CN1105595C - Arrangement for combining dissimilar streams - Google Patents
Arrangement for combining dissimilar streams Download PDFInfo
- Publication number
- CN1105595C CN1105595C CN98814291A CN98814291A CN1105595C CN 1105595 C CN1105595 C CN 1105595C CN 98814291 A CN98814291 A CN 98814291A CN 98814291 A CN98814291 A CN 98814291A CN 1105595 C CN1105595 C CN 1105595C
- Authority
- CN
- China
- Prior art keywords
- stream
- baffle
- temperature
- air
- enclosure
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/20—Jet mixers, i.e. mixers using high-speed fluid streams
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/10—Mixing gases with gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/311—Injector mixers in conduits or tubes through which the main component flows for mixing more than two components; Devices specially adapted for generating foam
- B01F25/3111—Devices specially adapted for generating foam, e.g. air foam
- B01F25/31112—Devices specially adapted for generating foam, e.g. air foam with additional mixing means other than injector mixers, e.g. screen or baffles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/314—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
- B01F25/3141—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit with additional mixing means other than injector mixers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
- B01F25/4315—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor the baffles being deformed flat pieces of material
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Dispersion Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Solid Materials (AREA)
- Treatment Of Fiber Materials (AREA)
- Toys (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Abstract
Description
发明背景Background of the invention
1.发明领域1. Field of invention
本发明涉及一种用于结合不同流股的装置和方法,更具体地是涉及一种在导管或类似的封闭件中使用的折流板结构,目的是提高两股(或多股)不同材料流股(例如,两股温度不同的气流)结合形成一均匀的流股的效率。This invention relates to an apparatus and method for combining different streams, and more particularly to a baffle structure for use in conduits or similar closures in order to improve the flow of two (or more) strands of different materials The efficiency with which streams (for example, two streams of different temperatures) combine to form a homogeneous stream.
2.先有技术的描述2. Description of prior art
在许多工业设备中常常需要结合一些不同的气体(或液体)材料。例如,可能需要使由传统的(燃气或燃油)燃烧炉出来的高温燃烧气体与温度较低的过程气体混合燃烧(即如遇到空气干燥器时)。或者,可能需要使来自燃气轮机的出口的废气(高温)与来自例如空气干燥器的过程气体混合。这些装置的结构一般包括通过一导管(或类似的封闭件)运行的第一空气流,与通过一输入口引入该导管的第二流股。In many industrial installations it is often necessary to combine several different gaseous (or liquid) materials. For example, it may be desirable to combust high temperature combustion gases from conventional (gas or oil) fired furnaces with cooler process gases (eg as encountered in air dryers). Alternatively, it may be desirable to mix the exhaust gas (high temperature) from the outlet of the gas turbine with process gas from eg an air dryer. The construction of these devices generally includes a first air stream running through a conduit (or similar enclosure), and a second stream introduced into the conduit through an inlet.
为了实施这种不同流股的结合,先有技术的装置一般依赖于采用第二气流的射入点下游的“搅动”和紊流。一般而言,这种装置需要大量的能量(因此降低了结合的流股的流速),而且最终结合两流股和形成均匀特性的流股需要的距离也较长。在另一种先有技术的装置中,在射入流股的下游插入偏转叶片,从而在管道中产生反向旋流。To effectuate this combination of different streams, prior art devices generally rely on "agitation" and turbulence downstream of the point of injection of the second gas stream to be employed. In general, such devices require a large amount of energy (thus reducing the flow rate of the combined streams) and the distance required to ultimately combine the two streams and form a stream of uniform characteristics. In another prior art arrangement, deflecting vanes are inserted downstream of the injected stream, thereby creating a reverse swirl in the pipe.
因此,为了便于不同流股的结合,在先有技术中需要对装置进行改进,要求这种装置不但能效高,而且所用附加管道的长度最短。Therefore, in order to facilitate the combination of different streams, there is a need in the prior art for an improved device which is not only energy efficient but also uses the shortest length of additional piping.
发明概要Summary of the invention
先有技术中所存在的需要通过本发明得到满足,本发明涉及一种用于结合不同流股的装置和方法,更具体地是涉及一种在导管或类似的封闭件中所用的折流板结构,以提高两股(或多股)不同材料流股(例如,两股温度不同的气流)结合形成一均匀流股的效率。The needs existing in the prior art are met by the present invention, which relates to an apparatus and method for combining different streams, and more particularly to a baffle for use in a conduit or similar closure structure to increase the efficiency with which two (or more) streams of different materials (eg, two streams of different temperatures) combine to form a uniform stream.
本发明提供一种用于将通过一封闭件运行的第一材料流与第二材料流结合的装置,上述第二材料流包括与上述第一流股不同的特性,上述装置包括:The present invention provides an apparatus for combining a first material stream running through an enclosure with a second material stream, said second material stream comprising different characteristics from said first stream, said apparatus comprising:
一个用于将上述第二流股引入上述封闭件的输入口,其中,上述入口向上述封闭件内凸入一预定高度h;和an inlet for introducing said second stream into said enclosure, wherein said inlet projects into said enclosure by a predetermined height h; and
一个设置在上述封闭件内且定位成在上述输入口的上游的一位置处横断上述第一流股的折流板,上述折流板与上述输入口分离一预定距离d,其中,上述第一流股越过上述折流板,在上述折流板和上述输入口之间形成一个足以提高上述第一流股和第二流股的结合效率的低压区。a baffle disposed within said closure and positioned to traverse said first stream at a position upstream of said inlet, said baffle separated from said inlet by a predetermined distance d, wherein said first stream Beyond the above-mentioned baffle, a low-pressure area is formed between the above-mentioned baffle and the above-mentioned inlet port, which is sufficient to improve the combining efficiency of the above-mentioned first stream and the second stream.
如上所述的装置,其中,该折流板包括一锥形结构,构成形式为包括较宽的底部和较窄的顶部,上述锥形折流板的设置是使上述较宽的的底部位于距输入口最近处,而该锥形折流板在封闭件的宽度方向延伸。The above-mentioned device, wherein, the baffle includes a conical structure, which is configured to include a wider bottom and a narrower top, and the configuration of the above-mentioned conical baffle is such that the wider bottom is located at a distance from The inlet port is nearest and the tapered baffle extends across the width of the closure.
如上所述的装置,其中,上述折流板形成锥形使得上述折流板的较窄的顶部不与该封闭件接触。The device as described above, wherein said baffle is tapered such that the narrower top of said baffle does not contact the closure.
如上所述的装置,其中,该锥形折流板包括圆锥截面的几何形状。The apparatus as described above, wherein the tapered baffle comprises a conical cross-sectional geometry.
如上所述的装置,其中,上述锥形折流板包括三角形截面的几何形状。The apparatus as described above, wherein said tapered baffles comprise a triangular cross-sectional geometry.
