DE19515691A1 - Dispersion of finely-divided solids in liquid - Google Patents

Dispersion of finely-divided solids in liquid

Info

Publication number
DE19515691A1
DE19515691A1 DE19515691A DE19515691A DE19515691A1 DE 19515691 A1 DE19515691 A1 DE 19515691A1 DE 19515691 A DE19515691 A DE 19515691A DE 19515691 A DE19515691 A DE 19515691A DE 19515691 A1 DE19515691 A1 DE 19515691A1
Authority
DE
Germany
Prior art keywords
dispersion
finely
finely divided
solids
liquid
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.)
Ceased
Application number
DE19515691A
Other languages
German (de)
Inventor
Hans-Michael Dipl Ing Sulzbach
Juergen Dipl Ing Wirth
Robert Dr Eiben
Hans Dr Hettel
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.)
Bayer AG
Hennecke GmbH
Original Assignee
Bayer AG
Hennecke GmbH
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 Bayer AG, Hennecke GmbH filed Critical Bayer AG
Priority to DE19515691A priority Critical patent/DE19515691A1/en
Priority to JP8122790A priority patent/JPH08302027A/en
Priority to CA002174893A priority patent/CA2174893A1/en
Priority to KR1019960013135A priority patent/KR960037106A/en
Priority to NO961679A priority patent/NO961679D0/en
Publication of DE19515691A1 publication Critical patent/DE19515691A1/en
Ceased legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50Mixing liquids with solids
    • B01F23/51Methods thereof
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50Mixing liquids with solids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/70Pre-treatment of the materials to be mixed
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/70Pre-treatment of the materials to be mixed
    • B01F23/703Degassing or de-aerating materials; Replacing one gas within the materials by another gas

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

Air present between finely-divided solid particles is at least partially displaced before dispersion by CO2. Also claimed are: (i) a method of mfg. plastics reinforced by finely-divided solids by dispersion of the solids in liquid plastics precursor products with displacement of air before dispersion by CO2, and (ii) a method of mfg. soft polyurethane foam materials modified by finely-divided solids by dispersion of the finely-divided solids in at least one component of the polyurethane reactive mixture, with displacement of air by CO2.

Description

Ein Problem bei der Dispergierung von feinteiligen Feststoffen in Flüssigkeiten ist die zwischen den feinteiligen Feststoffteilchen eingeschlossene Luft.There is a problem with the dispersion of finely divided solids in liquids the air trapped between the finely divided solid particles.

Die Einarbeitung von Feststoffteilchen in eine Flüssigkeit erfolgt entweder im Batch-Betrieb oder kontinuierlich. Bei der Einarbeitung im Batch-Betrieb werden die feinteiligen Feststoffe auf die in einem Rührbehälter vorgelegte Flüssigkeit aufgeschüttet und eingerührt. Die Feststoff-Schüttungen enthalten aber 30 bis 60 Vol-% Luft zwischen den Feststoffteilchen. Im Falle der teilweisen Fluidi­ sierung beim Aufbringen der Feststoffe auf die Flüssigkeit kann der Anteil der in die Schüttung eingeschlossenen Luft sogar bis 80 Vol-% betragen. Diese Luft wird beim Einrühren des Feststoffes in die Flüssigkeit in Form von feinteiligen Luft­ blasen in der Flüssigkeit dispergiert. Nach Abstellen des Rührers treten die Glas­ bläschen unter Ausbildung eines Schaumes auf der Oberfläche der Flüssigkeit aus. Die erforderliche Zeit für die Segregation der Gasbläschen in Form von Schaum auf der Flüssigkeitsoberfläche und die anschließend erforderliche Kollabierung des Schaumes ist abhängig von der Viskosität der Flüssigkeit und deren Oberflächen­ spannung. Innerhalb technisch realisierbarer Zeiten können häufig blasenfreie Fest­ stoffdispersionen nicht erhalten werden. Es wurde daher bereits vorgeschlagen, die Dispergierung von Feststoffen in Flüssigkeiten unter Vakuum vorzunehmen. Dies erfordert jedoch erheblichen apparativen Aufwand.Solid particles are incorporated into a liquid either in the Batch operation or continuously. When training in batch mode the finely divided solids onto the liquid placed in a stirred tank heaped up and stirred in. The solid fillings contain 30 to 60 vol% air between the solid particles. In the case of partial fluidi When the solids are applied to the liquid, the proportion of in the bed of trapped air can even be up to 80% by volume. This air will when the solid is stirred into the liquid in the form of finely divided air bubbles dispersed in the liquid. After switching off the stirrer, the glass is kicked blow out to form a foam on the surface of the liquid. The time required for the segregation of the gas bubbles in the form of foam on the liquid surface and the subsequent collapse of the Foam depends on the viscosity of the liquid and its surfaces tension. Bubble-free festivals can often take place within technically feasible times dispersions are not obtained. It has therefore already been proposed that Dispersion of solids in liquids under vacuum. This however, requires considerable equipment.

