WO1990000083A1 - Pastilles d'acides gras metalliques - Google Patents

Pastilles d'acides gras metalliques Download PDF

Info

Publication number
WO1990000083A1
WO1990000083A1 PCT/US1989/002767 US8902767W WO9000083A1 WO 1990000083 A1 WO1990000083 A1 WO 1990000083A1 US 8902767 W US8902767 W US 8902767W WO 9000083 A1 WO9000083 A1 WO 9000083A1
Authority
WO
WIPO (PCT)
Prior art keywords
powder
metallic salt
pellets
salt powder
weight
Prior art date
Application number
PCT/US1989/002767
Other languages
English (en)
Inventor
Neil Dunski
Original Assignee
Mallinckrodt, Inc.
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 Mallinckrodt, Inc. filed Critical Mallinckrodt, Inc.
Publication of WO1990000083A1 publication Critical patent/WO1990000083A1/fr

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
    • C08K5/00—Use of organic ingredients
    • C08K5/04—Oxygen-containing compounds
    • C08K5/09—Carboxylic acids; Metal salts thereof; Anhydrides thereof
    • C08K5/098—Metal salts of carboxylic acids
    • 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
    • C08K9/00—Use of pretreated ingredients
    • C08K9/08—Ingredients agglomerated by treatment with a binding agent