如上所述的装置,其中,该锥形折流板的较宽底部包括一狭缝区,使得上述较宽底部的一部分由封闭件的表面移离一预定的狭缝距离g。Apparatus as described above, wherein the wider base of the tapered baffle includes a slit region such that a portion of said wider base is displaced from the surface of the closure by a predetermined slit distance g.
如上所述的装置,其中,该输入口设置为在封闭件内以一大于与锥形折流板相关的狭缝g的预定高度h凸出。A device as described above, wherein the inlet is arranged to protrude within the enclosure by a predetermined height h greater than the slit g associated with the conical baffle.
如上所述的装置,其中,第一流股包括温度较低的空气,而第二流股包括温度较高的空气,上述锥形折流板的狭缝因此可使上述温度较低的空气能从上述折流板下方通过,进入低压区并降低上述折流板的环境温度。Apparatus as described above, wherein the first stream comprises air at a lower temperature and the second stream comprises air at a higher temperature, the slits of the conical baffles thereby allowing the cooler air to flow from Passing under the above-mentioned baffle, enter the low-pressure area and reduce the ambient temperature of the above-mentioned baffle.
如上所述的装置,其中,该锥形折流板包括一个或多个孔,从而为上述锥形折流板提供额外的冷却。The apparatus as described above, wherein the conical baffle includes one or more holes to provide additional cooling to the conical baffle.
如上所述的装置,其中,上述第一流股包括第一种气态材料,而第二流股包括第二种气态材料。The apparatus as described above, wherein said first stream comprises a first gaseous material and said second stream comprises a second gaseous material.
如上所述的装置,其中,该第一气体为氮气,而第二气体为氧气。The device as described above, wherein the first gas is nitrogen and the second gas is oxygen.
如上所述的装置,其中,该第一材料是第一种液体,而第二材料是第二种液体。The device as above, wherein the first material is a first liquid and the second material is a second liquid.
如上所述的装置,其中,该第一液体流股包括一种清洁液体,而第二液体流股包括一种乳化剂。The apparatus as above, wherein the first liquid stream comprises a cleaning liquid and the second liquid stream comprises an emulsifier.
如上所述的装置,其中,该第一液体流股包括一种清洁液体,而第二液体流股包括一种悬浮液。The apparatus as described above, wherein the first liquid stream comprises a cleaning liquid and the second liquid stream comprises a suspension.
如上所述的装置,其中,该折流板包括一个或多个孔。The apparatus as described above, wherein the baffle comprises one or more holes.
如上所述的装置,其中,该折流板包括一狭缝区,以使上述折流板离输入口最近的一个边缘由封闭件的表面移离一预定的狭缝距离g。A device as described above, wherein the baffle includes a slit region such that an edge of said baffle closest to the inlet is displaced from the surface of the closure by a predetermined slit distance g.
如上所述的装置,其中,该输入口设置为在封闭件内以一大于与折流板的边缘的移离相关的狭缝g的预定高度h凸出。A device as described above, wherein the inlet is arranged to protrude within the enclosure by a predetermined height h greater than the slit g associated with the displacement of the edge of the baffle.
如上所述的装置,其中,第一流股包括一高速流股,而第二流股包括一低速流股。The apparatus as described above, wherein the first stream comprises a high velocity stream and the second stream comprises a low velocity stream.
如上所述的装置,其中,该折流板包括一种非锥形板的几何形状。The apparatus as described above, wherein the baffle comprises a non-tapered plate geometry.
如上所述的装置,其中,该折流板包括一整体部件。The apparatus as described above, wherein the baffle comprises an integral part.
如上所述的装置,其中,该折流板包括多个部件,使得各单个部段可以根据需要添加或去除。Apparatus as described above, wherein the baffle comprises multiple parts, such that individual sections may be added or removed as required.
如上所述的装置,其中,该折流板包括一下板部段和一以可拆卸方式附接于上述下板部分的上板部段。The apparatus as described above, wherein the baffle comprises a lower panel section and an upper panel section detachably attached to said lower panel section.
本发明还提供一种用于使通过一封闭件运行的第一材料流股与多股不同的材料流股混合的装置,上述多股不同流股的每股包括与上述第一流股不同的特性,上述装置包括:The invention also provides a device for mixing a first stream of material running through an enclosure with a plurality of different streams of material, each of said plurality of different streams comprising different properties than said first stream , the above devices include:
布置成凸入到该封闭件内的多个输入口,各输入口用于引入上述多股不同流股的单独一股;和a plurality of inlet ports arranged to protrude into the closure, each inlet port for introducing a single one of said plurality of different streams; and
多个折流板,上述多个折流板与上述多个输入口呈—一对应关系,各折流板设置在其相关的输入口的上游,并与其分离一预定距离d,其中上述第一流股越过上述多个折流板的各折流板的流动,在各折流板及其相关的输入口之间形成足以提高上述第一流股与上述多股不同流股的结合效率的低压区。A plurality of baffles, the plurality of baffles are in a one-to-one correspondence with the plurality of input ports, and each baffle is arranged upstream of its associated input port and separated from it by a predetermined distance d, wherein the first flow The flow of the strand across each baffle of said plurality of baffles creates a region of low pressure between each baffle and its associated inlet port sufficient to enhance the efficiency of combining said first stream with said plurality of different streams.
如上所述的装置,其中,多个折流板的至少一个折流板包括一种锥形结构,其构成是包括一较宽的底部和一较窄的顶部,上述至少一个锥形折流板设置为使上述较宽底部距相关的至少一个输入口最近,且上述至少一个锥形折流板在封闭件的宽度方向延伸。Apparatus as described above, wherein at least one baffle of the plurality of baffles comprises a conical configuration comprising a wider base and a narrower top, said at least one conical baffle The wider base is located closest to the associated at least one inlet and the at least one tapered baffle extends across the width of the closure.
如上所述的装置,其中,至少一个折流板形成锥形,从而形成使较窄的顶部不与该封闭件接触。Apparatus as described above, wherein at least one baffle is tapered so as to form a narrower top out of contact with the closure.
如上所述的装置,其中,多个输入口沿封闭件的长度方向设置。The device as described above, wherein the plurality of inlets are arranged along the length of the closure.
如上所述的装置,其中,多个输入口在封闭结构的宽度方向设置。The device as described above, wherein a plurality of input ports are arranged in the width direction of the closed structure.
