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DE1270534B - Filler for mass transfer columns - Google Patents

Filler for mass transfer columns

Info

Publication number
DE1270534B
DE1270534B DEP1270A DE1270534A DE1270534B DE 1270534 B DE1270534 B DE 1270534B DE P1270 A DEP1270 A DE P1270A DE 1270534 A DE1270534 A DE 1270534A DE 1270534 B DE1270534 B DE 1270534B
Authority
DE
Germany
Prior art keywords
factor
fabric
quotient
mass transfer
weft
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.)
Pending
Application number
DEP1270A
Other languages
German (de)
Inventor
Dipl-Ing Dr Max Huber
Dr August Sperandio
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sulzer AG
Original Assignee
Sulzer AG
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 Sulzer AG filed Critical Sulzer AG
Publication of DE1270534B publication Critical patent/DE1270534B/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F25/00Component parts of trickle coolers
    • F28F25/02Component parts of trickle coolers for distributing, circulating, and accumulating liquid
    • F28F25/08Splashing boards or grids, e.g. for converting liquid sprays into liquid films; Elements or beds for increasing the area of the contact surface
    • F28F25/087Vertical or inclined sheets; Supports or spacers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D11/00Solvent extraction
    • B01D11/04Solvent extraction of solutions which are liquid
    • B01D11/0426Counter-current multistage extraction towers in a vertical or sloping position
    • B01D11/043Counter-current multistage extraction towers in a vertical or sloping position with stationary contacting elements, sieve plates or loose contacting elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D59/00Separation of different isotopes of the same chemical element
    • B01D59/28Separation by chemical exchange
    • B01D59/32Separation by chemical exchange by exchange between fluids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J10/00Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
    • B01J10/02Chemical 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/32Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details 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
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details 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
    • B01J2219/322Basic shape of the elements
    • B01J2219/32286Grids or lattices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details 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
    • B01J2219/324Composition or microstructure of the elements
    • B01J2219/32408Metal

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Woven Fabrics (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Description

BUNDESREPUBLIK DEUTSCHLANDFEDERAL REPUBLIC OF GERMANY

DEUTSCHESGERMAN

PATENTAMTPATENT OFFICE

AUSLEGESCHRIFTEDITORIAL

Int. Cl.:Int. Cl .:

BOIjBOIj

Deutsche Kl.: 12 e-1/03 German class: 12 e- 1/03

Nummer; 1 270 534Number; 1 270 534

Aktenzeichen: P 12 70 534.9-43File number: P 12 70 534.9-43

Anmeldete;·: 10. August 1964Registered; ·: August 10, 1964

Auslegetag: 20. Juni 196»Opening day: June 20, 196 »

Das Hauptpatent betrifft Füllkörper für Stoffaustauschkolonnen, bestehend aus einem Gewebe, dessen Schuß- und Kettfäden gleichen oder verschiedenen Durchmesser aufweisen, der höchstens 0,6 mm beträgt, wobei das Gewebe mindestens in Schuß- oder Kettfadenrichlung so ausgebildet ist, daß das Produkt eines sloffabhängigen Faktors A und eines strukturabhängigen Faktors B mindestens den Wert 38 hat, wobei der Faktor A gebildet ist aus dem Quotienten der Oberflächenspannung der Flüssigkeit gegen ihren Dampf (dyn/cm) zu der Flüssigkeitsdichte (p/cm3), multipliziert mit dem cos des Benelzungswinkels, und der Faktor B aus dem Verhältnis des Fadendurchmessers d zur lichten Maschenweite α gebildet ist.The main patent relates to packing for mass transfer columns, consisting of a fabric, the weft and warp threads of which have the same or different diameter, which is at most 0.6 mm, the fabric being designed at least in the weft or warp thread direction so that the product of a sloff-dependent factor A and a structure-dependent factor B has at least the value 38, where the factor A is formed from the quotient of the surface tension of the liquid against its vapor (dyn / cm) to the liquid density (p / cm 3 ), multiplied by the cos of the wetting angle, and the factor B is formed from the ratio of the thread diameter d to the clear mesh size α .