Definitions

  • the present invention relates to powder metallic salts of aliphatic monocarboxylic acids, for example, commercial stearic acid, and particularly to a modified powder form and method of manufacture.
  • Powder metallic salts of commercial stearic acid commonly known as metallic stearates, which generally consists of 50% to 75% by weight stearic acid (octodecanoic acid), 25% to 50% by weight palmitic acid (hexadecanoic acid), and small amounts, i.e. generally less than 2% by weight, other Cia-Caa aliphatic saturated and unsaturated monocarboxylic acids, are used as additives in a variety of consumer products.
  • aluminum stearate is used as a defoamer for oil well drilling muds, a thickening agent for crayons, a gelling agent for greases and oils, and a suspension agent in paints and inks.
  • Calcium stearate is used as a secondary stabilizer, mold release agent and lubricant in rigid PVC, a neutralizer of residual catalysts in polyethylene and polypropylene, and an anticaking agent in food applications.
  • Magnesium stearate is used as a mold release agent in powders and tablets for cosmetic and pharmaceutical applications, a dispersant and anticaking agent for fire extinguisher powder mixtures, and a lubricant and processing aid in acrylonitrile- butadiene-styrene (ABS) polymers.
  • Zinc stearate is used as a processing and lubricant aid for crystal and impact polystyrene, a dispersing agent in pigment blending, and a lubricant and mold release agent in polyethylene.
  • Lead stearate is used as a stabilizer for PVC.
  • a finely divided or small particle size such as an average particle size in the range from 2 to 200 microns, is needed for the proper blending and functioning of the metallic stearate. In other applications, an average particle size up to 100 mesh (0.2 mm) can be used.
  • Dry powder metallic stearates after manufacture, are transported and handled in bulk form, for exeunple, by tank car or truck or may be placed in bags which are then handled and transported to the user. At the user, the bulk metallic stearate, either from storage facilities or bags, is further handled and placed in hoppers to mixers and blenders. During this handling and transport, the fine powdery metallic stearate material is subject to producing dust which is hazardous.
  • powder metallic salts of aliphatic monocarboxylic acids can be pelletized to avoid the formation of dust during transport and handling when from 0.5.to 20% by weight liquid or pliable solid binder material is blended with the powder prior to passing the mixture through a pellet mill.
  • the pellets readily disintegrate to their powder form, and thus additional grinding equipment is not necessary to return the pellets to a powder form prior to use.
  • careful selection of the particular binding material avoids altering the properties of the end product or the effectiveness of the powder in its intended function.
  • An object of the invention is to eliminate explosion hazards produced in handling and transport of powder metallic salts of aliphatic monocarboxylic acids.
  • One advantage of the invention is that expensive dust handling facilities for preventing hazardous dust conditions of powder metallic salts of aliphatic monocarboxylic acids is eliminated.
  • One feature of the invention is that a variety of materials are suitable for assisting in the binding of the powdery metallic salts of aliphatic monocarboxylic acids so that a particular material may be selected based upon its being relatively inert and non-altering to the end use or consumer product.
  • the drawing is a flow diagram illustrating a process for manufacturing powder pellets of metallic salts of aliphatic monocarboxylic acids in accordance with the invention.
  • powder pellets of metallic salts of aliphatic monocarboxylic acids are produced in accordance with the invention by blending the dry powder and from 0.5 to 20% by weight binder material in a blender 10 and passing the blended material through a pellet mill 12 to form product powder pellets suitable for handling and transport with substantially reduced risk for generating hazardous dust conditions.
  • the dry powder metallic salt is any powder metallic salt of an aliphatic monocarboxylic acid which is used commercially, is handled and transported in bulk form, and tends to generate hazardous dust conditions during the handling and transport.
  • calcium, magnesium, aluminum, zinc and lead salts of aliphatic monocarboxylic acids having from 12 to 22 carbon atoms are such powders.
  • Examples are commercial metallic stearates including calcium, magnesium, aluminum, zinc, and lead stearates produced by conventional precipitation and fusion processes from commercial stearic acids which generally consist of 50% to 75% by weight stearic acid (octadecanoic acid), 25% to 50% by weight palmitic acid (hexadecanoic acid) , and small amounts, i.e.
  • the dry powder metallic salt is generally in the range from 80% to 99.5% by weight of the material being added to the blender 10.
  • the dry powder metallic salt is in the range from 90% to 99% by weight of the material in the powder pellets, and most preferably, in the range from 96% to 98% by weight of the material in the powder pellets.
  • powder metallic stearates generally contain relatively little residual unreacted fatty acid, i.e., less than 1%, so that the powder material cannot be pelletized at ordinary ambient temperature by mechanical pelletizing equipment. Pellets made from dry powder metallic stearates without the addition of the binder material have little strength and integrity, and will revert back to their dusty, powdery form under normal minimal forces exerted on the pellets during handling and transport.
  • the binder material is a liquid or pliable solid material which can be readily blended with the metallic stearate without altering the end use properties of the metallic stearate including the dispersal and mixing of the fine powder in a consumer or intermediate product.
  • suitable binder materials such as mineral oils, plasticizers, etc. or low melting waxes, fats, fatty acids, silicone oils, etc. Examples of suitable mineral oils with a viscosity in the range from 7 cst to 70 cst at 40°C; mineral oils with a viscosity in the range of 7 to 30 cst are known as light mineral oils.
  • suitable plasticizers include bis( 2-ethylhexyl )phthalate, bis.2-ethylhexyl )adipate , epoxidized soybean oil, epoxidized linseed oil, and diethylene glycol dipelargonate.
  • suitable waxes include waxes, such as paraffin wax and bayberry wax, having a melting point below 60° C.