本发明还提供一种用于使通过一导管运行的温度较低的第一气流与温度较高的第二气流混合的装置,该装置包括:The present invention also provides an apparatus for mixing a first cooler air stream with a second warmer air stream traveling through a conduit, the apparatus comprising:
一个设置为凸入到该导管内的输入口,上述输入口用于将第二流股引入上述导管;和an inlet configured to project into the conduit for introducing a second stream into said conduit; and
一个设置在上述导管内且横断上述第一流股的流动的锥形折流板,其中上述锥形折流板位于上述输入口上游一预定距离d处,上述锥形折流板包括较宽的底表面和沿其长度方向变窄以形成一锥形顶部区的侧壁,上述折流板设置为使宽的底表面邻接上述导管有上述输入口穿过其凸出的部分,上述锥形折流板随后在上述导管的宽度方向延伸。a conical baffle disposed within said conduit and transverse to the flow of said first stream, wherein said conical baffle is located a predetermined distance d upstream of said inlet, said conical baffle comprising a wider base Surfaces and sidewalls that narrow along their length to form a tapered top region, said baffles are arranged so that the wide bottom surface adjoins the portion of said conduit through which said inlet protrudes, said tapered baffles The plate then extends across the width of the duct.
本发明提供一种使第一材料流与第二材料流结合的方法,上述第二材料流包括与上述第一流股不同的特性,上述方法包括的步骤有:The present invention provides a method of combining a first material stream with a second material stream, said second material stream comprising different properties from said first stream, said method comprising the steps of:
a)将第一流股引入一封闭件,使上述第一流股沿该封闭件的长度方向运行;a) introducing the first stream into a closure such that said first stream runs along the length of the closure;
b)利用设置在该封闭件内的折流板阻断上述第一流股的流动;和b) blocking the flow of said first stream by means of a baffle arranged in the closure; and
c)将第二流股引入上述封闭件,上述第二流股在上述折流板下游的一位置处引入,上述第一流股越过上述折流板的流动的阻断,在上述折流板和上述第二流股引入点之间形成一足以提高上述第一流股和第二流股的结合效率的低压区。c) introduction of a second stream into said closure, said second stream being introduced at a position downstream of said baffle, the interruption of flow of said first stream over said baffle, between said baffle and A low-pressure area is formed between the introduction points of the second stream, which is sufficient to improve the combining efficiency of the first stream and the second stream.
如上所述的方法,其中,该第一流股包括温度较低的空气,而第二流股包括温度较高的空气。The method as above, wherein the first stream comprises air at a lower temperature and the second stream comprises air at a higher temperature.
如上所述的方法,其中,该第一流股包括第一气态材料,而第二流股包括第二气态材料。The method as above, wherein the first stream comprises a first gaseous material and the second stream comprises a second gaseous material.
如上所述的方法,其中,该第一气体是氦气,而第二气体是氧气。The method as above, wherein the first gas is helium and the second gas is oxygen.
如上所述的方法,其中,该第一材料是第一液体,而第二材料是第二液体。The method as above, wherein the first material is a first liquid and the second material is a second liquid.
如上所述的方法,其中,第一流股包括一高速流股,而第二流股包括一低速流股。The method as above, wherein the first stream comprises a high speed stream and the second stream comprises a low speed stream.
本发明还提供一种使多股不同材料流股结合的方法,上述方法包括的步骤有:The present invention also provides a method for combining multiple streams of different materials, the method comprising the steps of:
a)将第一流股引入一封闭件,使上述第一流股沿该封闭结构的长度方向运行;a) introducing the first stream into an enclosure so that said first stream runs along the length of the enclosure;
b)利用设置在封闭件内的折流板阻断上述第一流股的流动;b) blocking the flow of the above-mentioned first stream by means of a baffle arranged in the closure;
c)将第二流股引入上述封闭件,上述第二流股在上述折流板下游的一位置处引入,上述第一流股越过上述折流板的流动的阻断,在上述折流板和上述第二流股引入点之间形成一足以提高上述第一流股和第二流股的结合效率的低压区;和c) introduction of a second stream into said closure, said second stream being introduced at a position downstream of said baffle, the interruption of flow of said first stream over said baffle, between said baffle and A low-pressure zone is formed between the introduction points of the above-mentioned second stream enough to improve the combining efficiency of the above-mentioned first stream and the second stream; and
d)对于留存在多股不同流股的每一股重复步骤b)和c),直至所有流股结合。d) Repeat steps b) and c) for each of the remaining streams in a number of different streams until all streams are combined.
本发明还提供一种在纺织材料制造中通过使上述织造材料经遇基本恒温室气而对该织造材料进行干燥的方法,其包括的步骤有:The present invention also provides a method for drying the woven material by subjecting the above-mentioned woven material to a substantially constant temperature during the manufacture of the textile material, comprising the steps of:
a)将该织造材料插入一合适的干燥设备内;和a) inserting the woven material into a suitable drying device; and
b)将温度基本恒定的空气流提供到上述织造材料的表面,该基本恒温室气流的形成方式如下:b) providing to the surface of said woven material an air flow of substantially constant temperature, the substantially constant temperature air flow being formed as follows:
c)将第一温度的第一气流引入一封闭件,使上述第一流股沿该封闭结构的长度方向运行;c) introducing a first air flow at a first temperature into an enclosure so that the above-mentioned first stream runs along the length of the enclosure;
d)利用设置在该封闭件内的折流板阻断上述第一流股的流动;和d) blocking the flow of said first stream by means of a baffle arranged in the closure; and
e)将温度为与上述第一温度不同的第二温度的第二气流引入上述封闭件,上述第二流股在上述折流板下游的一位置处引入,上述第一流股越过上述折流板的流动的阻断,在上述折流板和上述第二流股引入点之间形成一足以提高上述第一流股和第二流股的结合效率的低压区,且提供基本恒温的输出空气流,用于干燥上述织造材料。e) introducing into said enclosure a second gas stream at a second temperature different from said first temperature, said second stream being introduced at a position downstream of said baffle, said first stream passing over said baffle The blocking of the flow of the above-mentioned baffle plate and the introduction point of the above-mentioned second stream forms a low-pressure zone sufficient to improve the combining efficiency of the above-mentioned first stream and the second stream, and provides an output air flow with a substantially constant temperature, For drying the above mentioned woven materials.
如上所述的方法,其中,该第一气流股包括温度较低的空气,而第二气流股包括温度较高的空气。The method as above, wherein the first air stream comprises cooler air and the second air stream comprises higher temperature air.
如上所述的方法,其中,第一温度为250°F,而第二温度为2440°F。The method as above, wherein the first temperature is 250°F and the second temperature is 2440°F.
