for the ageing of sensors, catalysts and filters.
- the use of the aerosols for measuring reaction kinetics makes possible the development of descriptive and/or predictive simulation models Likewise, kinetic investigations of model aerosols can be taken as a basis for functional development for optimizing filter loading models and regeneration strategies.
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Abstract
Description
- This application is a divisional of U.S. patent application Ser. No. 15/257,675 which was filed with the U.S. Patent and Trademark Office on Sep. 6, 2016 the entirety of which is incorporated herein by reference. Priority is claimed for this invention and application, on corresponding application having been filed in Germany on Sep. 10, 2015, No. 10 2015 011 853.6.
- The invention relates to an aerosol generator, in particular a soot generator, and a method for creating an aerosol, in particular a method for creating soot.
- To reduce particles from the exhaust gas of an engine, particle-reducing components are used, such as filter systems and/or catalytic converters. The filter systems that are used today differ essentially by the type of regeneration (burning off of the soot) they employ. Active regeneration is the term used here for the deliberate burning off of the soot for a limited time and passive regeneration is the term used here for the continuous breakdown of soot, ideally in dynamic equilibrium. For the technical testing of the filtering efficiency or the reactivity of soots, model soots and actual soots are used. At present, various particle measuring techniques, which determine the particle mass and the number of particles, are used for testing the legally limited emission of particles. At present, there are no standardized particle aerosols being used for the validation and calibration of these particle measuring techniques.
- Apart from internal combustion engines, currently various soot generators are used for producing soot particles.
- EP 0 353 746 A2 describes a device that creates soot particles by a spark discharge at graphite electrodes. U.S. Pat. No. 4,751,069 A describes a system for creating soot particles by cracking carbon-containing materials at high temperatures.
EP 1 055 877 B1 describes a burner for creating soot particles that burns a combustible gas and an oxidizing gas in a combustion chamber. A refinement of this burner is described inEP 1 590 408B 1. A further refinement is described in WO 2014/085941 A1, which describes the use of a liquid fuel for creating soot particles. - A disadvantage of the known devices is that the chemical composition of the particles and also the particle morphology, i.e. the size and nature of the particles created of the aerosol, cannot be influenced, or influenced only to a limited extent.
- An object of the invention is providing an improved device for creating model aerosols, in particular soot, with which disadvantages of conventional techniques can be avoided. An object of the invention is providing an aerosol generator, in particular a soot generator that makes it possible to exert a direct influence on the chemical composition and/or morphology of the particles created. A further object is that of providing a method for creating an aerosol or soot with which disadvantages of conventional methods can be avoided.
- According to a first aspect of the invention, an aerosol generator, in particular a soot generator, comprises a combustion chamber, in which fuel can be burned with an oxidizing agent in at least one soot-particle-creating flame, and a fluid feeding device for feeding fuel and an oxidizing agent into the combustion chamber.
- The fluid feeding device is distinguished by the fact that the fluid feeding device has at least three feed lines for a fluid, the outlet-side end portions of which are parallel, so that at least three fluids of different types, in particular gases, can be introduced into the combustion chamber unmixed and in a parallel inflow direction. The fluids, in particular gases, are consequently conducted separately into the combustion chamber and to the flame. The inflow direction is the average direction of flow of the fluid stream that flows out at the outlet of the feed line and enters the combustion chamber.
- This arrangement of the feed lines offers the advantage that a number of combustible gases and/or oxidizing gases of different types and/or inert gases can be conducted into a combustion chamber. The combination of at least three feed lines and a parallel inflow direction makes a flexible combination and composition of the components of the gas mixture that can be burned in the flame possible, in order to bring about a desired particle morphology and/or chemical composition of the particles.
- According to a preferred embodiment, the end portions of the at least three feed lines may be arranged coaxially in one another. In other words, according to this embodiment the end portions have diameters of different sizes and are arranged nested coaxially in one another. This makes a compact arrangement of the end portions of the feed lines possible, in order to introduce the different gases into the combustion chamber as far as possible at the same point, or at the point at which the flame is created.
- According to an alternative embodiment, the end portions may be arranged lying parallel next to one another. In particular when there are a large number of feed lines, this embodiment can be produced with little effort. In the case of an advantageous variant of this embodiment, the end portions are arranged parallel next to one another to form an arrangement of lines with a packing density that is as great as possible.