  • suitable fatty acids include stearic acid, palmitic acid, oleic acid, lauric acid, and yristic acid; and suitable fats include those formed from such acids.
  • suitable silicone fluids include polydimethylsiloxanes having viscosities in the range from 10 to 10,000 cst, copolymers of di ethysiloxane and diphenylsiloxane , and copolymers of dimethylsiloxane and ethylphenylsiloxane.
  • the binder material is generally in the range from 0.5% to 20% by weight of the material being added to the blender 10.
  • the binder material is in the range from 1% to 10% by weight of the material forming the pellets, and most preferably, in the range from 2% to 4% by weight of the material in the pellets.
  • the blender 10 is a commercial blender apparatus suitable for blending dry powdery metallic salts of fatty acids with liquid or pliable solid materials in sufficiently large batch or continuous flow techniques suitable to produce the desired quantity of product.
  • the blender is operated in a manner to produce a homogeneous mixture of the binder material and dry powder metallic salt.
  • the mixed powder and binder material from the blender 10 is then fed to a pellet mill 12 which is also a conventional pellet mill selected for producing throughput at a rate sufficient to handle the desired quantity of product.
  • the output of the pellet mill is then passed through a sieve 14 where the product metallic powder pellets are separated from a residual powder fraction. Some of the material passing through the pellet mill will not be adequately pelletized or is subject to disintegration upon impinging upon the sieve 14. Such material is then recycled back to the feed hopper or entrance of the pellet mill 12 for further processing. Alternatively, the powder fraction from the sieve 14, or a portion thereof, can be recycled back to the blender 10 as shown in the dashed line.
  • powder metallic salts of Cia-Caa aliphatic monocarboxylic acids can be formed into pellets when binder materials are blended with the powder and the resulting blended material is passed through a pellet mill.
  • the blending and pelletizing is performed at temperatures well below the melting point of the powder metallic salt to avoid fusion of the powder.
  • Such pellets substantially eliminate the risk of producing hazardous dust conditions during handling and transport of the bulk powder material.
  • the powder pellets are subsequently passed to commercial blenders or mixing equipment in the formation of consumer products, the powder pellets readily disintegrate, due to the much greater stress applied by such blending and mixing equipment, so that the powder is dispersed and mixed in the same manner as if the powder material had not been formed into pellets.
  • Example 1 Mineral oil, ERVOL light, viscosity 24 to 26 cst at 40° C, white mineral oil, Witco Chemical, 40 g was added gradually to 2000 g Calcium Stearate HP Granular, Mallinckrodt, Inc., being blended in laboratory ribbon mixer model O-A, Paul 0. Abbe, Inc. The mixture was allowed to blend for about 20 minutes. The dry blend thus produced was transferred to the hopper of a laboratory pellet mill model CL-3, California Pellet Mill Company. The pellet mill was equipped with an L89 alloy steel 1/8" x 1/2" die and was operating at about 250 rpm. Dry blended calcium stearate/mineral oil was then fed from the hopper into the die cavity. Product was collected as it emerged out of the die.
  • a product mix containing pellets and powder was collected. It was sieved on a U.S. standard sieve No. 10 separating the pellets from the powder fraction. The fractions were by weight 56% pellets and 46% powder. The powder fraction was passed through the mill for a second time resulting in a total yield by weight of 74% pellets and 26% powder.
  • Pellets made in accordance with Example 1 were substituted for powder calcium stearate in the manufacture of a polyethylene resin. The pellets readily disintegrated in the blending apparatus and formed a homogeneous mixture of linear low density polyelylene which was equal to that normally formed using unpelletized powder calcium stearate.
  • Example 2 In the manner described in Example 1, unmodified Calcium Stearate HP Granular was fed to the pellet mill and the product collected. It consisted of 100% powdery material. Passing the product for a second time and then a third time through the pellet mill did not alter the physical form of the product collected which remained about 100% powder.
  • Example 3 In the manner described in Example 1, 4,000 g Calcium Stearate Standard, Mallinckrodt, Inc. was blended with 80 g 300 Plastics Oil, viscosity 48-60 cst at 40° C, Witco Chemical. After pelletizing the blend and sieving the product, the following fractions by weight were collected: pellets 64%, powder 36%.
  • Example 4 In the manner described in Example 1, 4,000 g Calcium Stearate Standard was blended with 160 g 300 Plastics Oil. After pelletizing the blend and sieving the product, the following fractions by weight were collected: pellets 94.5%, powder 5.5%.
  • Example 5 In the manner described in Example 1, 4,000 g Calcium Stearate Standard was blended with 160 g 300 Plastics Oil. After pelletizing the blend and sieving the product, the following fractions by weight were collected: pellets 94.5%, powder 5.5%. Example 5
  • Aluminum Stearate AX603, Mallinckrodt, Inc. contains about 3.5% of unreacted fatty acid. The material was fed to the pellet mill described in Example 1 and a mixture containing by weight 46% pellets and 54% powder was collected.
  • Example 6 Aluminum Stearate AX603, 550 g, was blended with 11.0 g mineral oil. The blend was then pelletized as described in Example 1. A mixture containing by weight 65% pellets and 35% powder was collected. Improvement in feeding rate, without jamming the mill, as well as in level of pellets produced resulted from the incorporation of mineral oil into the aluminum stearate. The integrity of the pellets produced in the above Examples 1-6 was ascertained by determining percentage of attrition, i.e. powder produced, in a 50 g sample tumbled at 30 rpm minutes as shown in the following Table I. Tests were run using a PHARMA TEST instrument type PTFR D6452 manufactured in Hainbury, West Germany. Following the 30 minutes test period the sample was transferred to a U.S. standard sieve No. 16. The fraction of sample passing through the screen was determined. The higher that fraction, the weaker the pellets. The following results were obtained:

Abstract

On forme des pastilles de poudre de sels métalliques en mélangeant de la poudre de sels métalliques d'acide monocarboxylique aliphatique, avec une matière de liaison capable de lier la poudre de sels métalliques dans des conditions normales de manipulation et de transport en vrac, sans altérer les propriétés d'utilisation terminale de la poudre de sels métalliques, et en passant la composition mélangée dans un moulin (12) à pastilles. On peut manipuler et transporter les pastilles de poudre de sels métalliques avec des risques de production de poussière dangereuse très réduits, et une désintégration facile dans un appareil classique d'amalgame et de mélange afin qu'elles se dispersent de manière similaire à de la poudre de sels métalliques ne se présentant pas sous la forme de pastilles.
PCT/US1989/002767 1988-06-27 1989-06-23 Pastilles d'acides gras metalliques WO1990000083A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US21232088A 1988-06-27 1988-06-27
US212,320 1988-06-27

Publications (1)

Publication Number Publication Date
WO1990000083A1 true WO1990000083A1 (fr) 1990-01-11

Family

ID=22790513

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US1989/002767 WO1990000083A1 (fr) 1988-06-27 1989-06-23 Pastilles d'acides gras metalliques

Country Status (3)

Country Link
AU (1) AU3961889A (fr)
CA (1) CA1326859C (fr)
WO (1) WO1990000083A1 (fr)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL133881C (fr) * 1966-03-15
US3321425A (en) * 1959-05-23 1967-05-23 Vinypal S A Vinyl chloride polymers containing fatty acid and fatty acid salts
DE2124040A1 (en) * 1971-05-14 1972-11-23 Sakai Kagaku Kogyo K.K., Sakai, Osaka (Japan) Complex stabilizer for a chlorine - contg resin - contains lead and calcium stearate
GB1346082A (en) * 1971-04-16 1974-02-06 Sakai Chemical Industry Co Method of producing granular stabilizers for chlorine-containing vinyl resins
US4446086A (en) * 1981-10-30 1984-05-01 Envirostrand, Inc. Process and apparatus for extruding stabilizers
EP0169382A2 (fr) * 1984-06-25 1986-01-29 The B.F. GOODRICH Company Procédé pour granuler des matériaux poudreux et produits obtenus

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3321425A (en) * 1959-05-23 1967-05-23 Vinypal S A Vinyl chloride polymers containing fatty acid and fatty acid salts
NL133881C (fr) * 1966-03-15
GB1346082A (en) * 1971-04-16 1974-02-06 Sakai Chemical Industry Co Method of producing granular stabilizers for chlorine-containing vinyl resins
DE2124040A1 (en) * 1971-05-14 1972-11-23 Sakai Kagaku Kogyo K.K., Sakai, Osaka (Japan) Complex stabilizer for a chlorine - contg resin - contains lead and calcium stearate
US4446086A (en) * 1981-10-30 1984-05-01 Envirostrand, Inc. Process and apparatus for extruding stabilizers
EP0169382A2 (fr) * 1984-06-25 1986-01-29 The B.F. GOODRICH Company Procédé pour granuler des matériaux poudreux et produits obtenus

Also Published As

Publication number Publication date
CA1326859C (fr) 1994-02-08
AU3961889A (en) 1990-01-23

Similar Documents

Publication Publication Date Title
US4235794A (en) Method for the manufacture of metal soap granulates
EP0223539B1 (fr) Agents retardateurs de flamme granulaires, leur procédé de préparation, méthode et matériaux obtenus
JP2001502375A (ja) 金属顔料成分
EP0296552B1 (fr) Liant pour métaux et composition de moulage
DE202010017705U1 (de) Flüssige Formulierung
US5028486A (en) Metallic fatty acid pellets and method of manufacture
US4092187A (en) Process for coating crystalline high explosives
EP0052693B1 (fr) Procédé de fabrication de corps en verre expansé
DE60128128T2 (de) Metall und metalloxyd enthaltendes granulat und verfahren zur herstellung
DE19823999A1 (de) Verfahren zur Herstellung pyrotechnischer Anzündsätze
WO1990000083A1 (fr) Pastilles d'acides gras metalliques
US3668144A (en) Dust-free lead stabilizer for synthetic resins
JPS6341509B2 (fr)
JPH0689362B2 (ja) 粉末冶金用鉄基粉末混合物の製造方法
JP3316243B2 (ja) 粉末シリカの高分散性造粒物及びその製造方法
US3883363A (en) Friable composition and process
EP0020156A2 (fr) Composition explosive pulvérulente sensible aux amorces
DE4241902A1 (fr)
CA1120628A (fr) Poudre d'aluminium ne produisant pas de poussiere et dispersible dans l'eau
JPH06256763A (ja) 粒状難燃剤組成物
JPH0242375B2 (fr)
JPS5937296B2 (ja) 迅速分散性を有する塩素含有重合体用粒状安定剤の製法
US8557066B1 (en) Method for forming energetic nanopowders
AU633134B2 (en) Continuous process for preparation of aqueous dispersions of metal soaps
USH925H (en) Encapsulated signal illumination flare composition

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AU JP

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE CH DE FR GB IT LU NL SE