本发明还提供一种在针织材料制造中通过使上述针织材料经进基本恒温空气而对该针织材料进行干燥的方法,其包括的步骤有:The present invention also provides a method for drying the knitted material by passing the above-mentioned knitted material through air at a substantially constant temperature in the manufacture of the knitted material, which includes the following steps:
a)将针织材料插入一合适的干燥设备内;和a) Insert the knitted material into a suitable drying device; and
b)将温度基本恒定的空气流提供到上述针织材料的表面,该基本恒温空气流的形成方式如下:b) providing an air flow of substantially constant temperature to the surface of said knitted material, the substantially constant temperature air flow being formed as follows:
c)将第一温度的第一气流引入一封闭件,使上述第一流股沿该封闭件的长度方向运行;c) introducing a first gas flow at a first temperature into an enclosure so that the first stream runs along the length of the enclosure;
d)利用设置在该封闭件内的折流板阻断上述第一流股的流动;和d) blocking the flow of said first stream by means of a baffle arranged in the closure; and
e)将温度为与上述第一温度不同的第二温度的第二气流引入上述封闭件,上述第二流股在上述折流板的下游的一位置处引入,上述第一流股越过上述折流板的流动的阻断,在上述折流板和上述第二流股引入点之间形成一足以提高上述第一流股和第二流股的结合效率的低压区,且提供基本恒温的输出空气流,用于干燥上述针织材料。e) introducing into said enclosure a second gas stream having a temperature of a second temperature different from said first temperature, said second stream being introduced at a position downstream of said baffle, said first stream passing over said baffle The blocking of the flow of the plate forms a low-pressure zone between the above-mentioned baffle plate and the introduction point of the above-mentioned second stream, which is sufficient to improve the combining efficiency of the above-mentioned first stream and the second stream, and provides a substantially constant temperature output air flow , for drying the above knitted material.
如上所述的方法,其中,该第一气流股包括温度较低的空气,而第二气流股包括温度较高的空气。The method as above, wherein the first air stream comprises cooler air and the second air stream comprises higher temperature air.
如上所述的方法,其中,第一温度为250°F,而第二温度为2440°F。The method as above, wherein the first temperature is 250°F and the second temperature is 2440°F.
本发明还提供一种在非织造材料制造中通过使上述非织造材料经遇基本恒温空气而对该非织造材料进行干燥的方法,其包括的步骤有:The present invention also provides a method of drying a nonwoven material in the manufacture of the nonwoven material by subjecting said nonwoven material to air at a substantially constant temperature, comprising the steps of:
a)将非织造材料插入一合适的干燥设备内,该材料的基重小于每平方米5克或大于每平方米200克;和a) nonwoven material having a basis weight of less than 5 grams per square meter or greater than 200 grams per square meter is inserted into a suitable drying apparatus; and
b)将温度基本恒定的空气流提供到上述非织造材料的表面,该基本恒温空气流的形成方式如下:b) providing an air flow of substantially constant temperature to the surface of the above-mentioned nonwoven material, the substantially constant temperature air flow being formed as follows:
c)将第一温度的第一气流引入一封闭件,使上述第一流股沿该封闭件的长度方向运行;c) introducing a first gas flow at a first temperature into an enclosure so that the first stream runs along the length of the enclosure;
d)利用设置在该封闭结构内的折流板阻断上述第一流股的流动;和d) blocking the flow of the above-mentioned first stream by means of a baffle arranged in the closed structure; and
e)将温度为与上述第一温度不同的第二温度的第二气流引入上述封闭件,上述第二流股在上述折流板的下游一位置处引入,上述第一流股越过上述折流板的流动的阻断,在上述折流板和上述第二流股引入点之间形成一足以提高上述第一流股和第二流股的结合效率的低压区,且提供基本恒温的输出空气流,用于干燥上述非织造材料。e) introducing into said enclosure a second gas stream having a temperature of a second temperature different from said first temperature, said second stream being introduced at a position downstream of said baffle, said first stream passing over said baffle The blocking of the flow of the above-mentioned baffle plate and the introduction point of the above-mentioned second stream forms a low-pressure zone sufficient to improve the combining efficiency of the above-mentioned first stream and the second stream, and provides an output air flow with a substantially constant temperature, For drying the above nonwoven materials.
如上所述的方法,其中第一气流包括温度较低的空气,而第二气流包括温度较高的空气。A method as described above, wherein the first air stream comprises cooler air and the second air stream comprises higher temperature air.
如上所述的方法,其中第一温度为250°F,而第二温度为2440°F。The method as above, wherein the first temperature is 250°F and the second temperature is 2440°F.
在本发明的优选实施例中,一锥形折流板设置在导管内第二气流输入源的上游处,该第二气流将与通过该导管流动的第一气流结合。该导管的结构包括平行且间隔开的壁,形成导管的顶和底。第二流股的入口通过导管的底插入,而该折流板的锥形方式是该折流板最宽的部分距该入口最近,随着它靠近导管的顶,它在导管的宽度方向上变窄。第一气流(例如,低温)通过该导管运行,而第二气流(例如,高温)通过该入口引入。第一流股越过折流板的流动使得沿该折流板最靠近入口的表面形成一低压区。由该入口引入的第二流股因此自然流入由本发明的折流板结构所形成的该低压区,从而与第一流股的高效混合。In a preferred embodiment of the invention, a conical baffle is positioned within the duct upstream of the input source of the second air flow which will combine with the first air flow flowing through the duct. The structure of the conduit includes parallel and spaced apart walls forming the top and bottom of the conduit. The inlet of the second stream is inserted through the bottom of the conduit, and the baffle is tapered in such a way that the widest part of the baffle is closest to the inlet, and as it approaches the top of the conduit, it extends across the width of the conduit. narrowed. A first gas stream (eg, low temperature) is run through the conduit, while a second gas stream (eg, high temperature) is introduced through the inlet. The flow of the first stream across the baffle creates a low pressure zone along the surface of the baffle closest to the inlet. The second stream introduced by the inlet thus naturally flows into the low pressure zone formed by the baffle structure of the present invention, thereby efficiently mixing with the first stream.
在本发明的另一个实施例中,折流板的结构可以是包括一靠近导管的底横贯该折流板的底边缘的狭缝区。此实施例特别适用于要使低温气流与高温气流结合之处所用的装置。具体地讲,该狭缝使低温气流能够从折流板下面通过,并被吸入该折流板前的低压区,从而为该折流板结构提供额外冷却。In another embodiment of the invention, the baffle may be configured to include a slit region across the bottom edge of the baffle near the bottom of the conduit. This embodiment is particularly suitable for installations where a low temperature gas flow is to be combined with a high temperature gas flow. Specifically, the slots allow cold air to pass under the baffle and be drawn into a low pressure area in front of the baffle, thereby providing additional cooling to the baffle structure.