- According to a preferred embodiment, the fluid feeding device has at least four feed lines. According to this variant, for example, at least two different combustible gases, an oxidizing gas and a further inert gas or reactive gas can be introduced into the combustion chamber. A reactive gas is a gas with so-called heteroatoms (non-carbon atoms), such as for example nitrogen, sulphur or other elements. On account of their nature, these reactive gases can act as an oxidizing agent (for example S0 2, N0 2) or as a reducing agent (for example NH3, H2S, N2O). A variant of this embodiment therefore provides that the fluid feeding device has four or more feed lines.
- A further advantageous variant of this embodiment provides that the fluid feeding device has seven feed lines. This variant offers still greater flexibility in setting the composition of the gas mixture that is burned in the flame. A further advantage is that, with seven feed lines, their seven parallel end portions can be arranged with a packing density that is as great as possible. For this purpose, the end portions are arranged parallel next to one another, one of the end portions being arranged in the middle, while the six remaining end portions are arranged uniformly distributed around the circumference and at as little distance as possible from the end portion that is arranged in the middle.
- It is also particularly advantageous if the outlets of the feed lines are located at the same height with respect to the inflow direction, so that the gases are introduced into the combustion chamber as close to one another as possible and as far as possible mix at the same time.
- In a preferred exemplary embodiment, a first of the feed lines is connected on the inlet side to a first fluid container (fuel container), containing a first fuel. Furthermore, a second of the feed lines is connected on the inlet side to a second fluid container (fuel container), containing a second fuel. The first fuel may be a first combustible gas and the second fuel may be a second combustible gas that is different from the first combustible gas. Examples of such combustible gases are hydrogen (H2), propane (C3H8) or ethine or acetylene (C2H2).
- A further advantageous possibility for realizing the invention is a third of the feed lines are connected on the inlet side to a third fluid container containing an oxidizing gas Likewise possible is the use of one or more oxidizing gases with different oxygen components, for example air, oxygen, or ozone, which are conducted into the combustion chamber by way of separate feed lines in each case. According to this variant, then at least two feed lines of the fluid feeding device are connected on the inlet side in each case to respective a container that contains an oxidizing gas, different oxidizing gases being stored in the containers.
- Furthermore, at least one of the feed lines may be connected on the inlet side to a fluid container, which contains a reactive gas. In this way, one or more different reactive gases can be introduced into the combustion chamber.
- Furthermore, the aerosol generator may be formed such that at least one of the feed lines is connected on the inlet side to a fluid container, which contains a so-called inert gas. Inert gases are distinguished by the fact that they do not take part directly in the combustion. Possible inert gases are, for example, N2, CO2 or noble gases. In this way, one or more different inert gases can be introduced into the combustion chamber, in order to influence the physical-chemical boundary conditions of the combustion, and as a result the particle morphology.
- Furthermore, the aerosol generator may have a regulator, by which a fluid flow rate can be set in each of the feed lines. The regulator may for example be a valve arrangement, such that each feed line has at least one valve, by which a flow rate through the feed line can be set. In this way, the mixing ratio of the gases fed in can be varied and in this way a direct influence can be exerted on the morphology (size and nature) of the particles generated and on the chemical composition of the particles.
- Thus, for example, increasing the acetylene component in the combustible gas mixture leads to a greater carbon component in the combustible gas, and consequently to a greater formation of soot in the flame. Increasing the hydrogen component leads to a greater carbon component in the particles formed. The use of pure hydrogen leads to a flame that is free from soot. In this case, the emission of particles may be caused for example by other reactive or inert gas components, for example sulphur-containing particles due to the use of S0 2 and/or H2S.
- According to a second aspect of the invention, a method for creating an aerosol, in particular a method for creating soot, is provided, in which method at least one fuel and an oxidizing agent are fed to a combustion chamber by an aerosol generator as disclosed in this document, and a soot-particle-creating flame, in particular a diffusion flame, is formed in the combustion chamber.
- An advantageous variant provides here that, by an aerosol generator with at least four feed lines, at least two combustible gases, at least one oxidizing gas and at least one reactive gas or inert gas are introduced into the combustion chamber.
- The invention also relates to a method for testing or calibrating a particle measuring device, particle sensor, particle filter or particle catalyst, characterized in that, for testing or calibrating such a device, it is fed an aerosol, in particular soot particles, which are created by an aerosol generator as disclosed in this document or by means of a method as disclosed in this document.
