US2666685A - Mold release emulsion - Google Patents
Mold release emulsion Download PDFInfo
- Publication number
- US2666685A US2666685A US238574A US23857451A US2666685A US 2666685 A US2666685 A US 2666685A US 238574 A US238574 A US 238574A US 23857451 A US23857451 A US 23857451A US 2666685 A US2666685 A US 2666685A
- Authority
- US
- United States
- Prior art keywords
- per cent
- weight
- carbon atoms
- mold release
- fatty acids
- 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.)
- Expired - Lifetime
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22C—FOUNDRY MOULDING
- B22C3/00—Selection of compositions for coating the surfaces of moulds, cores, or patterns
-
- 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
- C08K13/00—Use of mixtures of ingredients not covered by one single of the preceding main groups, each of these compounds being essential
- C08K13/02—Organic and inorganic ingredients
Definitions
- mold build-up indicates the failure of the release agent to entirely separate all of the molding from the pattern.
- the amount of mold material left on the pattern on any single release is, of course, very small.
- This invention concerns a mold release emulsion composed of 1 to 75 per cent by weight of organopolysiloxane fluids, 1 to 6 per cent by weight emulsifying agents, 2 to per cent by 7 LMichs assigngrs to lj 'ow'ffli irnm n Midland, Mich; "a; orneratidii'df "eels-gases reassess P esses empiqastasm -aiiej d. t m alma ter. metal.
- the org'anopolysiloxane fluids suitable for use inc-+3832) co" blymers thereof are "sealants thi tiQn Inaddition; thesiloxanesmay co ited amounts of m onoorganpsiloxane un which we "ergaiis' rsaica-l etliy j, phenyl.
- the defined siloxan'es may" ha e" y vi osity but preferably they haveviscositi's in essa es? .199 team e ntistq sesl qase hias. latpmac 529 mm a 11 6 ...ium fili -S.
- the emulsifying agent vention are commercially available materialsand ay he. oicither th cationier anionieprsnonioric We--. males qis elsma erials w ch. ,lr lo erative are morpholinesalts of fatty; ci wher in t fatt c contains ro is amine acetate, n-octadecen'yl y p0 ye er y 7 kali metal salts of alkylated arylpolyether sul-" fates.
- a commercial sodium salt of an alkylated arylpolyether sulfate is available under the tradename of Triton '7 71.
- the organosiloxane fluid and part of the emulsifying agent are mixed in an agitator. Separately, "water and the balance of emulsifying agent are also mixed together by suitable means.
- the water phase is then added to the siloxane phase, stirred and passed through a colloid mill, homogenizer or the like. This dispersion is finally added to silica well wet with water and again passed through suitable dispersing means.
- This mold release composition in its emulsion form may be applied in manners well known to the art such as by brush or spray.
- Example 1 A mold release emulsion was prepared in the following manner: 1.25 pounds of oleic acid and 17.75 pounds of dimethylsiloxane fiuid were mixed in an agitator. In a separate container 0.25 pound of a sodium alkylated arylpolyether sulfate and 0.875 pound of morpholine were dissolved in pounds of water. This water solution was then added to the siloxane-oleic acid and agitation continued until homogeneity was obtained. The resulting mixture, which may be called the thick phase, was passed through a colloid mill. Separately, 2.25 pounds of an aerogel, commercially known as Santocel C, was thoroughly wet down with 23.125 pounds of water.
- an aerogel commercially known as Santocel C
- the thick phase containing the polysiloxane was added to the wet-down Santocel and suitably mixed and then dispersed by means of a colloid mill.
- the foregoing process resulted in an emulsion having the following composition in percentages by weight:
- Example 2 Compositions corresponding to that of Example 1 were prepared using the following commercial silicas:
- Example 3 Mold release emulsions were prepared in the proportions and manner of Example 1 using the following polysiloxane fluids:
- a mold release emulsion consisting essentially of (1) from 1 to per cent by weight of organosiloxane fluids, said organosiloxanes having from 1.9 to 3 hydrocarbon radicals selected from the group consisting of methyl, ethyl and phenyl radicals, per silicon atom, (2) from 2 to 20 per cent by weight finely divided silica, (3) from 1 to 6 per cent by weight emulsifying agents selected from the group consisting of morpholine salts of fatty acids having from 12 to 18 carbon atoms in the acid chain, acetates of n-primary amines having from 12 to 18 carbon atoms in the amine chain, monoesters of polyethylene glycols and fatty acids having 12 to 18 carbon atoms in the acid chain, alkylated aryl polyether alcohols and alkali metal salts of alkylated aryl polyether sulfates and (4) from 20 to per cent by weight water.
Description
fatented jan- No Drawing. Amiucatfiiuiy Serial No. 238374 .il f ilt zf suitable use. injhe Croning process for .sand
Fea ts. s .Q s n. and san p 'bm ex tlr e el pe S; fiultahleresins r s z m, cure and eject the comple ed sliell molds has made the sand casting process available 'for mass production of metal parts. {is a result,- this process has become 'siohs sweeterteeteh aseasnetresp ss cleaning becomes necessary. Thus; the mowing":
machine is closed down from time to time to clean the master pattern. This entails a loss to production and an increase to unit cost. Actually, mold build-up indicates the failure of the release agent to entirely separate all of the molding from the pattern. The amount of mold material left on the pattern on any single release is, of course, very small.
It is the object of this invention to largely eliminate the above mentioned mold build-up and thereby to effect greater efficiencies and lower production costs.
' This invention concerns a mold release emulsion composed of 1 to 75 per cent by weight of organopolysiloxane fluids, 1 to 6 per cent by weight emulsifying agents, 2 to per cent by 7 LMichs assigngrs to lj 'ow'ffli irnm n Midland, Mich; "a; orneratidii'df "eels-gases reassess P esses empiqastasm -aiiej d. t m alma ter. metal.
pattern lresults ultimately in altering the dimen weight finely divided silica and 20 to 90 per cent water.
The org'anopolysiloxane fluids suitable for use inc-+3832) co" blymers thereof are "sealants thi tiQn Inaddition; thesiloxanesmay co ited amounts of m onoorganpsiloxane un which we "ergaiis' rsaica-l etliy j, phenyl. The defined siloxan'es may" ha e" y vi osity but preferably they haveviscositi's in essa es? .199 team e ntistq sesl qase hias. latpmac 529 mm a 11 6 ...ium fili -S.
The emulsifying agent vention are commercially available materialsand ay he. oicither th cationier anionieprsnonioric We--. males qis elsma erials w ch. ,lr lo erative are morpholinesalts of fatty; ci wher in t fatt c contains ro is amine acetate, n-octadecen'yl y p0 ye er y 7 kali metal salts of alkylated arylpolyether sul-" fates. A commercial sodium salt of an alkylated arylpolyether sulfate is available under the tradename of Triton '7 71.
The order in which the various ingredients of applicants composition may be added can be varied. The preferred method of preparation, however, is as follows:
The organosiloxane fluid and part of the emulsifying agent are mixed in an agitator. Separately, "water and the balance of emulsifying agent are also mixed together by suitable means. The water phase is then added to the siloxane phase, stirred and passed through a colloid mill, homogenizer or the like. This dispersion is finally added to silica well wet with water and again passed through suitable dispersing means. This mold release composition in its emulsion form may be applied in manners well known to the art such as by brush or spray.
The following examples show how this invention may be practiced. These examples are illustrative only and the invention is in no way limited by them.
Example 1 A mold release emulsion was prepared in the following manner: 1.25 pounds of oleic acid and 17.75 pounds of dimethylsiloxane fiuid were mixed in an agitator. In a separate container 0.25 pound of a sodium alkylated arylpolyether sulfate and 0.875 pound of morpholine were dissolved in pounds of water. This water solution was then added to the siloxane-oleic acid and agitation continued until homogeneity was obtained. The resulting mixture, which may be called the thick phase, was passed through a colloid mill. Separately, 2.25 pounds of an aerogel, commercially known as Santocel C, was thoroughly wet down with 23.125 pounds of water. The thick phase containing the polysiloxane was added to the wet-down Santocel and suitably mixed and then dispersed by means of a colloid mill. The foregoing process resulted in an emulsion having the following composition in percentages by weight:
Per cent Dimethylsiloxane fluid 35 Santocel C (Silica aerogel) 4 /2 Qleic' acid 2 Morpholine Sodium salt of alkylated arylpolyether sulfate (Triton 771) Water 56%,
Example 2 Compositions corresponding to that of Example 1 were prepared using the following commercial silicas:
LudoxColloidal silica,
water HiSil-Precipitated silica gel Superflos-Diatomaceous earth DegussaFumed silica dispersed (30%) in All of these compositions gave excellent release when used in the Croning or shell molding process, and they gave no indication of mold build- 4 Example 3 Mold release emulsions were prepared in the proportions and manner of Example 1 using the following polysiloxane fluids:
Diethyl siloxane Phenylmethyl siloxane Ethylmethyl siloxane All emulsions prepared gave excellent release and were free of mold build-up when tested in the Croning process.
That which is claimed is:
1. A mold release emulsion consisting essentially of (1) from 1 to per cent by weight of organosiloxane fluids, said organosiloxanes having from 1.9 to 3 hydrocarbon radicals selected from the group consisting of methyl, ethyl and phenyl radicals, per silicon atom, (2) from 2 to 20 per cent by weight finely divided silica, (3) from 1 to 6 per cent by weight emulsifying agents selected from the group consisting of morpholine salts of fatty acids having from 12 to 18 carbon atoms in the acid chain, acetates of n-primary amines having from 12 to 18 carbon atoms in the amine chain, monoesters of polyethylene glycols and fatty acids having 12 to 18 carbon atoms in the acid chain, alkylated aryl polyether alcohols and alkali metal salts of alkylated aryl polyether sulfates and (4) from 20 to per cent by weight water.
2. A mold release emulsion as in claim 1 wherein the organosiloxane fluid is dimethylsiloxane.
MAURICE C. HOMMEL. CHESTER C. CURRIE.
References Cited in the file of this patent UNITED STATES PATENTS Number Name Date 2,462,242 Webb et al. Feb. 22, 1949 2,523,281 Currie Sept. 26, 1950 2,529,835 Dailey et al. Nov. 14, 1950 2,549,535 Skooglund Apr. 17, 1951 2,573,337 Hyde Oct. 20, 1951 OTHER REFERENCES The Foundry, August 1950, pages 106, 107 and 212.
Dow Corning Silicone Mold Release Agents, pages 6 and '7.
Claims (1)
1. A MOLD RELEASE EMULSION CONSISTING ESSENTIALLY OF (1) FROM 1 TO 75 PER CENT BY WEIGHT OF ORGANOSILOXANE FLUIDS, SAID ORGANOSILOXANES HAVING FROM 1.9 TO 3 HYDROCARBON RADICALS SELECTED FROM THE GROUP CONSISTING OF METHYL, (2) FROM 2 TO PHENY RADICALS, PER SILICON ATOM, (2) FROM 2 TO 20 PER CENT BY WEIGHT FINELY DIVIDED SILICA, (3) FROM 1 TO 6 PER CENT BY WEIGHT EMULSIFYING AGENTS SELECTED FROM THE GROUP CONSISTING OF MORPHOLINE SALTS OF FATTY ACIDS HAVING FROM 12 TO 18 CARBON ATOMS IN THE ACID CHAIN ACETATES OF N-PRIMARY AMINES HAVING FROM 12 TO 18 CARBON ATOMS IN THE AMINE CHAIN, MONOESTERS OF POLYETHYLENE GLYCOLS AND FATTY ACIDS HAVING 12 TO 18 CARBON ATOMS IN THE ACID CHAIN, ALKYLATED ARYL POLYETHER ALCOHOLS AND ALKALI METAL SALTS OF ALKYLATED ARYL POLYETHER SULFATES AND (4) FROM 20 TO 90 PER CENT BY WEIGHT WATER.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US238574A US2666685A (en) | 1951-07-25 | 1951-07-25 | Mold release emulsion |
GB12370/52A GB710033A (en) | 1951-07-25 | 1952-05-15 | Improvements in or relating to organopolysiloxane mould release agents |
FR1065356D FR1065356A (en) | 1951-07-25 | 1952-07-09 | Improvement in emulsions facilitating mold release |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US238574A US2666685A (en) | 1951-07-25 | 1951-07-25 | Mold release emulsion |
Publications (1)
Publication Number | Publication Date |
---|---|
US2666685A true US2666685A (en) | 1954-01-19 |
Family
ID=22898499
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US238574A Expired - Lifetime US2666685A (en) | 1951-07-25 | 1951-07-25 | Mold release emulsion |
Country Status (3)
Country | Link |
---|---|
US (1) | US2666685A (en) |
FR (1) | FR1065356A (en) |
GB (1) | GB710033A (en) |
Cited By (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2742368A (en) * | 1951-08-02 | 1956-04-17 | Dow Corning | Stabilized and rust inhibited polymeric organosilicon compositions |
US2755194A (en) * | 1955-02-07 | 1956-07-17 | Dow Corning | Organosiloxane emulsions |
US2757094A (en) * | 1953-08-07 | 1956-07-31 | Guss Charles | Liquid cleaner and polisher and method of compounding the same |
US2827387A (en) * | 1953-02-25 | 1958-03-18 | Socony Mobil Oil Co Inc | Stabilized paraffin wax |
US2833658A (en) * | 1958-05-06 | Organosilicon release agents | ||
US2870043A (en) * | 1954-06-03 | 1959-01-20 | Du Pont | Printable polyethylene film |
US2881146A (en) * | 1956-07-10 | 1959-04-07 | Du Pont | Organopolysiloxane emulsion containing polymerization catalyst and colloidal silica |
US2891920A (en) * | 1955-01-26 | 1959-06-23 | Dow Corning | Polymerization of organopolysiloxanes in aqueous emulsion |
US2943068A (en) * | 1957-08-23 | 1960-06-28 | Monsanto Chemicals | Shell molding compositions |
US2965589A (en) * | 1956-10-26 | 1960-12-20 | Dow Chemical Co | Aqueous dispersions of zinc stearate and polyethylene glycol monoesters |
US3077460A (en) * | 1955-08-17 | 1963-02-12 | Celanese Corp | Composition comprising an organopolysiloxane and colloidal silica, and textile treated therewith |
US3220070A (en) * | 1959-11-23 | 1965-11-30 | Gen Electric | Method of casting molten metal in coated ingot mold |
US3235923A (en) * | 1963-11-19 | 1966-02-22 | Harbison Walker Refractories | Method of forming refractory mold shapes |
US3313648A (en) * | 1965-04-05 | 1967-04-11 | Boeing Co | Treatment of glass glazing vulnerable to impact by insects |
US3416934A (en) * | 1964-07-02 | 1968-12-17 | Abrasive Dev | Treatment of mould surfaces |
US3941864A (en) * | 1973-06-04 | 1976-03-02 | Wacker-Chemie Gmbh | Method for manufacturing molded structures and coatings based on inorganic binding agents |
US4191578A (en) * | 1977-11-02 | 1980-03-04 | Gene Conreaux & Co., Inc. | Release agents |
EP0044143A1 (en) * | 1980-07-11 | 1982-01-20 | The Mead Corporation | Low friction plastics track and extrusion process |
US4525502A (en) * | 1983-05-05 | 1985-06-25 | General Electric Company | Water based resin emulsions |
US4532096A (en) * | 1983-05-09 | 1985-07-30 | Bogner Ben R | Method of shaping articles using shaping surfaces having release agent coating |
USRE32318E (en) * | 1980-11-20 | 1986-12-30 | The Goodyear Tire & Rubber Company | Tire curing bladder lubricant |
USRE34584E (en) * | 1984-11-09 | 1994-04-12 | The Procter & Gamble Company | Shampoo compositions |
DE102008015966A1 (en) * | 2008-03-20 | 2009-09-24 | Itn Nanovation Ag | Casting mold production from mixture of granular refractory and binder, by shaping in model at least partially coated with organosilicon composition as separating agent |
US20100225026A1 (en) * | 2006-09-15 | 2010-09-09 | Sika Technology Ag | Mould release composition |
US20110036528A1 (en) * | 2007-12-21 | 2011-02-17 | Itn Nanovation Ag | Production of moldings for foundry purposes |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB8718546D0 (en) * | 1987-08-05 | 1987-09-09 | Austin Rover Group | Moulded article |
CN101837428B (en) * | 2010-05-14 | 2012-07-25 | 福建省闽华电源股份有限公司 | Coating agent for casting lead acid battery slab lattices |
CN102873265B (en) * | 2012-09-10 | 2015-05-13 | 超威电源有限公司 | Release agent used for pouring lead-acid storage battery grid and preparation method of release agent |
DE102016223619A1 (en) * | 2015-12-15 | 2017-06-22 | Robert Bosch Gmbh | Sizing for application to the porous surface of molds and / or cores for metal casting |
CN105921689A (en) * | 2016-06-13 | 2016-09-07 | 岳良珍 | Demolding agent for lead-acid storage battery grid pouring mold cavity and preparation method thereof |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2462242A (en) * | 1948-04-06 | 1949-02-22 | Paul S Webb | Silicone surfaced cooking implement |
US2523281A (en) * | 1950-09-26 | automobile polish | ||
US2529835A (en) * | 1947-01-18 | 1950-11-14 | United States Gypsum Co | Metal-casting molds and processes and materials for producing the same |
US2549535A (en) * | 1949-02-11 | 1951-04-17 | Standard Oil Dev Co | Glass molding lubricant |
US2573337A (en) * | 1948-02-16 | 1951-10-30 | Corning Glass Works | Coated metal mold for blowing glass and method of preparing the same |
-
1951
- 1951-07-25 US US238574A patent/US2666685A/en not_active Expired - Lifetime
-
1952
- 1952-05-15 GB GB12370/52A patent/GB710033A/en not_active Expired
- 1952-07-09 FR FR1065356D patent/FR1065356A/en not_active Expired
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2523281A (en) * | 1950-09-26 | automobile polish | ||
US2529835A (en) * | 1947-01-18 | 1950-11-14 | United States Gypsum Co | Metal-casting molds and processes and materials for producing the same |
US2573337A (en) * | 1948-02-16 | 1951-10-30 | Corning Glass Works | Coated metal mold for blowing glass and method of preparing the same |
US2462242A (en) * | 1948-04-06 | 1949-02-22 | Paul S Webb | Silicone surfaced cooking implement |
US2549535A (en) * | 1949-02-11 | 1951-04-17 | Standard Oil Dev Co | Glass molding lubricant |
Cited By (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2833658A (en) * | 1958-05-06 | Organosilicon release agents | ||
US2742368A (en) * | 1951-08-02 | 1956-04-17 | Dow Corning | Stabilized and rust inhibited polymeric organosilicon compositions |
US2827387A (en) * | 1953-02-25 | 1958-03-18 | Socony Mobil Oil Co Inc | Stabilized paraffin wax |
US2757094A (en) * | 1953-08-07 | 1956-07-31 | Guss Charles | Liquid cleaner and polisher and method of compounding the same |
US2870043A (en) * | 1954-06-03 | 1959-01-20 | Du Pont | Printable polyethylene film |
US2891920A (en) * | 1955-01-26 | 1959-06-23 | Dow Corning | Polymerization of organopolysiloxanes in aqueous emulsion |
US2755194A (en) * | 1955-02-07 | 1956-07-17 | Dow Corning | Organosiloxane emulsions |
US3077460A (en) * | 1955-08-17 | 1963-02-12 | Celanese Corp | Composition comprising an organopolysiloxane and colloidal silica, and textile treated therewith |
US2881146A (en) * | 1956-07-10 | 1959-04-07 | Du Pont | Organopolysiloxane emulsion containing polymerization catalyst and colloidal silica |
US2965589A (en) * | 1956-10-26 | 1960-12-20 | Dow Chemical Co | Aqueous dispersions of zinc stearate and polyethylene glycol monoesters |
US2943068A (en) * | 1957-08-23 | 1960-06-28 | Monsanto Chemicals | Shell molding compositions |
US3220070A (en) * | 1959-11-23 | 1965-11-30 | Gen Electric | Method of casting molten metal in coated ingot mold |
US3235923A (en) * | 1963-11-19 | 1966-02-22 | Harbison Walker Refractories | Method of forming refractory mold shapes |
US3416934A (en) * | 1964-07-02 | 1968-12-17 | Abrasive Dev | Treatment of mould surfaces |
US3313648A (en) * | 1965-04-05 | 1967-04-11 | Boeing Co | Treatment of glass glazing vulnerable to impact by insects |
US3941864A (en) * | 1973-06-04 | 1976-03-02 | Wacker-Chemie Gmbh | Method for manufacturing molded structures and coatings based on inorganic binding agents |
US4191578A (en) * | 1977-11-02 | 1980-03-04 | Gene Conreaux & Co., Inc. | Release agents |
EP0044143A1 (en) * | 1980-07-11 | 1982-01-20 | The Mead Corporation | Low friction plastics track and extrusion process |
USRE32318E (en) * | 1980-11-20 | 1986-12-30 | The Goodyear Tire & Rubber Company | Tire curing bladder lubricant |
US4525502A (en) * | 1983-05-05 | 1985-06-25 | General Electric Company | Water based resin emulsions |
US4532096A (en) * | 1983-05-09 | 1985-07-30 | Bogner Ben R | Method of shaping articles using shaping surfaces having release agent coating |
USRE34584E (en) * | 1984-11-09 | 1994-04-12 | The Procter & Gamble Company | Shampoo compositions |
US20100225026A1 (en) * | 2006-09-15 | 2010-09-09 | Sika Technology Ag | Mould release composition |
US20110036528A1 (en) * | 2007-12-21 | 2011-02-17 | Itn Nanovation Ag | Production of moldings for foundry purposes |
DE102008015966A1 (en) * | 2008-03-20 | 2009-09-24 | Itn Nanovation Ag | Casting mold production from mixture of granular refractory and binder, by shaping in model at least partially coated with organosilicon composition as separating agent |
Also Published As
Publication number | Publication date |
---|---|
FR1065356A (en) | 1954-05-24 |
GB710033A (en) | 1954-06-02 |
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