Kolonnen mit solchen Füllkörpcrn können zur Durchführung von Destillationen, Rektifikationen, Absorptionen, Extraktionen, zur Durchführung chemischer Reaktionen, wie ζ. Β Abtrennung isotoper Elemente, aus einem Stoff auf Grund einer chemischen Austauschreaktion u. dgl. verwendet werder.Columns with such packing elements can be used to carry out distillations, rectifications, Absorptions, extractions, to carry out chemical reactions, such as ζ. Β Separation isotopic Elements made of a substance due to a chemical exchange reaction and the like are used.

Werden Füllkörper aus Gewebe der vorstehend beschriebenen Art in derartigen Kolonnen verwendet, so müssen diese Füllkörper vor Betrieb nicht geflutet werden, da diese Gewebe selb-.tbenctzend sind.If packing made of fabric of the type described above is used in such columns, This means that these fillers do not have to be flooded before operation, as these fabrics are self-contained.

Die Einhaltung des Zahlen volles 38 für das Produkt Füllkörper für StoffaustauschkolonnenCompliance with the full number 38 for the product Packing for mass transfer columns

Zusatz zum Patent: 1 242 187Addendum to the patent: 1 242 187

Anmelder:Applicant:

Gebrüder Sulzer Aktiengesellschaft,Sulzer Brothers Aktiengesellschaft,

Winterthur (Schweiz)Winterthur (Switzerland)

Vertreter:Representative:

Dipl.-Ing. H. Marsch, Patentanwalt,Dipl.-Ing. H. Marsch, patent attorney,

4000 Düsseldorf, Lindemannstr. 314000 Düsseldorf, Lindemannstr. 31

Als Erfinder benannt:Named as inventor:

Dipl.-Ing. Dr. Max Huber,Dipl.-Ing. Dr. Max Huber,

Dr. August Sperandio, Winterthur (Schweiz)Dr. August Sperandio, Winterthur (Switzerland)

Beanspruchte Priorität:
Schweiz vom 3. September 1963 (10 919),
vom 24.JuIi 1964(9691)
Claimed priority:
Switzerland of September 3, 1963 (10 919),
of June 24, 1964 (9691)

JJ.LJJ.L

'Jl.'Jl.

COSCOS

s η ■ — = .-1 · B ( mit --- = B s η ■ - = .-1 · B ( with --- = B

ergibt bei bestimmtem A und d zugleich einen Maximalwert für den Abstand α für die Maschenweite. Die Werte für die Dichte der Flüssigkeil und der Oberflächenspannung gegen die Dampfphase sind aber oft mit einer Unsicherheit behaftet. Man begegnet dieser Unsicherheit mit einer Verkleinerung Scr Maschenweite a. Damit wird der Zahknwert des Produktes A ■ B größer und hierdurch die Voraussetzung für die Selbst benetzung des Gewebes günstiger. Wenn die lichte Maschenweile jedoch sehr klein wird, bewirkt dieses einen unter Umständen stark verminderten Wirkungsgrad für den Stoffaustausch.at a certain A and d simultaneously results in a maximum value for the distance α for the mesh size. However, the values for the density of the liquid wedge and the surface tension against the vapor phase are often fraught with uncertainty. This uncertainty is countered by reducing the size of the mesh size a. This increases the tooth value of the product A ■ B and thus the prerequisite for the self-wetting of the tissue is more favorable. However, if the clear mesh width becomes very small, this may result in a greatly reduced efficiency for the mass transfer.

Die Erfindung besteht in der Auffindung desThe invention consists in finding the

oberen Grenzwertes 2,5 für den Quotienten ' . wo-upper limit value 2.5 for the quotient '. Where-

""

durch ein guter Stoffaustausch gewährleistet ist. Daß das mit der Erfindung angestrebte Ziel durch Einhaltung der vorstehenden Forderung erreicht wird, konnte durch experimentelle Untersuchungen an einer Reihe von Geweben bestätigt werden.is guaranteed by a good exchange of substances. That the aim pursued by the invention through Compliance with the above requirement is achieved through experimental investigations a number of tissues can be confirmed.

In einem Ausführungsbeispiel der Erfindung sollen die Abmessungen eines Gewebes für die Füllkörper einer Rektifizkrkolonne bestimmt werden, in der ein Gemisch vi η cis-Dekalin/trans-Dekalin bei 100 C getrennt werden soll. Für die genannte flüssigkeit ist die DichteIn one embodiment of the invention, the dimensions of a fabric for the packing a rectification column can be determined in the a mixture vi η cis-decalin / trans-decalin at 100 ° C should be separated. For the liquid mentioned is the density

o, = 0,79 --T ,
cm3
o, = 0.79 - T ,
cm 3

.die Oberflächenspannung.the surface tension

-T1 = 24 d-yü cm-T 1 = 24 d - y ü cm

und der Benet/ungswinkel « = 0 bei Verwendung von rostfreiem Stahl.and the wetting angle «= 0 when used of stainless steel.

Setzt man diese Werte in die angegebene Formel A ■ B 2: 38 ein, so ergibt sich daraus, dali /ur Erreichung einer Selbst benetzung des Gewebes der Quotient ' ^ 1,2 sein muß.If these values are inserted into the given formula A · B 2: 38, it follows that the quotient must be '^ 1.2 to achieve self-wetting of the tissue.

Um einen guten Stoffaustausch zu erreichen, soll gemäß der vorliegenden Erfindung die Beziehung d- ^ 2,5 erfüllt sein.In order to achieve a good mass transfer, the relationship d - ^ 2.5 should be fulfilled according to the present invention.

Da, wie erwähnt, die Zahlenwerte der in die Formel einzusetzenden Siol'feigenschaften mit einem gevissenSince, as mentioned, the numerical values in the formula Siol'fe properties to be used with a gevissen

SO" H-C 4>SO " HC 4>

Unsicherheitsfaktor behaftet sind, wird man in diesem ./ Fall zweckmäßig das Verhältnis von d zu α etwa 1,6 wählen. Bei einem Drahtdurchmesser d = 0,016 cm ergibt sich dann für a — 0,010 cm.If there is an uncertainty factor, the ratio of d to α approximately 1.6 will be chosen in this ./ case. With a wire diameter d = 0.016 cm, the result for a is - 0.010 cm.

Während durch die eingangs angegebene Beziehung A ■ B ^ 38 bei gegebenem A und d eine Grenze für die größte Maschenweite α gegeben wird, bei der noch eine Selbstbenetzung des Gewebes verwirklicht werden kann, so gibt die vorliegende Erfindung bei gegebenem d eine untere Grenze für die Maschenweite α an, bei der lichte Maschenöffnungen von einer Größe gewährleistet sind, bei denen ein guier Stoffaustausch, in dem die Maschenöffnungen bedeckenden Flüssigkeitsfilm mit der Dampfphase von beiden Seiten her erfolgen kann. While the relationship A ■ B ^ 38 given at the beginning, given A and d , gives a limit for the largest mesh size α at which self-wetting of the fabric can still be achieved, the present invention gives a lower limit for the given d Mesh size α at which clear mesh openings of a size are guaranteed in which a good exchange of substances, in which the liquid film covering the mesh openings can take place with the vapor phase from both sides.

Vorteilhaft sind die Füllkörper so in der Kolonne angeordnet, daß die Kapillarwirkung in der Horizontalen auftritt, d. h., der engste Maschenabstand a soll zwischen zwei übereinanderliegenden horizontalen Drähten bzw. Fäden liegen.The packing elements are advantageously arranged in the column in such a way that the capillary action occurs horizontally, ie the narrowest mesh spacing a should lie between two horizontal wires or threads lying one above the other.

Claims (2)

Patentansprüche:Patent claims: 1. Füllkörper für Stoffaustauschkolonnen, bestehend aus einem Gewebe, dessen Schuß- und Kettfaden gleichen oder verschiedenen Durchmesser aufweisen, der höchstens 0,6 mm beträgt, wobei das Gewebe mindestens in Schuß- oder Kettfadenrichtung so ausgebildet ist, daß das Produkt eines stoffabhängigen Faktors A und eines struklurabhängigen Faktors B mindestens den Wert 38 hat, wobei der Faktor A gebildet ist aus dem Quotienten der Oberflächenspannung der Flüssigkeit gegen ihren Dampf (dyn/cm) zu der Flüssigkeitsdichte (o/cm3), multipliziert mit . dem cos des Benetzungswinkels, und der Faktor B aus dem Verhältnis des Fadendurchmessers d zur lichten Maschenweite α gebildet ist nach Patent 1242 187, dadurch gekennzeichnet, daß die Abmessungen des Fadendurchmessers d und der Maschenweite α mindestens in Schuß- oder Kettfadenrichtung . so gewählt1. Packing for mass transfer columns, consisting of a fabric whose weft and warp threads have the same or different diameter, which is at most 0.6 mm, the fabric being designed at least in the weft or warp thread direction so that the product of a fabric-dependent factor A. and a structure-dependent factor B has at least the value 38, the factor A being formed from the quotient of the surface tension of the liquid versus its vapor (dyn / cm) to the liquid density (o / cm 3 ), multiplied by. the cos of the wetting angle, and the factor B from the ratio of the thread diameter d to the clear mesh size α is formed according to patent 1242 187, characterized in that the dimensions of the thread diameter d and the mesh size α at least in the weft or warp thread direction. so chosen werden, daß der Quotient - höchstens einenbe that the quotient - at most one Wert von 2,5 erreicht.Achieved a value of 2.5. 2. Füllkörper nach Anspruch 1, dadurch gekennzeichnet, daß der Quotient '- zwischen dem Zahlenwert 1,2 und 2,5 hegt.2. Filler body according to claim 1, characterized in that the quotient '- between the The numerical value is 1.2 and 2.5. 309 560,425 6. 68 0 Bundesdruckerei Berlin309 560.425 6. 68 0 Bundesdruckerei Berlin
DEP1270A 1963-09-03 1964-08-10 Filler for mass transfer columns Pending DE1270534B (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CH1091963A CH412806A (en) 1963-09-03 1963-09-03 Process for the production of fabrics for packing in mass transfer columns
CH969164A CH430658A (en) 1963-09-03 1964-07-24 Process for the production of fabrics for packing in mass transfer columns

Publications (1)

Publication Number Publication Date
DE1270534B true DE1270534B (en) 1968-06-20

Family

ID=25705157

Family Applications (2)

Application Number Title Priority Date Filing Date
DES87299A Pending DE1242187B (en) 1963-09-03 1963-09-14 Filler for mass transfer columns
DEP1270A Pending DE1270534B (en) 1963-09-03 1964-08-10 Filler for mass transfer columns

Family Applications Before (1)

Application Number Title Priority Date Filing Date
DES87299A Pending DE1242187B (en) 1963-09-03 1963-09-14 Filler for mass transfer columns

Country Status (5)

Country Link
BE (1) BE652484A (en)
CH (2) CH412806A (en)
DE (2) DE1242187B (en)
GB (1) GB1020190A (en)
NL (2) NL6410270A (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3997632A (en) * 1971-11-24 1976-12-14 Julius Montz Gmbh Monofil fabric for use as a perpendicular trickle wall in exchange columns
US4183681A (en) * 1978-05-19 1980-01-15 Exxon Research & Engineering Co. Emulsion preparation method using a packed tube emulsifier
CH664091A5 (en) * 1985-01-30 1988-02-15 Sulzer Ag PACKING BODY MADE OF THIN, FILM-LIKE MATERIAL FOR FABRIC AND HEAT EXCHANGE COLUMNS BETWEEN LIQUID AND GASEOUS PHASES.
US4929399A (en) * 1988-03-17 1990-05-29 Union Carbide Industrial Gases Technology Inc. Structured column packing with liquid holdup
US5950455A (en) * 1998-04-01 1999-09-14 Praxair Technology, Inc. Cryogenic air separation system for feed air flow disturbances
FR2929134B1 (en) * 2008-03-28 2010-12-31 Air Liquide METHOD FOR MANUFACTURING A CROSS-CROSSOVER TRIM

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE853287C (en) * 1941-12-22 1952-10-23 Basf Ag Filler for columns
US2615699A (en) * 1946-02-28 1952-10-28 Ici Ltd Contacting liquids with gases or vapors

Also Published As

Publication number Publication date
NL129702C (en)
DE1242187B (en) 1967-06-15
NL6410270A (en) 1965-03-04
GB1020190A (en) 1966-02-16
CH430658A (en) 1967-02-28
CH412806A (en) 1966-05-15
BE652484A (en) 1965-03-01

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