本发明的装置和方法可用于结合任何两种不同的材料,例如蒸气和空气、低湿度空气和高湿度空气、氮气和氧气、或者甚至是两种液体(例如一种干净液体和一种乳化液或悬浮液)。具体地讲,这种结合两种不同材料流股(例如低温气体和高温气体)的能力在造纸工业和纺织工业非常有用。例如,在生产织造或针织织物,以及特定的非织造材料时,需要用均匀的气流(在该技术中通常称作“通过空气干燥”)对该材料进行“空气干燥”。根据本发明教授的,该均匀气流是通过利用插入两股气流之间的折流板使低温空气和高温空气结合而形成的。The apparatus and method of the present invention can be used to combine any two different materials, such as vapor and air, low humidity air and high humidity air, nitrogen and oxygen, or even two liquids (such as a clean liquid and an emulsion) or suspension). In particular, this ability to combine two streams of different materials (eg, low temperature gas and high temperature gas) is very useful in the paper and textile industries. For example, in the production of woven or knitted fabrics, and certain nonwoven materials, it is desirable to "air dry" the material with a uniform air flow (commonly referred to in the art as "through air drying"). According to the teaching of the present invention, this uniform air flow is created by combining cold air and high temperature air by means of baffles interposed between the two air streams.
在本发明的再又一个实施例中,可利用一种非锥形的折流板为两种或多种材料流股提供结合。具体地讲,非锥形折流板可用于高速的第一流股要与低速的第二流股结合的场合。在先有技术中,如果低速流股射入高速流股的通道,那么低速流股的入口可能会产生应变,因此使低速材料流误沿导管的底流动,使混合效率降低。根据本发明教授的,非锥形板结构的折流板起到了在高速流股通道中屏蔽该入口的作用。这样,低速材料能够沿导管的宽度扩展,使下游的混合效率更高。In yet another embodiment of the invention, a non-tapered baffle may be used to provide a combination of two or more material streams. In particular, non-tapered baffles may be used where a high velocity first stream is to be combined with a low velocity second stream. In the prior art, if the low-velocity stream is injected into the passage of the high-velocity stream, the inlet of the low-velocity stream may be strained, thereby causing the low-velocity material flow to flow along the bottom of the conduit and reduce the mixing efficiency. According to the teaching of the present invention, the baffles of non-tapered plate configuration serve to shield the inlet in the high velocity stream channel. This allows low velocity material to spread across the width of the conduit, allowing more efficient mixing downstream.
在本发明再进一步的一个实施例中,通过利用多个单独的折流板,每个折流板设置在多个入口之一的上游,可将多种不同的流股结合形成一种均匀的流股。该多个入口相对于封闭件可设置在任何所需的位置。例如,该入口可位于该封闭件的长度方向上,或者,也可沿该封闭件的宽度定位。另外,该折流板可由材料的实体件构成,或者也可包括一个或多个孔。In yet a further embodiment of the invention, by utilizing a plurality of individual baffles, each positioned upstream of one of the plurality of inlets, a plurality of different streams can be combined to form a uniform stream. The plurality of inlets may be located at any desired location relative to the closure. For example, the inlet may be located along the length of the enclosure, or alternatively may be located along the width of the enclosure. Additionally, the baffle may be formed from a solid piece of material, or may also include one or more apertures.
在下面讨论中和通过参见附图,本发明的这些和其它一些实施例将更加明显。These and other embodiments of the invention will be more apparent in the following discussion and by reference to the accompanying drawings.
附图的简要说明Brief description of the drawings
现在参见附图,在多个附图中相同参考标记表示相同的部件:Referring now to the drawings, like reference numerals designate like parts throughout the several views:
图1给出了本发明的混合装置的示例性实施例的透视图;Figure 1 provides a perspective view of an exemplary embodiment of a mixing device of the present invention;
图2为图1的装置沿2-2线所截取的截面图;Fig. 2 is a sectional view taken along line 2-2 of the device of Fig. 1;
图3为图1的装置沿3-3线所截取的另一截面图;Fig. 3 is another sectional view taken along line 3-3 of the device of Fig. 1;
图4给出了本发明的另一实施例,其包括一带狭缝的折流板;Figure 4 shows another embodiment of the invention comprising a baffle with a slit;
图5为图4的装置沿5-5线所截取的截面图;Fig. 5 is a sectional view taken along line 5-5 of the device of Fig. 4;
图6为图4的装置沿6-6线所截取的另一截面图;Fig. 6 is another sectional view taken along line 6-6 of the device of Fig. 4;
图7为图5的装置沿7-7线所截取的截面图,特别表示在示例折流板结构中所包括的狭缝区;FIG. 7 is a cross-sectional view of the device of FIG. 5 taken along line 7-7, particularly showing the slit region included in an exemplary baffle structure;
图8以透视图示出了本发明采用了多个折流板和相关输入口的另一实施例;Figure 8 shows in perspective view another embodiment of the invention employing multiple baffles and associated inlets;
图9为图8的装置沿9-9线所截取的截面图;和Figure 9 is a cross-sectional view of the device of Figure 8 taken along line 9-9; and
图10是表示采用了本发明装置同先有技术相比所取得的结果,特别是在使低温气体与高温气体结合时在温度“混合”方面改善效果的曲线图。Figure 10 is a graph showing the results obtained using the apparatus of the present invention compared to the prior art, particularly the improvement in temperature "mixing" when combining low temperature gas with high temperature gas.
