DE1794380B2 - Use of chrysotile asbestos as a thixotropic thickener excretion from 1619771 - Google Patents
Use of chrysotile asbestos as a thixotropic thickener excretion from 1619771Info
- Publication number
- DE1794380B2 DE1794380B2 DE1794380A DE1794380A DE1794380B2 DE 1794380 B2 DE1794380 B2 DE 1794380B2 DE 1794380 A DE1794380 A DE 1794380A DE 1794380 A DE1794380 A DE 1794380A DE 1794380 B2 DE1794380 B2 DE 1794380B2
- Authority
- DE
- Germany
- Prior art keywords
- asbestos
- chrysotile
- chrysotile asbestos
- rpm
- excretion
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K7/00—Use of ingredients characterised by shape
- C08K7/02—Fibres or whiskers
- C08K7/04—Fibres or whiskers inorganic
- C08K7/14—Glass
-
- 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
- B01J19/06—Solidifying liquids
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/34—Silicon-containing compounds
- C08K3/36—Silica
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K7/00—Use of ingredients characterised by shape
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K7/00—Use of ingredients characterised by shape
- C08K7/02—Fibres or whiskers
- C08K7/04—Fibres or whiskers inorganic
- C08K7/10—Silicon-containing compounds
- C08K7/12—Asbestos
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D7/00—Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
- C09D7/40—Additives
- C09D7/43—Thickening agents
- C09D7/44—Combinations of two or more thickening agents
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M113/00—Lubricating compositions characterised by the thickening agent being an inorganic material
- C10M113/12—Silica
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2201/00—Inorganic compounds or elements as ingredients in lubricant compositions
- C10M2201/10—Compounds containing silicon
- C10M2201/102—Silicates
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2201/00—Inorganic compounds or elements as ingredients in lubricant compositions
- C10M2201/10—Compounds containing silicon
- C10M2201/105—Silica
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2290/00—Mixtures of base materials or thickeners or additives
- C10M2290/10—Thickener
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/02—Bearings
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2050/00—Form in which the lubricant is applied to the material being lubricated
- C10N2050/015—Dispersions of solid lubricants
- C10N2050/02—Dispersions of solid lubricants dissolved or suspended in a carrier which subsequently evaporates to leave a lubricant coating
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2050/00—Form in which the lubricant is applied to the material being lubricated
- C10N2050/10—Semi-solids; greasy
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Polymers & Plastics (AREA)
- Medicinal Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Wood Science & Technology (AREA)
- Detergent Compositions (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Lubricants (AREA)
- Processing Of Solid Wastes (AREA)
Description
Zur näheren Erläuterung der Erfindung sollen die nachfolgenden Beispiele dienen.The following examples are intended to provide a more detailed explanation of the invention.
Beispiel 1
15 example 1
15th
Herstellung vonProduction of
Die Verwendung von Asbest als Verdickungsmittel strahlvermahlenem ChrysotilastcstThe use of asbestos as a thickening agent in jet-milled chrysotile paste
zur Herstellung von Schmierfetten aus Schmierölenfor the production of lubricating greases from lubricating oils
ist an sich bereits bekannt, beispielsweise aus der In eine handelsübliche Strahlmühle mit einemis already known per se, for example from the In a commercially available jet mill with a
USA.-Patentschrift 3 010 896 sowie aus einem Aufsatz 20 Mahlkammerdurchmesser von 20,3 cm wurden durch von C. J. B ο η e r, »Manufacture and Application einen Venturiinjektor (mit Druckluft von 10,5 bis of Lubricating Greases«. 17,5 kg/cm2) Chrysotilasbestteilchen mit einer Ge-USA.-Patent 3 010 896 and from an attachment 20 grinding chamber diameters of 20.3 cm were made by CJ B o η er, "Manufacture and Application, a Venturi injector (with compressed air from 10.5 to of lubricating greases". 17.5 kg / cm 2 ) chrysotile asbestos particles with a
Es wurde nunmehr gefunden, daß ein erheblich schwindigkeit von etwa 25 g/min eingeführt. In den in verbessertes Verdickungsmittel für Flüssigkeiten, bei- der Strahlmühle gebildeten Wirbelkörper aus Asbestspielsweise zur Herstellung von thixotropen Schmier- 25 teilchen wurde zur Erzeugung einer turbulenten fetten oder thixotropen Anstrichfarben bzw. ahn- Masse Luft von Raumtemperatur mit einem Druck liehen Zusammensetzungen, erhalten wird, wenn man von etwa 21 kg/cm2 eingeblasen. Die feinteiligen Chrysotilasbest einer Vermahlung in einer Strahl- Asbestfasern wurden in einem Sackfänger von dem mühle unterwirft. Nach der Behandlung in der Strahl- Luftstrom abgetrennt.It has now been found that a substantial rate of about 25 g / min was introduced. In the improved thickener for liquids, in the case of the jet mill, the vortex body made of asbestos for the production of thixotropic lubricating particles was obtained for the production of a turbulent, fat or thixotropic paint or a mass of air at room temperature with a pressure, is obtained, when blown in by about 21 kg / cm 2. The finely divided chrysotile asbestos was ground in a jet asbestos fibers in a bag catcher from the mill. After treatment in the jet air stream separated.
mühle liegt der Asbest in Form von feinen Fasern vor, 30 Einzelheiten über Art und Menge der Ausgangsderec Durchmesser im kolloidalen Bereich liegt. materialien sind in den nachfolgenden Tabellen 1 und 2mill, the asbestos is in the form of fine fibers Diameter is in the colloidal range. materials are shown in Tables 1 and 2 below
Die Chrysotilasbest-Fasern lassen sich dadurch her- angegeben.The chrysotile asbestos fibers can thereby be specified.
stellen, daß man unter Überdruck und bei einer Tem- Die Teilchengröße des Ausgangsmaterials ist nurput that one under positive pressure and at a tem- The particle size of the starting material is only
peratur zwischen Raumtemperatur und 650° C einen insofern begrenzt, als das Material sich in den Venturibewegten
Körper aus in einem gasförmigen Medium 35 injektor einführen lassen muß. Zu große Asbestteilsuspendierten
Asbestteilchen herstellt und in diesen chen können zur Verringerung der Faserlänge auf den
kontinuierlich weiteres gasförmiges Medium in meh- erforderlichen Bereich einer Vorbehandlung unterreren
Strömen mit einer Temperatur in dem genannten worfen werden.
Bereich und hoher Geschwindigkeit unter ErzeugungTemperature between room temperature and 650 ° C is limited to the extent that the material must be able to be introduced into the Venturi moving body from an injector in a gaseous medium. Excessively large asbestos-suspended asbestos particles are produced and in this area, further gaseous medium can be thrown into the continuously further gaseous medium in a number of required areas to reduce the fiber length, with a temperature in the above mentioned range.
Area and high speed under generation
starker Turbulenz in dem Körper und damit unter 40 B e i s ρ i e 1 2strong turbulence in the body and thus less than 40 B e i s ρ i e 1 2
Zerkleinerung der suspendierten Teilchen einführt, die ,, ,■ , ^ ,Comminution of the suspended particles introduces the ,,, ■, ^,
zerkleinerten Asbestteilchen zusammen mit dem gas- Verd.ckung von Polyesterncrushed asbestos particles together with the gas thickening of polyesters
förmigen Medium kontinuierlich abzieht und die feinen Als Harz wurde ein flüssiges Polyesterharz mitshaped medium continuously withdraws and the fine resin was made using a liquid polyester resin
Asbestteilchen von dem Suspendierungsgas abtrennt. einer Viskosität von 150 bis 20OcP bei 250C (ge-AIs Suspendierungsmedium werden Luft und Dampf 45 messen im Brookfield-Viskosimeter mit einer Spindel bevorzugt. Nr. 2 bei 20 U/min) und einem auf 41 % eingestelltenSeparating asbestos particles from the suspending gas. a viscosity of 150 to 20OcP at 25 0 C (ge-AIs suspension medium, air and steam are preferably measured in a Brookfield viscometer with a spindle. No. 2 at 20 rpm) and one set to 41 %
Zum Zerkleinern der Asbestteilchen eignen sich Styrolgehalt verwendet. Als Verdickungsmittel wurden Strahlmühlen bekannter Art. Bevorzugt wird eine die nach Beispiel 1 hergestellten Chrysotilasbest-Fasern Strahlmühle, in welcher verhältnismäßig große Teil- eingesetzt. Der Polyester wurde mit dem Verdickungschen in einem Gasmedium suspendiert und um eine 50 mittel vermischt und die Viskositätserhöhung bei innen angeordnete Basis gewirbelt werden und 6 U/min und 60 U/min wurde im Brookfield-Viskosiin den Wirbelkörper weiteres Gas unter Erzeugung meter gemessen. Die Viskosität des verdickten Harzes von Turbulenz in dem Körper und unter Zerkleine- wurde dabei sofort und nach 7 Tagen Lagerung bei rung und Zerreibung der Teilchen eingeführt wird. 38°C bestimmt. Das Absetzvermögen der verdicktenStyrene contents are suitable for crushing the asbestos particles. Used as a thickener Jet mills of known type. One of the chrysotile asbestos fibers produced according to Example 1 is preferred Jet mill, in which relatively large part used. The polyester was made with the thickening suspended in a gas medium and mixed by a 50 medium and the viscosity increase at internally arranged base to be vortexed and 6 rpm and 60 rpm was in Brookfield viscose the vertebral body measured further gas under generation meter. The viscosity of the thickened resin of turbulence in the body and under crushing was done immediately and after 7 days of storage at tion and attrition of the particles is introduced. 38 ° C determined. The settling power of the thickened
Die Strahlmühle wird bei der Verwendung von 55 Polyesterharze wurde durch Messen der überstehenden
Luft als gasförmigem Mahlmedium zweckmäßig mit Flüssigkeit ermittelt,
