US1927376A - Process and apparatus for the mechanical production of froth - Google Patents

Description

Sept. 19, 1933. a. SCHRODER El AL 1,927,375

- PROCESS APPARATUS FORJTHE MECHANICAL PRODUCTION FROTH v Filed Feb. 3. 1930 :umnmumm w lllllllllllllll INVENTO'RS EINER ScHRb'DER 7 JAN 14.5. VAN DEuRs By ATTORNEY Patented Sept. f9, 1933 raocnss AND APPARATUS son THE ME- cnmcar. rnonuc'rron or morn Einer some" and Jan Arent Schoenheyder Deurs, Copenhagen, Denmark Application February 3, 1930, Serial No. 425,580, and in Germany February 6, 1929 'Claims. (Cl. 261-93) The present invention relates to an improved process and apparatus for the mechanical production of froth by directing a liquid and a gas into a vessel where said substances are converted 5 into froth by the relative motion of said. subgteances and rotary or stationary mixm' g mem- In processes'of this nature heretofore known,

the formation of froth has been effected in two W stages, viz, first by passing the gas through a filter which distributes the gas uniformly in the inflowing liquid, so that the'formation of froth is instantly promoted, and then by causing the froth ormed to continue passing through the vessel, which time it is exposed to the action of rotary stirring members, whereby the froth isbmken up into smaller bubbles.

' One disadvantage of such processes is that the quantity of froth produced per unit of time is,

limited, since the velocity of the stirring members must not be so high that separation of the heavy liquid from the light gas will be efiected, as a result of which the liquid would collect along the inner pe phery ofthe container, while the gas would escape. Y

' In the apparatuses of the above mentioned nature already known, the froth is free to pass axially through the apparatus, that is to say, no members are provided for forcing the froth to pass through the apparatus in such manner, viz, alternately towards the axis and the periphery of the stirring apparatus, that thorough and efiicient mixing is obtained. The froth necessarily partakes of the motion of the stirring members 85 and becomes atomized by being broken up between the stirring members and stationary vanes provided on the insideof the mixing vessel. The efleot thereby obtained, however, is not so efiicient as might be desired.

According to a previously known process foam hasbeenproducedbycausing gasorairtopass. through a porous substance immersed in a solution of a foam ge erating liquid, but with this process the gas or air was not mixed so intimately with the said liquid that the foam produced did not include a considerable amount of liquid, requiring removal from the foam; Further the bubbles of the foam, were not sufficiently fine to form a satisfactory foam.

Furthermore. it has been proposed to produce foam by passing a gas and a foam generating liquid under pressure througha mixing body comprising inner cavities, for instancepores or anchannels, by which the gas andliquid is Russuw streams impinging against and intersecting each other within the said body, thereby causing eddies or whirling motions, for securing intimate mixture of the said gas and liquid.

A mixing body having the character of a perous body offers a considerable resistance to the penetration of the gas and liquid and is also liable to become non-porous. Therefore such mixing bodies are not applicable if the rapid and continuous production of a considerable amount of foam is required. A mixing body comprising annular cavities or channels of considerable width in which eddies or whirling motions of the gas and liquid are produced is not able to secure a sumciently fine subdivision of the constituents and a homogeneous and stable foam.

The present invention has for its object to obtain the very eflicient formation of froth by whipping gas into liquid, the froth produced being far more stable than the froth heretofore produced by mechanical means. The main object of the invention is, in other words, to produce a froth in which the gas and the liquid are so intensively mixed that the froth practically consists merely of closely adjacent gas-filled bubbles separated by thin liquid films. In contradistinction to this the, froth heretofore produced by mechanical means frequently consists in fact of gas bubbles immersed in a larger or smaller quantity of liquid, which consequently to a certain extent acquires a frothy character.

:According to the present invention froth is mechanically produced by directing a gas and a froth forming liquid against stationary or rotary members in a mixing apparatus wires, or wire gauze, by or through which the gas and liquid are passed at high speed. The distance between two adjacent wires may be considerably larger than the diameter of the bubbles of foam to be produced.

By carrying out the mixing of the gas into the liquid under a pressure which is one half to ten atmospheres higher than atmospheric pressure, more gas will be dissolved in the liquid than is otherwise possible, and the gas inthe bubbles formed will be under a pressure exceeding that of the atmosphere and depending on=. the diameterof the bubbles and the surface tension of the liquid relatively to that of theses. when the walls of the bubbles become thinner and therebyobtain greater strength. At the. same time the expansion of the bubbles results .in an appreciable increase in the volume of the froth formed.

The equalization of the excess pressure will also.

cause the formation of a multitude of fine froth bubbles filling out the interstices between the larger bubbles produced by the mixing, so that. the froth becomes more stable than froth as here-.

tofore formed by mixing gas into liquid.

The production of froth under pressure possesses the further advantage that the production of a certain quantity of froth per unit of time can be performed in an apparatus which is smaller'than the apparatus in which heretofore a corresponding quantity of froth could be produced under ordinary atmospheric pressure.

The pressure on the liquid and gas to be whipped together in the mixing apparatus may be obtained by injecting the liquid'and the gas into the apparatus either separately by means of a separate pump for each or, as far as the liquid is concerned, by means of an ejector, or by pumping liquid and gas into the mixing apparatus by means of one and the same pump, in which case a preliminary mixing may be effected in the pump itself. If a gear-wheel pump or piston pump is used or some other pump which is able to pump a certain volume per unit of time independently of the counter acting head, then the liquid may be caused to flow so that it is pumped at such a velocity that any predetermined ratio of mixture between liquid and gas is obtained. At the discharge end, or in the discharge passage of the mixing apparatus a suitable resistance is provided against the motion of the froth, for example, by means of a valve, or by using as the discharge passage a pipe or hose offering a suitable resistance to the motion of the froth. By this means it becomes practicable to adjust the pressure in the mixing apparatus to any suitable magnitude.

In order to more clearly describe the present invention reference will be made to the accompanying drawing in which:

Fig. 1 is a diagrammatic side view of an apparatus shown partly in section and constructed according to the invention for the production of froth by the use of rotary mixing members;

Fig. 2 is a diagrammatic side view of a modified apparatus according to the invention for the production of froth by the use of stationary mixing members and s'Figs. 3 and 4 are end views of two different arrangements of stationary mixing members.

In Fig. 1 a is a cylindrical vessel, in one end of which is journalled a shaft 1), which is coupled to a motor 0. On the shaft p is mounted a series of stirring members q consisting suitably of radially disposed brushes; Between the brushes are disposed a number of transverse walls 1- and s, which are perforated alternately at their outer peripheries, i. e., the walls 1' are perforated immediately adjacent the wall of the vessel 11- and the walls s at their centers.

1) is a pump which is driven by a motor (not shown), which motor may be the same motor 0, which drives the shaft p. The water flows to the pump 1) through a pipe d, and a foaming agent, located in the container h, is fed continuously and in small amounts to the pipe d through the pipe which is fitted with an adjustable valve 2'.

Air flows in the direction of the arrow 10 in Fig. 1 to the pump through the pipe f, in which the pipe d terminates. The pump b drives the air and liquid through a pipe t into the container a, in which the said liquid and air under the action of the pump 1) will be forced to pass sinuously through the vessel a along the dotted path u due to the different locations of the perforations in the walls s and 1'.

During the passage of the liquid and air through the vessel a, the rotary-brushes q cause an intimate mixing of the air and liquid, so that the said two substances together form a dispersion under a pressure which depends upon the efl'iciency of the pump b and lies ordinarily between 1.5 and 11 atmospheres, so that the pressure in the vessel a would be 0.5 to 10 atmospheres higher than the atmospheric pressure. The dispersion is discharged either directly in the atmosphere or preferably through a hose m of shorter or longer length, which-hose terminates in an outlet nozzle n. In the vessel a stationary walls a: are inserted alternately with the walls r and s and are fitted with slits through which the liquid and air flow during their passage through the vessel a. The walls a: stop or impede rotary motion of the liquid.

In the modification shown in Fig. 2 the vessel 0. is in the form of a pipe fitted with transversely disposed stationary Wires g, Figs. 2 and 3, or networks, Figs. 2 and 4, which are perforated transversely from a centrally disposed shaft 1) on which the wires or networks are attached or supported in any suitable manner The liquid and air are forced to pass through the said wire gauze or stationary wires, whereby an intimate mixing of the two constituents, air and water, to form a dispersion, is caused. Above it is assumed that the gas used for preparing the foam was air, but any other suitable fluid, for instance, carbon dioxide, may be usedfor the said purpose. The foaming agent contained in the vessel 71. is ordinarily a solution of saponine. The arrows in Figs. 1' and 2 indicate the directions in which the different constituents or mixture of. constituents flow. An air-jet water pump (ejector) may be substituted for the pump 1) in Figs. 1 and 2, in which event a source of compressed air tobe fed through the ejector is connected to the pipe f.

We claim:--

l. A method of mechanically producing froth, comprising feeding a fluid and a froth-forming liquid simultaneously through a mixing chamber, maintaining a superatmospheric pressure in the said chamber and forming therein a dispersion of the said fluid in the said liquid, and allowing the dispersion to expand and convert, into fro h in consequence of the discharge of the dispersion from said chamber. 1

2. A method of mechanically producing froth, comprising feeding a fluid and a froth-forming liquid simultaneously and continuously through a mixing chamber, maintaining in the said chamber a superatmospheric pressure and forming in the chamber a dispersion of said fluid in said liquid, and allowing the dispersion to expand gradually and convert into froth in consequence jof the discharge of -the dispersion from said chamber.

3. A method of mechanically producing froth, comprising feeding a fluid and a froth-forming liquid simultaneously through a mixing chamber in the mutual proportions of weight in which they would have to be present instable foam 'at I, i atmospheric pressure, forming in the said chamber at a superatmospheric pressure a dispersion (if Said fluid in said liquid, and allowing the dis uid simultaneously and continuously through a. mixing chamber, maintaining in the said cham-' her a pressure at least 0.5 atmosphere er than the atmospheric pressure, forming in the saidchar'nber a dispersion of the said fluid in 'said liquid, and allowing the dispersion to ex- 16 pand gradually and convert into froth in conseance of the discharge ofthe dispersion from said chamber through a hose; 4

5. An apparatus formechanically producing foam, comprising a container, a plurality of stationary wires disposedtransversely in the interior of the container, aninlet and an outlet on the container, and means. for simultaneously supa flowpfr fluid and a flow of a foaming liquid Bil under a pressure at 1eastf0.5 atmosphere higher than atmospheric pressure and for forcing the said fluid and liquid against and past the said wires on to the outlet, thereby causing the .fluid to be dispersed in the liquid to form a dispersion which when discharged through the outlet expands and forms froth.

6. An apparatus for mechanically producing foam, comprising a container, a plurality of stationary wires disposed transversely in the interior -of the container, an inlet and an outlet on the through said hose, thereby causing the air to be dispersed in the liquid to form a dispersion EINER, scrmonmz. 7 JAN aRnN'rscnonm-mmm vex pr ons. s

.95 h which when discharged through thehose expands and forms froth, plying to the container through the said inlet

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