优选实施例的详细说明Detailed Description of the Preferred Embodiment
图1示出了本发明的示例性的混合装置10。如图所示,该装置包括一设置在导管14内的锥形折流板12,折流板12的最宽边缘16邻接导管14的底壁18。折流板12而后向邻接导管14的顶壁22的一点20形成锥形。可以理解,尽管本实施例所示的导管14包括矩形横截面,但是具有任何预定几何形状的适用封闭件均可采用。另外,折流板12的几何形状也可根据具体情况而有所不同。对于图1的装置,所示折流板12包括锥形截面。其它锥形或非锥形的结构也可采用,并且也在本发明的精神和范围之内。Figure 1 shows an exemplary mixing device 10 of the present invention. As shown, the device includes a tapered
输入口24穿过导管14的底壁18凸出,且位于折流板12的下游(相对于通过导管14的流股的流动方向)输入口24的中心距折流板12的距离
d(如图2所示)是一个设计问题,作为距离
d的函数,在其间的区域提供或高或低的气压。The inlet 24 protrudes through the
在如图所示的实施例中,第一气流G1沿导管14的长度方向
1运行。气流G1可包括氧气、氮气、气流、空气或其它任何气态流股。第二气流G2通过管道26流动并通过输入口24引入导管14。根据本发明教授的,第一气流G1越过锥形折流板12的流动在折流板12的下游侧28形成一低压气腔。如图1所示,第二气流G2的通道由此进入该低压区。因此射入气体的射流随着自射入点的距离不断增大而扩展的自然趋势造成第二气流G2进入低压腔外侧的流动不断增加,并被卷入第一气流G1的流动之中,从而在第一气流G1的面(宽度)上均匀分布。因此由锥形折流板结构形成的紊流有助于使这种混合作用在第一个气流G的流动的前面扩散。In the illustrated embodiment, the first gas flow G 1 runs along the
可以理解,本发明通过采用锥形折流板所实现的混合还可以通过以下任何特性进一步加强:(1)改变导管12的横截面面积,从而控制气流G1的速度(例如,减小导管14在折流板12与输入口24的区域的横截面将提高气流G1的速度);(2)改变导管14的纵横比(从而控制气流G1的流动的前沿的宽度和幅面);或(3)改变第二气流G2排出输入口24的速度。It will be appreciated that the mixing achieved by the present invention through the use of conical baffles may be further enhanced by any of the following characteristics: (1) changing the cross-sectional area of
图2示出了图1中上述装置的侧视图。如该图所示,输入口24穿过导管24的底表面18凸出一预定高度
h。所示输入口24的中心位于距折流板12的后边缘30下游预定距离d处。高度
h和距离
d均可进行控制,为两流股提供最高效的混合,其中这些参数将是与两流股相关的各种条件(例如,温度、成分、湿度、流速等)的函数。正如在该图中清楚可见,折流板12的规格确定为使顶点20不与导管14的顶表面22相接触。因此气流G1围绕折流板12的流动产生低压腔区域32。因此随着自输入口24排出,气流G2自然倾向于进入压腔32并使气流G1和G2的混合效率提高。FIG. 2 shows a side view of the above-mentioned device in FIG. 1 . As shown in this figure, the input port 24 projects through the
如上所述,影响本发明的装置的效率的另一个参数是折流板的几何形状。图3以透视图形式给出了图1所示混合装置的顶视图。如图所示,折流板1 2的侧壁34的构成包括半径为
r的弧,其中已经发现此角位移能够控制低压腔32的整个尺寸,以及腔区域内的实际压力。As mentioned above, another parameter affecting the efficiency of the device of the invention is the geometry of the baffles. Figure 3 gives a top view of the mixing device shown in Figure 1 in a perspective view. As shown, the configuration of the
如上所述,利用本发明方法的一个特定环境是与织造和非织造纤维制造有关的“通气”干燥工艺,其中经常需要将低温气流和高温气流结合。图4给出了特别适合于这种环境的本发明的一个具体实施例。此环境适合于处理轻量软质纸产品,包括那些基重低于每平方米5克和大于每平方米200克的产品。具体地讲,混合装置50包括设于导管(或类似的封闭件)54内的折流板52,其中折流板52于距输入口56上游(相对于通过导管54的流股的流动方向)一预定距离
d(示于图5)。如图所示,第一低温室气流A高沿导管54的长度方向运行,并撞击在折流板52上,从而在折流板52的内部区域形成一低压腔56。第二高温空气流A高沿管道58流动并通过输入口56进入导管54。对于本发明的这种特定的低温/高温实施例,折流板52包括一通过使折流板52的底表面58距导管54的下表面60移开一预定的狭缝距离
g而形成的下狭缝区(示于图5)。如图4所示,折流板52包括多个孔53,而这些孔通过使较大量的低温空气从其中穿过而起到“冷却”折流板5 2的作用。可以理解,孔的数目和大小应受到限制,使其不妨碍由折流板结构形成的低压区。此具体实施例的另一特性是输入口56突入到导管54内的高度
h大于狭缝距离
g(参见图5)。与这种装置相关的特殊优点是流股A高的射入点将保持在A低的流动通道的上方。因此,流股A高的通道将不会妨碍流股A高,后者将不受妨碍地进入低压区。As noted above, one particular environment in which the method of the present invention is utilized is the "through-air" drying process associated with woven and nonwoven fiber manufacture, where a combination of low temperature and high temperature air streams is often required. Figure 4 shows a specific embodiment of the invention which is particularly suitable for this environment. This environment is suitable for handling lightweight soft paper products, including those with a basis weight below 5 grams per square meter and greater than 200 grams per square meter. Specifically, the mixing
图6给出了装置50的顶视图。如此具体实施例所示,锥形折流板52包括一个三角形的几何形状且包括一对以预定角度θ设置的侧壁62和64。低温空气流A低通过折流板52运行,从而在输入口56和折流板52之间形成一低压区66。因此,高温空气流A高将自然进入此低压腔并与流股A低高效混合,以形成输出气流A混。FIG. 6 gives a top view of the
图7包含图5所示装置沿7-7线所截的视图。在此图中,折流板和导管54的下表面60之间的狭缝区55很明显。如图所示,折流板52的只有较小的腿部57、59与表面60接触(出于稳定的目的),使A低的稳定流股能够通过狭缝区55并为折流板52提供冷却。Figure 7 contains a view of the device shown in Figure 5 taken along line 7-7. In this view, the
如上所述,利用根据本发明的折流板装置,在需要将低速流股射入高速流股的通道的情况下特别有利。图8给出了特别适合于这种目的的本发明的这样一种装置。另外,图8给出了一种包括一对折流板及与其相关的输入口的装置,如前面所讨论的,困为本发明的技术可以延及提供任何数目的不同材料的结合。实际上,尽管图中仅给出了两个示例性的折流板和相关的输入口,但是可以理解,可以采用任何所需数目的这种折流板和相关的输入口,且包括在本发明的实质和范围之内。另外,根据本发明教授的,多个折流板/输入口装置可以以任何所需的形式布置在封闭件内。例如,它们可以沿该封闭件的长度方向布置,或者沿该封闭件的宽度方向布置,或者是任何适用的组合形式。总体上讲,它们在封闭件内的位置(只要折流板设于其相关的输入口的上游)与本发明教授的无关。As mentioned above, the use of the baffle arrangement according to the invention is particularly advantageous where it is necessary to inject a low velocity stream into the channel of a high velocity stream. Figure 8 shows such a device of the invention which is particularly suitable for this purpose. Additionally, Figure 8 shows an arrangement comprising a pair of baffles and their associated inlets, as previously discussed, because the techniques of the present invention can be extended to provide any number of combinations of different materials. In practice, although only two exemplary baffles and associated inlets are shown in the drawings, it will be appreciated that any desired number of such baffles and associated inlets may be used and included in this within the spirit and scope of the invention. Additionally, multiple baffle/inlet arrangements may be arranged within the enclosure in any desired manner in accordance with the teachings of the present invention. For example, they may be arranged along the length of the closure, or along the width of the closure, or any suitable combination. In general, their position within the enclosure (as long as the baffles are located upstream of their associated inlets) is irrelevant to the teaching of the present invention.