einem Druck von etwa 7 bis 35 und vorzugsweise 7 bisThe jet mill is determined when using 55 polyester resins by measuring the excess air as a gaseous grinding medium with liquid,
a pressure of about 7 to 35, and preferably 7 to
21 kg/cm2 (über Atmosphärendruck) betrieben. Die B e i s ο i e 1 321 kg / cm 2 (above atmospheric pressure) operated. The bis ο ie 1 3
Turbulenz erzeugende zusätzliche Luft kann mit einemAdditional air that creates turbulence can be mixed with a
Druck von etwa 7 bis 35 kg/cm2, vorzugsweise etwa 60 Verdickung von PolyepoxidenPressure of about 7 to 35 kg / cm 2 , preferably about 60 thickening of polyepoxides
10,5 bis 17,5 kg/cm2, in den die Asbestteilchen enthaltenden Wirbelkörper eingeführt werden. Vorzugs- Als Harz wurde ein flüssiges Polyepoxid mit einer weise findet Luft von Raumtemperatur Verwendung. Viskosität von 400 bis 60OcP bei 25°C und mit Die durchschnittliche Teilchengröße kann durch Regu- einem Epoxidäquivalent von 175 bis 200 verwendet, lierung der Luftgeschwindigkeit und -temperatur so- 65 Die Verdickungswirkung der nach Beispiel 1 hergewie der Zuführgeschwindigkeit für den Asbest variiert stellten feinteiligen Chrysotilasbestfasern wurde wie werden. Das Produkt kann auf beliebige Weise von im Beispiel 2 bestimmt. Die Ergebnisse finden sich in dem Suspendierungsmedium abgetrennt werden; vor- der nachfolgenden Tabelle 2.10.5 to 17.5 kg / cm 2 , are introduced into the vertebral body containing the asbestos particles. The preferred resin is a liquid polyepoxide with room temperature air. Viscosity from 400 to 60 ocP at 25 ° C and with The average particle size can be used by regulating the air speed and temperature by regulating the air speed and temperature so that the asbestos feed rate varied according to Example 1 Chrysotile asbestos fiber was like to be. The product can be determined in any of the ways in Example 2. The results can be found in the suspending medium separated; in front of the following table 2.
I 794 380I 794 380
Chrysotil-AsbestKind of used
Chrysotile asbestos
100 Teile
PolyesterParts thickener each
100 parts
polyester
sofort gemessenViscosity in el
measured immediately
7 Tagenafter
7 days
überstehende Flüssigkeit
nach 7 TagenDeductibility,%
supernatant liquid
after 7 days
*) Teilweise durch Säurebehandlung entfasert.*) Partly defibrated by acid treatment.
Chrysotil-AsbestsKind of used
Chrysotile asbestos
je 100 Teile
PolyepoxidParts thickener
100 parts each
Polyepoxide
sofort gemessen
6 U/min | 60 U/minViscosity in cP
measured immediately
6 rpm | 60 rpm
bei 54°C
6 U/minafter 7 days
at 54 ° C
6 rpm
überstehende
Flüssigkeit
nach 7 TagenDeductibility,%
protruding
liquid
after 7 days
CoalingaCalifornian
Coalinga
Claims (1)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US56908766A | 1966-08-01 | 1966-08-01 |
Publications (3)
Publication Number | Publication Date |
---|---|
DE1794380A1 DE1794380A1 (en) | 1973-08-09 |
DE1794380B2 true DE1794380B2 (en) | 1973-12-20 |
DE1794380C3 DE1794380C3 (en) | 1974-07-18 |
Family
ID=24274054
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE1619771A Expired DE1619771C3 (en) | 1966-08-01 | 1967-07-29 | Use of a mixture of chrysotile asbestos and silicon dioxide to thicken liquids |
DE1794380A Expired DE1794380C3 (en) | 1966-08-01 | 1967-07-29 | Use of chrysotile asbestos as a thixotropic thickener. Eliminated from: 1619771 |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE1619771A Expired DE1619771C3 (en) | 1966-08-01 | 1967-07-29 | Use of a mixture of chrysotile asbestos and silicon dioxide to thicken liquids |
Country Status (3)
Country | Link |
---|---|
DE (2) | DE1619771C3 (en) |
GB (1) | GB1146926A (en) |
SE (1) | SE319117B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU6465580A (en) * | 1980-02-29 | 1981-09-03 | W.R. Grace & Co. | Silica/fibrous polyolefin thickening agents |
-
1967
- 1967-07-03 GB GB30595/67A patent/GB1146926A/en not_active Expired
- 1967-07-25 SE SE10843/67*A patent/SE319117B/xx unknown
- 1967-07-29 DE DE1619771A patent/DE1619771C3/en not_active Expired
- 1967-07-29 DE DE1794380A patent/DE1794380C3/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
DE1619771C3 (en) | 1974-04-04 |
SE319117B (en) | 1969-12-22 |
DE1794380A1 (en) | 1973-08-09 |
DE1794380C3 (en) | 1974-07-18 |
DE1619771A1 (en) | 1970-07-30 |
GB1146926A (en) | 1969-03-26 |
DE1619771B2 (en) | 1973-08-23 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C3 | Grant after two publication steps (3rd publication) | ||
E77 | Valid patent as to the heymanns-index 1977 | ||
8339 | Ceased/non-payment of the annual fee |