Bei der kontinuierlichen Einmischung von feinteiligen Feststoffen in Flüssigkeiten stehen im allgemeinen keine ausreichenden Zeiträume für die Segregation disper­ gierter Gasblasen zur Verfügung, so daß zur Gewährleistung blasenfreier Fest­ stoffdispersionen nach dem Stand der Technik die Dispergierung unter Vakuum, zumindest unter gegenüber Normaldruck erheblich reduziertem Druck durchgeführt werden muß.With the continuous mixing of finely divided solids in liquids there are generally insufficient periods for segregation disper Gier gas bubbles available, so that to ensure bubble-free hard state-of-the-art material dispersions, dispersion under vacuum,  carried out at least under considerably reduced pressure compared to normal pressure must become.

Erfindungsgemäß wird nun vorgeschlagen, zur Herstellung blasenfreier Feststoff­ dispersionen vor der Dispergierung feinteiliger Feststoffe die zwischen den Fest­ stoffteilchen befindliche Luft zumindest teilweise durch Kohlendioxid auszutau­ schen.According to the invention, it is now proposed to produce bubble-free solid dispersions before dispersing fine particulate matter between the solid Particulate air at least partially thawed by carbon dioxide .

Aufgrund der hohen Löslichkeit von Kohlendioxid in nahezu allen organischen oder anorganischen Flüssigkeiten wird das zwischen den Feststoffteilchen in die Flüssigkeit eingetragene Kohlendioxid in der Flüssigkeit gelöst, so daß es nicht zur Ausbildung von Blasen bzw. Schaum kommt. Im allgemeinen ist die Löslichkeit von Kohlendioxid so hoch, daß die erfindungsgemäße Dispergierung sogar bei erhöhtem Druck durchgeführt werden kann, ohne daß es nach der Entspannung auf Normaldruck zur Ausbildung von Gasblasen in der Dispersion kommt. Dies ist insbesondere dann von Bedeutung, wenn an den Dispergierschritt weitere Verfah­ rensschritte angeschlossen werden sollen, so daß während der Dispergierung ein solcher Überdruck herrscht, der zur Überwindung des Strömungswiderstandes in nachgeschalteten Leitungen und Weiterverarbeitungsaggregaten ausreicht, ohne daß zwischengeschaltete Pumpen erforderlich sind.Due to the high solubility of carbon dioxide in almost all organic or inorganic liquids that is between the solid particles in the Liquid entered carbon dioxide dissolved in the liquid so that it is not used Formation of bubbles or foam occurs. In general, the solubility of carbon dioxide so high that the dispersion of the invention even at increased pressure can be carried out without it after relaxation Normal pressure for the formation of gas bubbles in the dispersion comes. This is This is particularly important if further processes are carried out on the dispersing step rens steps should be connected so that during the dispersion such overpressure prevails which in order to overcome the flow resistance in downstream lines and processing units is sufficient without intermediate pumps are required.

Insbesondere geeignet ist das erfindungsgemäße Dispergierverfahren für die Dispergierung von feinteiligen Feststoffen in Flüssigkeiten mit geringem Lösungs­ vermögen für Luft, d. h. für Sauerstoff und/oder Stickstoff, und hohem Lösungs­ vermögen für Kohlendioxid.The dispersion method according to the invention is particularly suitable for the Dispersion of finely divided solids in liquids with a low solution assets for air, d. H. for oxygen and / or nitrogen, and high solution assets for carbon dioxide.

Bevorzugte Flüssigkeiten sind flüssige Vorläuferverbindungen für die Herstellung von Kunststoffen. Insbesondere geeignet ist das Verfahren dann, wenn Formge­ bungsverfahren für den Kunststoff eingesetzt werden, bei denen der Kunststoff bei Umgebungsdruck aushärtet, da in solchen Fällen eine nachträgliche Auflösung von Gasblasen im Kunststoff, wie es z. B. im Falle der Formgebung unter Anwendung von hohem Forminnendruck erfolgt, nicht stattfindet. Der Vorteil der vorliegenden Erfindung kommt demgemäß insbesondere bei der Herstellung füllstoffhaltiger Kunststoffe, bei denen die Formgebung unter Anwendung von Gießverfahren mit oder ohne Verschäumung erfolgt, zum Tragen. Preferred liquids are liquid precursors for manufacture of plastics. The method is particularly suitable when molding Exercise procedures are used for the plastic, in which the plastic Ambient pressure cures, because in such cases a subsequent resolution of Gas bubbles in the plastic, as z. B. in the case of shaping using of high mold pressure, does not take place. The advantage of the present Accordingly, the invention comes in particular in the manufacture of fillers Plastics in which the shaping using casting processes with or without foaming, to wear.  

Der Austausch der Luft in der Feststoffschüttung kann auf beliebige Weise erfolgen. Z.B. kann am Boden des Feststoffsilos Kohlendioxid eingeleitet werden. Eine andere Möglichkeit ist, das Förderorgan, z. B. eine Schnecke, mit dem der Feststoff in den Dispergierbehälter geführt wird, mit Kohlendioxid zu spülen.The exchange of air in the solid bed can be done in any way respectively. E.g. can be introduced at the bottom of the solid silo carbon dioxide. Another possibility is to use the funding body, e.g. B. a snail with which the Solid is led into the dispersion tank to rinse with carbon dioxide.

Unter Einsatz des erfindungsgemäßen Dispergierverfahrens bei der Herstellung füllstoffhaltiger Weichschaumstoffe konnte die im Schaumstoff unregelmäßig auf­ tretende Rißbildung wirksam verhindert werden. Offenbar war die vorher beobach­ tete Rißbildung darauf zurückzuführen, daß die Füllstoffteilchen nach der Disper­ gierung aufgrund noch anhaftender Luft durch die Polyurethanmasse nur unzurei­ chend benetzt wurden.Using the dispersion method according to the invention in the manufacture Filler-containing soft foams could be irregular in the foam occurring cracking can be effectively prevented. Apparently that was previously observable teten due to the fact that the filler particles after the Disper due to air still adhering due to the polyurethane mass were wetted accordingly.

Claims (3)

1. Verfahren zum Dispergieren von feinteiligen Feststoffen in einer Flüssig­ keit, dadurch gekennzeichnet, daß die zwischen den feinteiligen Feststoff­ teilchen vorhandene Luft vor der Dispergierung zumindest teilweise durch Kohlendioxid verdrängt wird.1. A method for dispersing finely divided solids in a liquid speed, characterized in that the air present between the finely divided solid particles is at least partially displaced by carbon dioxide before the dispersion. 2. Verfahren zur Herstellung von durch feinteilige Feststoffe verstärkten Kunststoffen durch Dispergieren der Feststoffe in flüssigen Kunststoff- Vorläuferprodukten, dadurch gekennzeichnet, daß die zwischen den Feststoffteilchen enthaltene Luft vor der Dispergierung zumindest teilweise durch Kohlendioxid verdrängt wird.2. Process for the production of reinforced by finely divided solids Plastics by dispersing the solids in liquid plastic Precursor products, characterized in that the between the Air contains solid particles at least partially before dispersion is displaced by carbon dioxide. 3. Verfahren zur Herstellung von durch feinteilige Feststoffe modifizierten Polyurethan-Weichschaumstoffen durch Dispergieren der feinteiligen Fest­ stoffe in mindestens einer der Komponenten der Polyurethan-Reaktiv­ mischung, dadurch gekennzeichnet, daß die zwischen den Feststoffteilchen vorhandene Luft vor der Dispergierung zumindest teilweise durch Kohlen­ dioxid verdrängt wird.3. Process for the production of modified by finely divided solids Flexible polyurethane foams by dispersing the finely divided solid substances in at least one of the components of the polyurethane reactive mixture, characterized in that between the solid particles Air present at least partially through coal before dispersion dioxide is displaced.
DE19515691A 1995-04-28 1995-04-28 Dispersion of finely-divided solids in liquid Ceased DE19515691A1 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
DE19515691A DE19515691A1 (en) 1995-04-28 1995-04-28 Dispersion of finely-divided solids in liquid
JP8122790A JPH08302027A (en) 1995-04-28 1996-04-22 Method of dispersing finely divided solid particle in fluid
CA002174893A CA2174893A1 (en) 1995-04-28 1996-04-24 Process for dispersing finely divided solids in a liquid
KR1019960013135A KR960037106A (en) 1995-04-28 1996-04-26 Method of dispersion of fine solids in liquid
NO961679A NO961679D0 (en) 1995-04-28 1996-04-26 Process for dispersing finely divided solids in a liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19515691A DE19515691A1 (en) 1995-04-28 1995-04-28 Dispersion of finely-divided solids in liquid

Publications (1)

Publication Number Publication Date
DE19515691A1 true DE19515691A1 (en) 1996-10-31

Family

ID=7760623

Family Applications (1)

Application Number Title Priority Date Filing Date
DE19515691A Ceased DE19515691A1 (en) 1995-04-28 1995-04-28 Dispersion of finely-divided solids in liquid

Country Status (5)

Country Link
JP (1) JPH08302027A (en)
KR (1) KR960037106A (en)
CA (1) CA2174893A1 (en)
DE (1) DE19515691A1 (en)
NO (1) NO961679D0 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001046304A2 (en) * 1999-12-23 2001-06-28 Mobius Technologies, Inc. Polymeric foam processing

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1905874A1 (en) * 1968-02-08 1969-09-11 Union Carbide Corp Method and device for mixing fibrous materials into air-free dispersions

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1905874A1 (en) * 1968-02-08 1969-09-11 Union Carbide Corp Method and device for mixing fibrous materials into air-free dispersions

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
DE-Sch 9847 IVC/12e *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001046304A2 (en) * 1999-12-23 2001-06-28 Mobius Technologies, Inc. Polymeric foam processing
WO2001046304A3 (en) * 1999-12-23 2002-03-07 Mobius Technologies Inc Polymeric foam processing
US6670404B2 (en) 1999-12-23 2003-12-30 Mobius Technologies, Inc. Polymeric foam powder processing techniques, foam powders products, and foams produced containing those foam powders

Also Published As

Publication number Publication date
CA2174893A1 (en) 1996-10-29
JPH08302027A (en) 1996-11-19
NO961679D0 (en) 1996-04-26
KR960037106A (en) 1996-11-19

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