具体参见图8,装置70包括一第一折流板72和一第二折流板74各折流板均设置为沿封闭件76的宽度方向延伸。第一高速材料流VH(例如,某种清洁液体)通过封闭件76运行,首先撞击和越过第一折流板76,随后冲击和越过第二折流板74。第二低速材料流VL1(例如,某种乳化剂)通过第一入口78引入封闭件76。同样,第三低速材料流股VL2(例如,某种不同成分和/或速度的乳化剂)通过第二输入口80引入封闭件76。根据本发明教授的,各输入口位于自其相关的折流板的下游预定距离处。如上述讨论的其它实施例,装置70能够在各折流板及其相关的输入口之间的区域形成低压区。因此,在此特定实施例中,该低压区使低速流股VL1和VL2能够以足够的量射入封闭件76,结果形成高效混合。另外,如图8所示,本发明的折流板结构可以以多个单元结构构成,具有遇过添加或去掉分离单元来产生不同效果的能力。例如,第二折流板段82可接附于第一折流板72的顶部,而第二部段82将使该折流板结构能适应更高速的材料。因此可以理解,经过一段时问,可以对折流板的大小和形状进行调节,以适应不同速度的材料,而这种调节最好是通过利用多个单元折流板结构来实现。Referring specifically to FIG. 8 , the
图9包含图8所示装置70沿9-9线所截取的侧面剖视图。如前面所讨论的,在将低速流股射入高速流股的情况下采用折流板特别有利。在没有本发明的折流板结构的传统装置中,高速流股VH的力将使第一输入口78弯曲,如图9中阴影所示。低速材料VL1的射入通道因此受到干扰,进一步降低了流股VH和VL1的混合效率。因此,采用根据本发明教授的折流板72起到了在高速流股和输入口之间设置一物理屏障的作用,使低速材料能沿所需方向射入。FIG. 9 contains a side cross-sectional view of the
本发明效果的数值图示于图10。具体地讲,图10是当采用本发明的装置结合不同温度的气流时,表示沿一个诸如导管14或管道54的腔室,温度随距离变化的图形。对于如图9所示的结果,具有环境温度为250°F的第一气流与具有环境温度为2440°F的第二气流结合,各气流的结合的效率通过评定在两股气流开始结合的点的下游任意点的温度变化来测量。图10中的图形包括在三个独立位置的这种温度变化的测量值:在越过高温气流的输入口的位置575英寸距离处的第一点B;在越过输入口799英寸距离处的第二点C;和在越过输入口983英寸距离处的第三点D。与传统的先有技术结构相关的温度变化在图9中以圆圈表示。采用本发明的折流板装置所带来的混合效率的提高从同样在三个位置B、C和D测量、以三角表示的温度变化看是明显的。特别是在B处,温度变化从500°F降至60°F。在C处,这种变化从320°F降至24°F;且最后,在D处,其变化从180°F降至仅16°F。可以理解,这些数据点代表的是温度变化(是相关点上沿封闭件的宽度位置的函数),不是混合气流的实际环境温度。A numerical graph of the effect of the present invention is shown in FIG. 10 . In particular, FIG. 10 is a graph showing temperature as a function of distance along a chamber, such as
Claims (45)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/US1998/017967 WO2000012202A1 (en) | 1998-08-28 | 1998-08-28 | Arrangement for combining dissimilar streams |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1314824A CN1314824A (en) | 2001-09-26 |
| CN1105595C true CN1105595C (en) | 2003-04-16 |
Family
ID=22267779
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN98814291A Expired - Fee Related CN1105595C (en) | 1998-08-28 | 1998-08-28 | Arrangement for combining dissimilar streams |
Country Status (13)
| Country | Link |
|---|---|
| EP (1) | EP1107821B1 (en) |
| JP (1) | JP2002523228A (en) |
| KR (1) | KR100515233B1 (en) |
| CN (1) | CN1105595C (en) |
| AR (1) | AR020352A1 (en) |
| AU (1) | AU746491B2 (en) |
| BR (1) | BR9815994A (en) |
| CO (1) | CO4960669A1 (en) |
| DE (1) | DE69815403D1 (en) |
| HK (1) | HK1039582A1 (en) |
| SV (1) | SV1999000142A (en) |
| TW (1) | TW457123B (en) |
| WO (1) | WO2000012202A1 (en) |
Families Citing this family (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1568410B1 (en) | 2004-02-27 | 2010-05-05 | Haldor Topsoe A/S | Apparatus for mixing fluid streams |
| DE102006004069A1 (en) * | 2006-01-28 | 2007-09-06 | Fisia Babcock Environment Gmbh | Method and device for mixing a fluid with a large gas flow rate |
| JP4961847B2 (en) * | 2006-06-12 | 2012-06-27 | いすゞ自動車株式会社 | Exhaust gas purification method and exhaust gas purification system |
| DE102007035226A1 (en) | 2007-07-25 | 2009-01-29 | J. Eberspächer GmbH & Co. KG | Flow guiding device and thus equipped exhaust system |
| US9144774B2 (en) | 2009-09-22 | 2015-09-29 | Turbulent Energy, Llc | Fluid mixer with internal vortex |
| US9708185B2 (en) | 2007-09-07 | 2017-07-18 | Turbulent Energy, Llc | Device for producing a gaseous fuel composite and system of production thereof |
| US8715378B2 (en) | 2008-09-05 | 2014-05-06 | Turbulent Energy, Llc | Fluid composite, device for producing thereof and system of use |
| US9310076B2 (en) | 2007-09-07 | 2016-04-12 | Turbulent Energy Llc | Emulsion, apparatus, system and method for dynamic preparation |
| JP2010538152A (en) | 2007-09-07 | 2010-12-09 | タービュレント エナジー インコーポレイテッド | Mixed fluid and method, apparatus and system for dynamically mixing fluid |
| US8871090B2 (en) | 2007-09-25 | 2014-10-28 | Turbulent Energy, Llc | Foaming of liquids |
| US8844495B2 (en) | 2009-08-21 | 2014-09-30 | Tubulent Energy, LLC | Engine with integrated mixing technology |
| FR2952311A1 (en) * | 2009-11-09 | 2011-05-13 | Renault Sa | Device for mixing intake air flow with recirculated exhaust gas flow in internal combustion engine of e.g. diesel type motor vehicle, has mixing plate integrated to air duct and comprising downstream edge located upstream of axis of pipe |
| US8317390B2 (en) * | 2010-02-03 | 2012-11-27 | Babcock & Wilcox Power Generation Group, Inc. | Stepped down gas mixing device |
| PT3009185T (en) | 2010-09-28 | 2017-11-14 | Dow Global Technologies Llc | Reactive flow static mixer with cross-flow obstructions and mixing method |
| DE102011077645A1 (en) | 2011-06-16 | 2012-12-20 | Bosch Emission Systems Gmbh & Co. Kg | Static mixer |
| EP2570179A1 (en) * | 2011-09-16 | 2013-03-20 | Air Liquide Deutschland GmbH | Method and apparatus for dynamic gas mixture production |
| JP6296884B2 (en) * | 2014-04-30 | 2018-03-20 | 三菱日立パワーシステムズ株式会社 | Flue gas desulfurization equipment |
| GB2533331A (en) * | 2014-12-16 | 2016-06-22 | Daimler Ag | Mixing device for an exhaust gas system |
| JP6377575B2 (en) * | 2015-05-21 | 2018-08-22 | 住友金属鉱山株式会社 | Fluid blowing apparatus and chemical reaction apparatus using the same |
| JP6690485B2 (en) * | 2016-09-20 | 2020-04-28 | 住友金属鉱山株式会社 | Chemical reactor and method for producing particles using the chemical reactor |
| CN108479325A (en) * | 2018-05-16 | 2018-09-04 | 山东志伟环保科技有限公司 | A kind of mixing arrangement of oxidation and denitration |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3893654A (en) * | 1972-03-18 | 1975-07-08 | Harunobu Miura | Mixing apparatus |
