CH318803A - Device for generating directed, symmetrical to the vertical axis circulation flows of gases, vapors and liquids - Google Patents

Device for generating directed, symmetrical to the vertical axis circulation flows of gases, vapors and liquids

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Publication number
CH318803A
CH318803A CH318803DA CH318803A CH 318803 A CH318803 A CH 318803A CH 318803D A CH318803D A CH 318803DA CH 318803 A CH318803 A CH 318803A
Authority
CH
Switzerland
Prior art keywords
individual elements
dependent
vertical axis
individual
support members
Prior art date
Application number
Other languages
German (de)
Inventor
Walter Dipl Ing Kittel
Original Assignee
Walter Dipl Ing Kittel
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Walter Dipl Ing Kittel filed Critical Walter Dipl Ing Kittel
Publication of CH318803A publication Critical patent/CH318803A/en

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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
    • B01J19/32—Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14—Fractional distillation or use of a fractionation or rectification column
    • B01D3/16—Fractionating columns in which vapour bubbles through liquid
    • B01D3/22—Fractionating columns in which vapour bubbles through liquid with horizontal sieve plates or grids; Construction of sieve plates or grids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14—Fractional distillation or use of a fractionation or rectification column
    • B01D3/16—Fractionating columns in which vapour bubbles through liquid
    • B01D3/22—Fractionating columns in which vapour bubbles through liquid with horizontal sieve plates or grids; Construction of sieve plates or grids
    • B01D3/225—Dual-flow sieve trays
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14—Fractional distillation or use of a fractionation or rectification column
    • B01D3/16—Fractionating columns in which vapour bubbles through liquid
    • B01D3/24—Fractionating columns in which vapour bubbles through liquid with sloping plates or elements mounted stepwise
    • 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
    • B01J10/00—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
    • B01J10/02—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor of the thin-film type
    • 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
    • B01J19/2415—Tubular reactors
    • B01J19/2425—Tubular reactors in parallel
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/44—Fluidisation grids
    • 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
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
    • B01J2219/00078—Fingers
    • 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
    • B01J2219/00159—Controlling the temperature controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
    • 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
    • B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322—Basic shape of the elements
    • B01J2219/32203—Sheets
    • B01J2219/32206—Flat sheets
    • 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
    • B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322—Basic shape of the elements
    • B01J2219/32203—Sheets
    • B01J2219/32213—Plurality of essentially parallel sheets
    • 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
    • B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322—Basic shape of the elements
    • B01J2219/32203—Sheets
    • B01J2219/32237—Sheets comprising apertures or perforations
    • 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
    • B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322—Basic shape of the elements
    • B01J2219/32203—Sheets
    • B01J2219/32255—Other details of the sheets
    • B01J2219/32262—Dimensions or size aspects
    • 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
    • B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322—Basic shape of the elements
    • B01J2219/32203—Sheets
    • B01J2219/32265—Sheets characterised by the orientation of blocks of sheets
    • B01J2219/32268—Sheets characterised by the orientation of blocks of sheets relating to blocks in the same horizontal level
    • 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
    • B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322—Basic shape of the elements
    • B01J2219/32286—Grids or lattices
    • B01J2219/32289—Stretched materials
    • 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
    • B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/324—Composition or microstructure of the elements
    • B01J2219/32483—Plastics

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

  

  



  Vorrichtung zur Erzeugung von gerichteten, zur Vertikalachse symmetrischen    Zirkulationsstromungen    von Gasen, DÏmpfen und Flüssigkeiten
Zur technischen Durchführung von direk  ten,      Gegenstromprozessen, wie    z. B. Destillation, Absorption,   Extraktion, Gasreinigtmg, Kiih-      lung,    werden vertikal   angeordneteund    mei   stens zylindrisch ausgebildete Apparate, sog.



  Kolonnenapparate, gebraueht, durch welehe    die Medien z. B. Luft und Wasser geleitet werden. Diese Medien werden tangential in die Apparatur eingeführt und durch eingebaute Umlenkvorrichtungen in Zirkulation gesetzt.



   Die erfindungsgemässe Vorrichtung zur   Erzeugung    von gerichteten, zur Vertikalachse   symmetrischen Zirkulationsstromungen    von Gasen, Dampfen und Fl ssigkeiten, weist eine horizontale Bodenfläche mit einer Anzahl von gegen die FlÏche geneigt gerichteten   Durch-      lassstellen    auf und zeichnet sich dadurch aus, dass die Bodenfläche in Einzelelemente aufgeteilt und jedes Einzelelement auf vertikalen    Stutzorganen gelagert ist. Vorzugsweise kön-    nen die. Stützorgane symmetrisch um die Ver  tikalaehse    der Bodenfläche angeordnet sein.   



   Ausführungsformen der Vorrichtung sind    beispielsweise in der Zeiehnung dargestellt, und zwar zeigen :
Fig.   la--lu    verschiedene Ausbildungen einer Fläche,
Fig. 2a-2h zugeh¯rige FlÏchenelemente in Einzeldarstellung, in vergrössertem Massstab gezeichnet,
Fig. 3-6 Einzelheiten der Befestigung von verschiedenen Elementen an Tragorganen.



   Gemäss dem ersten Ausführungsbeispiel ist eine Vorrichtung vorgesehen, welche übereinander angeordnete B¯den oder Flächen aufweist, die den bekannten Austauschb¯den entsprechend mitDurchtrittsschlitzen ausgerüstet sind. Eine erste Ausführung einer solchen Bo  denfläche ist    in den Fig. 1a-1d dargestellt Die gezeigte Bodenfläche besteht nicht aus einem einzigen Teil, sondern ist aus Elementen   zu-      sammengesetzt,    die auf vertikalen   Stützorga-    nen gelagert sind. Die   Art und Weise    der La  gerung    ist spÏter beschrieben.



   Die Elemente sind im Grundriss z. B. gleichzeitige Dreiecke, Fig 2a-2d, die mit durch gestrichelte Linien dargestellten Sehlitzen   alllsgeriistet    sind. Diese bilden gegen die Bodenfläehe geneigte Durchlassöffnungen, die eine   Ablenkung des von wten nach    oben strömenden Mediums bewirken, so dass letztere annähernd parallel zur Bodenfläche aus den Schlitzen ausströmt. Die Elemente   unterschei-    den sieh nur   dureh    die   Schlitzrichtung, welche    mittels Richtungspfeilen angedeutet sind. Anstatt Dreiecke k¯nnen   auch Vierecke Verwen-      dung    finden, wie aus den Fig. 2e-2h ersichtlich ist.

   Diese Vierecke -weisen -wiederum gegen die   Bodenfläehe    geneigte schlitzartige   Offnun-    gen auf, die innerhalb eines Vierecks gleichgerichtet sind Aus den dargestellten Dreiecken und   Vierecken    lassen sich BodenflÏchen in einfacher Weise zusammenstellen Zweckmϯi  gerweise    werden die Einzelelemente so ge wählt, dass bei der durch die Fläche bewirkten   Umlenkung    des Strömungsmediums die tan   gentiale oder radiale Komponente bevorzugt.    wird.



   In der Fläche gemäss Fig. la ist die radiale Komponente bevorzugt, die Fläche gemäss Fig.   le    ist rein radial ausgerichtet, während die Fläche gemäss Fig. lb mit Schlitzen versehen ist zur Erzielung einer annähernd tangentialen Strömung.   InderFig.lo!ist    die Fläche so ausgebildet, dass bei der Strömung die rein   tangentia. le Richtung bevorzugt. wird.   



  Die Einzelelemente der Grundflächen sind in den zugehörigen Fig. 2a-2h dargestellt. Wie ferner aus den Fig.   la-lu    ersichtlich ist, k¯nnen innerhalb einer FlÏche sowohl   Dreieck-    als auch   Viereekelemente    Anwendung finden.



  Die relativ kleinen Flächenelemente sind mit wenig Materialabfall herstellbar.



   Die vorbeschriebene   Auflosung    der   Loden    flache in Flächenelemente gleicher Form und Grosse gestattet die Auflagerung derselben   reihenwesie    übereinander, mit wählbarem ge  genseitigem    Abstand auf gemeinsamen, durch ihre   Eckpunkte    oder zentral durch sie hindurchgeführte und vertikal angeordneten Stützorganen.



   Gemäss Fig. 3 sind die Elemente a und b dreieckförmig ausgebildet und weisen an ihren Ecken kreisbogenförmige Ausstanzungen auf, deren Durchmesser dem Aussendurchmesser der   Heiz-bzw. Kühlrohre    2, 3 entspricht. Die kreisbogenförmig ausgesparten Ecken können durch Stanzen, Pressen oder Giessen hergestellt werden. In der Fig. 4 sind viereckige Flächenelemente a und b gezeigt, die wiederum kreisförmig ausgestanzte Ecken aufweisen, deren Durchmesser dem Aussendurchmesser der Heiz- bzw K hlrohre 2,   3    entspricht.



   Die Befestig mg der Elemente ist auch aus den Fig. 5 und 11 ersichtlich. Die genannten Elemente werden im gewünschten   gegenseiti-    gen Abstande voneinander mit wahlweise gleicher oder wechselnder Ausrichtung ihrer    Durchlassöffnungen auf Zuganker l aufge-    reiht, welche sie im   Fläehenmittelpunkt    senk  reeht.    durchdringen Ein seitliches Verdrehen der Flächenelemente wird durch die   gleich-    zeitig als Führung dienenden   Heiz-bzw.      Kühl-    rohre 2 ; 3 verhindert Mit a und sind FlÏ  chenelemente    mit versehiedenen   Schlitzrich-    tungen bezeichnet, die in dem zwischen den Heiz- bzw.

   K hlrohren 2 vorhandenen freien Raum in wechselnder Reihenfolge überein  ander angeordnet    sind, so dass sich die Aus  stromungsrichtung    der Medien   etagenweise    ändert.



  



  Device for generating directed circulation flows of gases, vapors and liquids symmetrical to the vertical axis
For the technical implementation of direct th, countercurrent processes, such. B. Distillation, absorption, extraction, gas cleaning, cooling, are vertically arranged and mostly cylindrical devices, so-called.



  Column apparatus, used, through which the media z. B. air and water are passed. These media are introduced tangentially into the apparatus and put into circulation by built-in deflection devices.



   The device according to the invention for generating directed circulation flows of gases, vapors and liquids symmetrical to the vertical axis has a horizontal floor surface with a number of passage points inclined towards the surface and is characterized in that the floor surface is divided into individual elements and each individual element is mounted on vertical support members. Preferably, the. Support members can be arranged symmetrically around the ver tikalaehse of the floor surface.



   Embodiments of the device are shown for example in the drawing, namely show:
Fig. La - lu different configurations of a surface,
2a-2h associated surface elements in individual representation, drawn on an enlarged scale,
Fig. 3-6 Details of the attachment of various elements to supporting members.



   According to the first exemplary embodiment, a device is provided which has floors or surfaces arranged one above the other, which are equipped with passage slots in accordance with the known exchange floors. A first embodiment of such a floor surface is shown in FIGS. 1a-1d. The floor surface shown does not consist of a single part, but is composed of elements that are mounted on vertical support members. The method of storage is described later.



   The elements are z. B. Simultaneous triangles, Fig. 2a-2d, which are all-supported with seat braces shown by dashed lines. These form passage openings inclined towards the bottom surface, which deflect the medium flowing upwards from the bottom so that the latter flows out of the slots approximately parallel to the bottom surface. The elements can only be distinguished by the direction of the slot, which is indicated by the directional arrows. Instead of triangles, quadrilaterals can also be used, as can be seen from FIGS. 2e-2h.

   These quadrilaterals have, in turn, slit-like openings inclined towards the bottom surface, which are aligned within a quadrilateral. Bottom surfaces can be put together in a simple manner from the triangles and quadrilaterals shown. The individual elements are expediently selected so that the the surface caused deflection of the flow medium, the tangential or radial component is preferred. becomes.



   In the area according to FIG. 1 a, the radial component is preferred, the area according to FIG. 1e is aligned purely radially, while the area according to FIG. 1 b is provided with slots to achieve an approximately tangential flow. In Fig.lo! The surface is designed in such a way that the purely tangentia. le direction preferred. becomes.



  The individual elements of the base areas are shown in the associated FIGS. 2a-2h. As can also be seen from Figs. La-lu, both triangular and quadrangular elements can be used within a surface.



  The relatively small surface elements can be produced with little material waste.



   The above-described resolution of the loden flat in surface elements of the same shape and size allows the same rihenwesie to be superimposed, with selectable ge mutual spacing on common, through their corner points or centrally guided through them and vertically arranged support members.



   According to FIG. 3, the elements a and b are triangular and have circular arc-shaped punchings at their corners, the diameter of which corresponds to the outer diameter of the heating or heating element. Cooling tubes 2, 3 corresponds. The corners recessed in the shape of a circular arc can be produced by punching, pressing or casting. In FIG. 4, square surface elements a and b are shown, which in turn have circular punched-out corners, the diameter of which corresponds to the outer diameter of the heating or cooling pipes 2, 3.



   The fastening mg of the elements can also be seen from FIGS. 5 and 11. The elements mentioned are lined up at the desired mutual spacing from one another with either the same or alternating alignment of their passage openings on tie rods 1, which they perpendicular to the center of the area. penetrate A lateral rotation of the surface elements is caused by the heating or heating elements, which also serve as guides. Cooling tubes 2; 3 prevents with a and are surface elements with different slot directions, which are located in the area between the heating resp.

   Cooling pipes 2 existing free space are arranged one above the other in alternating order, so that the direction of flow of the media changes floor by floor.

Claims (1)

PATENTANSPRUCH Vorrichtung zur Erzeugung von gerichte- ten, zur Vertikalachse symmetrischen Zirkula- tionsstr¯mungen von Gasen, Dämpfen und Flüssigkeiten, welche Vorrichtung mindestens eine horizontale Flache mit einer Anzahl von gegen die Bodenfläehe geneigt gerichteten Durchla¯stellen aufweist, dadurch gekennzeichnet, dass die Bodenfläche in Einzelelemente aufgeteilt und jedes Einzelelement auf vertikalen Stützorganen gelagert ist. PATENT CLAIM Device for generating directed, symmetrical to the vertical axis circulation flows of gases, vapors and liquids, which device has at least one horizontal surface with a number of passages inclined towards the bottom surface, characterized in that the bottom surface in Divided individual elements and each individual element is mounted on vertical support members. ¯NTERANSPR¯CHE 1. Vorrichtung nach Patentanspruch, dadurch gekennzeichnet., da¯ die Einzelelemente e symmetrisch um die Vertikalaehse des Kolonnenbodens verteilt angeordnet sind (Fig. la bis ld). SUBSTANTIAL CLAIMS 1. Device according to patent claim, characterized in that the individual elements e are distributed symmetrically around the vertical axis of the column tray (Fig. La to ld). 2. Vorrichtung nach Patentanspruch und Unteranspruch 1, dadurch gekennzeichnet, da¯ die Einzelelemente aus gleichseitigen Dreiecken bestehen (Fig. 2a-2d). 2. Device according to claim and dependent claim 1, characterized in that the individual elements consist of equilateral triangles (Fig. 2a-2d). 3. Vorrichtung nach Patentanspruch und Unteranspruch l, dadurch gekennzeichnet, da. ¯ die Einzelelemente viereckig ausgebildet sind (Fig. 2e-2h) 4 Vorrichtung nach Patentanspruch und Unteransprueh 1, dadureh gekennzeiehnet, da¯ jedes Einzelelement gleichgerichtete Schlitze aufweist (Fig. 2a-2h). 3. Device according to claim and dependent claim l, characterized in that there. ¯ the individual elements are square (Fig. 2e-2h) 4 Device according to patent claim and dependent claim 1, dadureh gekennzeiehnet, dā each individual element has rectified slots (Fig. 2a-2h). 5. Vorrichtung nach Patentanspruch lmd Unteranspruch l, dadurch gekennzeichnet, dass in der Richtung der Vertikalachse sich erstreckende Stützorgane (44) vorhanden sind, die Mittel (2) zur Befestigung der Einzelelemente aufweisen. 5. Device according to claim lmd dependent claim l, characterized in that support members (44) extending in the direction of the vertical axis are present which have means (2) for fastening the individual elements. 6. Vorrichtung nach Patentanspruch und Unteransprüchen l und 5, dadurch gekenn zeichnet, dass die Einzelelemente in ihren Eck- punkten an den Stützorganen abgestützt sind. 6. Device according to claim and dependent claims 1 and 5, characterized in that the individual elements are supported in their corner points on the support members. 7. Vorrichtung nach Patentanspruch und Unteran, sprüchen 1 und 5, dadurch gekennzeichnet, da¯ die Einzelelemente (a, b) in ihrer Mitte von einem Stützorgan (1) durch gesetzt und an diesem abgestützt sind (Fig. 4 bis 6). 7. Device according to claim and Unteran, claims 1 and 5, characterized in that the individual elements (a, b) are set in their center by a support member (1) and are supported on this (Fig. 4 to 6). 8. Vorrichtung nach Patentanspruch, dadurch gekennzeichnet, dass die Vertikalstützen als Rohre ausgebildet sind zwecks Zu-und Abfuhr eines WÏrmeaustauschmediums. 8. Device according to claim, characterized in that the vertical supports are designed as tubes for the purpose of supply and Removal of a heat exchange medium. 9. Vorrichtung nach Patentanspruch und Unteranspruch 8, dadurch gekennzeichnet, dass die Abstützung der Einzelelemente aut dieselben im Flächenmitteilpunkt durchdrin- genden Zuganker (l) erfolgt, wobei die Einzelelemente ausgesparte Ecken aufweisen, durch welche Heiz-bzw. Kiihlrohre (2, 3) hindurchgeiührt sind. 2 9. Device according to claim and Sub-claim 8, characterized in that the support of the individual elements takes place on the same tie rods (1) penetrating in the area part point, the individual elements having recessed corners through which heating or Cooling tubes (2, 3) are passed through. 2
CH318803D 1952-03-07 1952-03-07 Device for generating directed, symmetrical to the vertical axis circulation flows of gases, vapors and liquids CH318803A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CH744906X 1952-03-07

Publications (1)

Publication Number Publication Date
CH318803A true CH318803A (en) 1957-01-31

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CH318803D CH318803A (en) 1952-03-07 1952-03-07 Device for generating directed, symmetrical to the vertical axis circulation flows of gases, vapors and liquids

Country Status (6)

Country Link
BE (1) BE518216A (en)
CH (1) CH318803A (en)
DE (1) DE950905C (en)
FR (1) FR1075488A (en)
GB (1) GB744906A (en)
NL (2) NL102607C (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3062517A (en) * 1956-09-07 1962-11-06 Shell Oil Co Gas-liquid contacting apparatus
EP0568713B1 (en) * 1992-05-05 1996-03-27 Deggendorfer Werft Und Eisenbau Gmbh Support grid for a tube bundle
US6425574B1 (en) * 1998-12-18 2002-07-30 Air Products And Chemicals, Inc. Mixed-resistance structured packing
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GB744906A (en) 1956-02-15
NL102607C (en)
BE518216A (en)
DE950905C (en) 1956-10-18
FR1075488A (en) 1954-10-18

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