- Other objects and features of the present invention will become apparent from the following detailed description considered in conjunction with the accompanying drawings. It is to be understood, however, that the drawings are designed solely for purposes of illustration and not as a definition of the limits of the invention, for which reference should be made to the appended claims. It should be further understood that the drawings are not necessarily drawn to scale and that, unless otherwise indicated, they are merely intended to conceptually illustrate the structures and procedures described herein.
- The preferred embodiments and features of the invention that are described above can be combined with one another as desired. Further details and advantages of the invention are described below with reference to the accompanying drawings, in which:
-
FIG. 1 is a schematic representation of a soot generator; -
FIGS. 2A and 2B are sectional views of an outlet-side end portion of the fluid feeding device; and -
FIG. 3 is a sectional view of an outlet-side end portion of the fluid feeding device. - Elements that are the same or functionally equivalent are denoted by the same designations in all of the figures.
-
FIG. 1 schematically shows a cross section of an exemplary embodiment of thesoot generator 1 according to the invention. - The soot generator represented in
FIG. 1 comprises acombustion chamber 7, in which at least one fuel with an oxidizing agent can be burned in at least one soot-particle-creatingflame 10. Thecombustion chamber 7 may be embodied in a way known per se and be formed for example by a cylindricalouter tube 6, at the lower end of which an end portion of afluid feeding device 2 protrudes into thecombustion chamber 7. - The
fluid feeding device 2 can be used for introducing combustible gases, an oxidizing gas and possibly further gases, such as a reactive gas or an inert gas, into the combustion chamber. - In the example shown, the
fluid feeding device 2 has four feed lines 3.1, 3.2, 3.3 and 3.4. However, it is emphasized that the fluid feeding device may also have a greater number n of feed lines. - The outlet-side end portions 4.1, 4.2, 4.3 and 4.4 of the feed lines 3.1, 3.2, 3.3 and 3.4 run parallel, the
outlets 9 of the feed lines being located at a same height with respect to the inflow direction R. In this way, in the exemplary embodiment shown four gases of different types can be introduced into thecombustion chamber 7 separately and in a parallel inflow direction. The inflow direction of the gases emerging from theoutlets 9 of the feed lines is indicated by the arrow identified by the designation R. - The end portions 4.1, 4.2, 4.3 and 4.4 of the feed lines 3.1, 3.2, 3.3 and 3.4 are arranged nested coaxially in one another, which is represented in
FIG. 1 by the dashed lines. The feed line 3.4 for example goes over into a cylindrical inner tube portion 4.4, which runs coaxially and inside the tube portion 4.3 of the feed line 3.3. The feed line 3.2 goes into a tube portion 4.2, inside which there runs the tube portion 4.3. The feed line 3.1 goes into an outer tube portion 4.1, inside which there runs the tube portion 4.2. - Such an arrangement of the respective end portions of the feed lines nested coaxially in one another is illustrated once again in
FIGS. 2A and 2B , but for an exemplary embodiment with three feed lines.FIG. 2A shows here a plan view of theoutlets 9 of the end portions 4.1, 4.2 and 4.3, whileFIG. 2B shows a sectional view along the direction of flow. - The
inlet 13 of one of the feed lines is connected to a fluid container (not represented), in which an oxidizing agent is stored, so that an oxidizing agent stored therein can be conducted with a certain inflow rate through theoutlet 9 of the corresponding end portion into thecombustion chamber 7. Respective inflow rates can be set by way of avalve 5. - Correspondingly, the
inlets 13 of two more of the feed lines are respectively connected to different fuel containers, different combustible gases being stored in the fuel containers. In this way, two different combustible gases can be conducted into thecombustion chamber 7. The inflow rate in each feed line can in turn be set by way of avalve 5. - The inlet of the fourth feed line can be connected or is connected to a fluid container (not represented), in which a reactive gas or an inert gas is stored, so that a reactive gas or an inert gas can be conducted with a certain inflow rate through the
outlet 9 of the corresponding end portion into thecombustion chamber 7. The inflow rate can in turn be set by way of avalve 5. - The fluid or fuel containers may for example be in each case a gas bottle, in which a gas is stored under positive pressure. For regulating the inflow rate, the
valves 5 may be embodied as reducing valves. - After ignition, a
flame 10, in which soot particles are formed as a result of combustion of the fuel with the oxidizing gas, forms over theoutlets 9 of the feed lines 3.1 to 3.4. - By setting the inflow rates by way of the
valves 5, the mixing ratio of the gases fed in can be varied, and consequently a direct influence can be exerted on the morphology (size and nature) of the particles generated and also on the chemical composition of the particles. Consequently, factors that influence the combustion, and with it the particle formation, can be varied independently of one another. If one of the combustible gases fed in is acetylene, then, for example, increasing the acetylene component in the combustible gas mixture leads to a greater carbon component in the combustible gas, and consequently to a greater formation of soot in the flame. If one of the combustible gases fed in is hydrogen, then increasing the hydrogen component leads to a greater carbon content in the particles formed. The use of pure hydrogen leads to a flame that is free from soot. In this case, the emission of particles may be caused for example by other reactive or inert gas components, for example sulphur-containing particles due to the use of S0 2 and/or H2S. - The
upper end 8 of the combustion chamber may be embodied in a way known per se. For example, an aerosol or soot discharging line (not represented) may be provided, with a mouth opening into the combustion chamber, through which soot particles and/or aerosols formed in the combustion chamber can be discharged. -
FIG. 3 illustrates a further variant of an embodiment of the feeding device, a plan view of theoutlets 9 of the end portion of the feeding device that opens out into the combustion chamber being shown. As can be seen inFIG. 3 , a special feature of this variant of the embodiment is that the feeding device has seven separate feed lines, the end portions of which are arranged parallel next to one another to form an arrangement oflines 12 with a packing density that is as great as possible. For this purpose, the end portions are arranged parallel next to one another, one of the end portions being arranged in the middle, while the six remaining end portions are arranged uniformly distributed around the circumference and at as little distance as possible from the end portion that is arranged in the middle. - Possible applications for the particles or the aerosols are for validating and/or calibrating particle measuring devices and particle sensors and also for testing and assessing filters and catalysts. By introducing appropriate chemical components, the aerosol generated can also be used for the ageing of sensors, catalysts and filters. The use of the aerosols for measuring reaction kinetics makes possible the development of descriptive and/or predictive simulation models Likewise, kinetic investigations of model aerosols can be taken as a basis for functional development for optimizing filter loading models and regeneration strategies.
- Although the invention has been described with reference to specific exemplary embodiments, it is clear to a person skilled in the art that various modifications can be made and equivalents used as replacements without departing from the scope of the invention. Consequently, the invention is not intended to be restricted to the exemplary embodiments disclosed, but also to include all exemplary embodiments that fall within the scope of the appended claims. In particular, the invention also claims protection for the subject matter and the features of the subclaims independently of the claims referred to.
- Thus, while there have shown and described and pointed out fundamental novel features of the invention as applied to a preferred embodiment thereof, it will be understood that various omissions and substitutions and changes in the form and details of the devices illustrated, and in their operation, may be made by those skilled in the art without departing from the spirit of the invention. For example, it is expressly intended that all combinations of those elements and/or method steps which perform substantially the same function in substantially the same way to achieve the same results are within the scope of the invention. Moreover, it should be recognized that structures and/or elements and/or method steps shown and/or described in connection with any disclosed form or embodiment of the invention may be incorporated in any other disclosed or described or suggested form or embodiment as a general matter of design choice. It is the intention, therefore, to be limited only as indicated by the scope of the claims appended hereto.
Claims (11)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US16/666,724 US20200061572A1 (en) | 2015-09-10 | 2019-10-29 | Aerosol Generator, In Particular Soot Generator |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
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DE102015011853.6 | 2015-09-10 | ||
DE102015011853.6A DE102015011853A1 (en) | 2015-09-10 | 2015-09-10 | Aerosol generator, in particular soot generator |
US15/257,675 US10583416B2 (en) | 2015-09-10 | 2016-09-06 | Aerosol generator, in particular soot generator |
US16/666,724 US20200061572A1 (en) | 2015-09-10 | 2019-10-29 | Aerosol Generator, In Particular Soot Generator |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US15/257,675 Division US10583416B2 (en) | 2015-09-10 | 2016-09-06 | Aerosol generator, in particular soot generator |
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US20200061572A1 true US20200061572A1 (en) | 2020-02-27 |
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US15/257,675 Active 2036-12-29 US10583416B2 (en) | 2015-09-10 | 2016-09-06 | Aerosol generator, in particular soot generator |
US16/666,724 Abandoned US20200061572A1 (en) | 2015-09-10 | 2019-10-29 | Aerosol Generator, In Particular Soot Generator |
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US15/257,675 Active 2036-12-29 US10583416B2 (en) | 2015-09-10 | 2016-09-06 | Aerosol generator, in particular soot generator |
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US (2) | US10583416B2 (en) |
EP (1) | EP3141585A1 (en) |
CN (1) | CN106519738B (en) |
DE (1) | DE102015011853A1 (en) |
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CN112782058B (en) * | 2020-12-28 | 2023-03-21 | 潍柴动力股份有限公司 | Particle generating device |
DE102023202665B3 (en) * | 2023-03-23 | 2024-07-11 | Benninghoven Zweigniederlassung Der Wirtgen Mineral Technologies Gmbh | Nozzle arrangement for a burner and burner with such a nozzle arrangement |
Citations (2)
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US6352680B1 (en) * | 1998-06-29 | 2002-03-05 | The Boc Group Plc | Partial combustion of hydrogen sulphide |
US20150232770A1 (en) * | 2012-08-14 | 2015-08-20 | Thyssenkrupp Industrial Solutions Ag | Device and method for introducing oxygen into a pressurized fluidized-bed gasification process |
Family Cites Families (12)
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US4751069A (en) | 1982-10-18 | 1988-06-14 | Columbian Chemicals Company | Automotive high color carbon |
DE8811320U1 (en) | 1988-08-04 | 1989-10-12 | Palas GmbH Partikel- und Lasermeßtechnik, 7500 Karlsruhe | Device for generating a solid aerosol |
EP1055877B1 (en) | 1999-05-26 | 2003-09-03 | Lianpeng Jing | Burner for producing carbon black |
EP1590408B1 (en) | 2003-01-24 | 2006-12-27 | Lianpeng Jing | Soot generator with constricted quench gas line |
DE10342498B4 (en) | 2003-09-12 | 2006-07-13 | Centrotherm Elektrische Anlagen Gmbh & Co. Kg | Method and device for thermal exhaust gas purification |
EP1616914A1 (en) | 2004-07-12 | 2006-01-18 | Matter Engineering AG | Apparatus for Producing Carbon Black |
EP1842880B1 (en) | 2006-04-06 | 2017-03-08 | Testo AG | Soot generator |
GB0607851D0 (en) * | 2006-04-24 | 2006-05-31 | Johnson Matthey Plc | Particulate matter generator |
WO2009020958A2 (en) | 2007-08-06 | 2009-02-12 | Washington University | Production process for single-walled carbon nanotubes |
DE102011011207A1 (en) * | 2011-02-14 | 2012-08-16 | Air Liquide Deutschland Gmbh | Burner for uniform heating of a long oven |
CH707316A1 (en) | 2012-12-07 | 2014-06-13 | Lianpeng Jing | Soot generator. |
GB201316637D0 (en) * | 2013-09-19 | 2013-11-06 | Rolls Royce Plc | A soot generating device |
-
2015
- 2015-09-10 DE DE102015011853.6A patent/DE102015011853A1/en active Pending
-
2016
- 2016-08-12 EP EP16001796.8A patent/EP3141585A1/en active Pending
- 2016-09-06 US US15/257,675 patent/US10583416B2/en active Active
- 2016-09-09 CN CN201610812081.4A patent/CN106519738B/en active Active
-
2019
- 2019-10-29 US US16/666,724 patent/US20200061572A1/en not_active Abandoned
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6352680B1 (en) * | 1998-06-29 | 2002-03-05 | The Boc Group Plc | Partial combustion of hydrogen sulphide |
US20150232770A1 (en) * | 2012-08-14 | 2015-08-20 | Thyssenkrupp Industrial Solutions Ag | Device and method for introducing oxygen into a pressurized fluidized-bed gasification process |
Also Published As
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CN106519738B (en) | 2021-04-16 |
DE102015011853A1 (en) | 2017-03-16 |
EP3141585A1 (en) | 2017-03-15 |
CN106519738A (en) | 2017-03-22 |
US20170073230A1 (en) | 2017-03-16 |
US10583416B2 (en) | 2020-03-10 |
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