| US4498786A (en) * | 1980-11-15 | 1985-02-12 | Balcke-Durr Aktiengesellschaft | Apparatus for mixing at least two individual streams having different thermodynamic functions of state |
| US5159958A (en) * | 1991-07-18 | 1992-11-03 | Hydro Systems Company | Chemical eductor with integral elongated air gap |
| WO1993004761A1 (en) * | 1991-09-03 | 1993-03-18 | Guiseppe Ragusa | Air filter |
| US5433596A (en) * | 1993-04-08 | 1995-07-18 | Abb Management Ag | Premixing burner |
| CN1147212A (en) * | 1994-04-09 | 1997-04-09 | 汉克尔特罗森公司 | Method and device for merging at least two flow media |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR0161082B1 (en) * | 1995-10-11 | 1999-01-15 | 김광호 | Petroleum combustion equipment |
-
1998
- 1998-08-28 AU AU92112/98A patent/AU746491B2/en not_active Ceased
- 1998-08-28 JP JP2000567295A patent/JP2002523228A/en active Pending
- 1998-08-28 CN CN98814291A patent/CN1105595C/en not_active Expired - Fee Related
- 1998-08-28 WO PCT/US1998/017967 patent/WO2000012202A1/en not_active Ceased
- 1998-08-28 BR BR9815994-1A patent/BR9815994A/en not_active IP Right Cessation
- 1998-08-28 DE DE69815403T patent/DE69815403D1/en not_active Expired - Lifetime
- 1998-08-28 EP EP98944606A patent/EP1107821B1/en not_active Expired - Lifetime
- 1998-08-28 KR KR10-2001-7002480A patent/KR100515233B1/en not_active Expired - Fee Related
- 1998-08-28 HK HK02101142.3A patent/HK1039582A1/en unknown
-
1999
- 1999-08-27 AR ARP990104329A patent/AR020352A1/en unknown
- 1999-08-27 CO CO99054267A patent/CO4960669A1/en unknown
- 1999-08-27 SV SV1999000142A patent/SV1999000142A/en unknown
- 1999-10-29 TW TW088114685A patent/TW457123B/en not_active IP Right Cessation
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3893654A (en) * | 1972-03-18 | 1975-07-08 | Harunobu Miura | Mixing apparatus |
| US4498786A (en) * | 1980-11-15 | 1985-02-12 | Balcke-Durr Aktiengesellschaft | Apparatus for mixing at least two individual streams having different thermodynamic functions of state |
| US5159958A (en) * | 1991-07-18 | 1992-11-03 | Hydro Systems Company | Chemical eductor with integral elongated air gap |
| WO1993004761A1 (en) * | 1991-09-03 | 1993-03-18 | Guiseppe Ragusa | Air filter |
| US5433596A (en) * | 1993-04-08 | 1995-07-18 | Abb Management Ag | Premixing burner |
| CN1147212A (en) * | 1994-04-09 | 1997-04-09 | 汉克尔特罗森公司 | Method and device for merging at least two flow media |
Also Published As
| Publication number | Publication date |
|---|---|
| AU9211298A (en) | 2000-03-21 |
| EP1107821B1 (en) | 2003-06-04 |
| CN1314824A (en) | 2001-09-26 |
| AR020352A1 (en) | 2002-05-08 |
| JP2002523228A (en) | 2002-07-30 |
| KR20010106455A (en) | 2001-11-29 |
| KR100515233B1 (en) | 2005-09-16 |
| HK1039582A1 (en) | 2002-05-03 |
| EP1107821A1 (en) | 2001-06-20 |
| BR9815994A (en) | 2001-10-16 |
| DE69815403D1 (en) | 2003-07-10 |
| TW457123B (en) | 2001-10-01 |
| SV1999000142A (en) | 2000-07-06 |
| AU746491B2 (en) | 2002-05-02 |
| CO4960669A1 (en) | 2000-09-25 |
| WO2000012202A1 (en) | 2000-03-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1105595C (en) | Arrangement for combining dissimilar streams | |
| US5334012A (en) | Combustion chamber having reduced NOx emissions | |
| JP7078708B2 (en) | Flue gas mixer and method | |
| EP0430973B1 (en) | Static fluid flow mixing apparatus | |
| JP4368112B2 (en) | Apparatus and method for injecting liquid fuel into an air stream for a combustion chamber | |
| CN110822424B (en) | Static air mixer | |
| US11654391B2 (en) | Device for bringing a gas stream and a liquid stream into contact | |
| AU2011200135B2 (en) | Stepped down gas mixing device | |
| WO2002086303A1 (en) | Lobe mixer for jet engine | |
| FI70431C (en) | OVER ANCHORING FOR FRAMSTAELLNING AV FIBERMATTOR | |
| CN108800175A (en) | A kind of large size flue Three-dimensional Flow homogenization method and device | |
| KR102007156B1 (en) | Apparatus for diffusion of aerosol particles using multi-stage fans | |
| CN100432533C (en) | Overfire air port and boiler system | |
| CN115076717A (en) | Combustion liner | |
| CN1829565A (en) | Mixing system | |
| CN1253622C (en) | Air nozzles for fabric drying machines | |
| CN86108214A (en) | Improved methods for pellet handling | |
| US7146961B1 (en) | Engine air inlet flow enhancement device for internal combustion engines | |
| CN1646859A (en) | Method and device for controlling injection of primary and secondary air in an incineration system | |
| CN212494449U (en) | Industrial equipment and cyclone exhaust devices | |
| CN116398210A (en) | Circulating ventilation equipment and method for subway tunnel | |
| CN1813123A (en) | Inducing air | |
| JP3316372B2 (en) | Powder material dispersion equipment | |
| US20250134119A1 (en) | Cooling device for food products | |
| US20070062424A1 (en) | Apparatus and Method for Enhancing Heat and Mass Transfer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| C10 | Entry into substantive examination | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| REG | Reference to a national code |
Ref country code: HK Ref legal event code: WD Ref document number: 1039582 Country of ref document: HK |
|
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |